Part 2 of 2, Rev. 00 to WCAP-15996-NP, Technical ...

Table G.A: Dictionary Listing

Index Long Variable Name Input System System System Variable's Tyxe Dimen- Definition ." Units

No._. Opuut Alt. 1 Alt. 2 Function slons 1144 RCSCONCPART Output RCS Solutes RE 50 RCS Node particulates concentrations. This parameter array is Microcure/lbm

-Int both a CENTS calculated output and a USER adjusted Input. For instance, particulate conc. = 0.0 at initialization. After Initialization, RCS_CONCPART(I) = 0.0. If the USER wanted to adjust the particulates in any or all nodes, then RCSCONCHYD (I) could be re-established at x mIcroC/lbm. CENTS would then calculate any changes to x as the given transient progressed, thus reverting RCSCONCPART to an output role affected by transport of the particulate and releases from the core damage model. Reference 1, Sections 4.15 and 5.8.2.

1145 RCSPCONCXEN Output! RCS Solutes RE 50 RCS Node xenon concentrations. This parameter array Is both a Microcune/Ibrn

-Int CENTS calculated output and a USER adjusted input. For instance, Xenon conc. = 0.0 at initialization. After initialization, RCSCONCXEN(I) = 0.0. If the USER wanted to adjust the Xenon in any or all nodes, then RCS_CONCXEN(I) could be reestablished at x microClIbm. CENTS would then calculate any changes to x as the given transient progressed, thus reverting RCSCONCXEN to an output role affected by transport of the Xenon and releases from the core damage model. Reference 1, Sections 4.15 and 5.8 2.

1146 RCSRELESOLU Output RCS Solutes RE 50, 5 RCS Node solute accumulation rates. Reference 1, Sections 4.15 Composite -_-_and 5 8.2. 1 Units

1147 RCS-RELE.SOLU.CORE Partition RE 5 Core solute releases. 1-5 Bo,Hy,lo,Ce,Xe Composite _ - - -Units

1148 COREBORONREL Input RE Core boron release. This is a fictitious quantity. Must be set = 0 0 Composite Units

1149 COREHYDREL I/O CORE RCS Solutes RE Core hydrogen release. This input parameter is not required for Lbm/sec code initialization. If POWZRH20_NYZIR=True (User flag: Zr oxidation calculation is performed) then this variable is set to the calculated H2 release rate, POWZRH20_H2M. If POWZRH20_NYZIR=False, then this variable can be set by the USER to simulate different core clad failure analyses

1150 COREJIODREL Input CORE RCS Solutes RE Core Iodine release. This input parameter is not required for code Microcude/sec initialization. This Is a USER defined input parameter which simulates a certain amount of core damage. Once released into node 1, the iodine is then distributed & tracked through the system by CENTS. Reference 1. Sections 4.15, 7.1.3 & 7.2.7.

1151 COREPARTREL Input CORE RCS Solutes RE Core particulate (cesium) release. This input parameter is not Microcurie/sec required for code initialization. This Is a USER defined Input parameter which simulates a certain amount of core damage. Once released into node 1, the particulate Is then distributed & tracked through the system by CENTS. Reference 1, Sections 4.15, 7.1.3 &

17.2.7.

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Index Long Variable Name Inout/ System System System Variable's TVye Dimen- Definition " - Units , No. Output Alt. 1 Alt. 2 Function sions '

1152 CORE.XENREL Input CORE RCS Solutes RE Core xenon release. This input parameter Is not required for code Microcurie/sec initialization. This is a USER defined input parameter which simulates a certain amount of core damage. Once released into node 1, the Xenon is then distributed & tracked through the system by CENTS. Reference 1, Sections 4.15, 7.1 3 & 7.2.7.

1153 RCSDOSE VARIABLES Partition RE 20 Dose Model variables Partition 1154 RCSDOSE_INIT_IOD Input DOSE RCS Solutes RE Dose Model Initial RCS Iodine Conc. This input is scenario Microcune/Ibm

dependent, entered by the code USER. It defines the initial Iodine concentration In all the RCS nodes, collectively. Note that after initialization, the iodine concentration in all nodes will be RCSCONC_IOD(I) = RCSDOSEINITIOD. At that point individual node(x) concentration can be adjusted by USER modification of RCS_CONC_IOD(x). Reference 1, Section 5.8.2 and Appendix D.

1155 RCSDOSEFLASH Input DOSE RCS Solutes RE Dose model flashing factor flag. This USER defined input Dimensionless apportions the iodine entering the SG from the RCS during a tube leak, by allocating the fraction of iodine to the steam space of the SG, with the remainder going to the liquid in the SG secondary. RCS_DOSE_FLASH=O.O is best-estimate, 1.0 is conservative, and 2 0 is most conservative. Reference 1, Section 7.3.5.

1156 RCS_DOSE_BF Input DOSE RCS Plant Design RE Dose model breathing factor. This is a USER supplied input. Note FTW/sec that the units are normally in m3 /sec and require conversion to ft3

/sec. Reference 1, Section 7.3 5. 1157 RCS_DOSE_CF Input DOSE RCS Plant Design RE Dose model conversion factor. This a plant independent variable, Rem/Cune

which converts the units of iodine released to the atmosphere from curies to REM. Reference 1, Section 7 3 5.

1158 RCSDOSEXOQ2 Input DOSE RCS Plant Design RE Dose model 2Hr site dispersion factor. This is a plant dependent sec/FT' Input based upon the documented weather patterns at a given utility. It accounts for the iodine dispersion into the atmosphere from the release point to the site boundary, during the first 2 hrs after the release. It is used in determining 2 hr dose rates. Reference 1, Section 7 3 5.

1159 RCSDOSE_XO08 Input DOSE RCS Plant Design RE Dose model 8hr site dispersion factor. This is a plant dependent sec/FT'3

input based upon the documented weather pattems at a given utility. It accounts for the iodine dispersion into the atmosphere from the release point to the site boundary, during the first 2 hrs after the release. It is used in determining 2 hr dose rates. Reference 1, Section 7.3.5.

1160 RCS_DOSE_CONT_LEAK Input DOSE RCS Plant Design RE Dose Model Containment Leak Rate. This is a USER defined input. FracJday It is used by the code to calculate the iodine being released to the

I _atmosphere via the containment Reference 1, Section 7.3 5.

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Table G.A: Dictionary Listine

Index Long Variable Name, Input/ System System System Variable's Type Dlmen- Definition, ,,,- ,, , UnI , v..,No. .. - Output Alt. 1 Alt. 2 Function - slons,

1161 RCSDOSECONDDF Input DOSE RCS Plant Design RE Dose Model Turb & cond Decontamination Factor. This Is a USER Dimensionless defined input which indicates the scrubbing capability of the turbine and condenser to remove Iodine. 1/RCSDOSECONDDF is the fraction of Iodine going the turbine & condenser which would escape to the atmosphere. Reference 1, Section 7.3.5.

1162 RCS.DOSETOTCURIE Output DOSE RCS RE Dose Model Total Curies of Iodine affecting offsite doses, released Curies

from all sources. This is a CENTS calculated output MSLHIOINTATM+MSLH_IO_CONT_INT_LEAK +(MSLH_10_INT_COND+MSLHI0_INTTURB)*RCSDOSECO _NDDF. Reference 1, Section 7.3.5.

1163 RCSDOSE 2HR Output DOSE RCS RE Dose Model Total 2 Hour DOSE Accum. This Is the CENTS REM calculated 2 hr dose = RCS..DOSE_TOT_CURIE * RCS_DOSECF * RCSDOSEBF - RCSDOSE_XO02. Reference 1, Section 7.3.5.

1164 RCSDOSE_8HR Output DOSE RCS RE Dose Model Total 8 Hour DOSE Accum. This is the CENTS REM calculated 8 hr dose = RCSDOSE_TOT_CURIE * RCSDOSECF * RCSDOSEBF- RCS.DOSE_X008. Reference 1, Section 7.35.

1165 RCSPASTVALUES Partition RE 651 Retained variables from last execution Partition

1166 ENGY STM LAST Output RCS T/H State RE 50 RCS node steam energy at last time step Btu

1167 ENGYTOTLAST Output RCS T/H State RE 50 RCS node total energy at last time step Btu

1168 MASSLIQLAST Output RCS T/H State RE 50 RCS node mass of liquid at last time step Lbm

1169 MASSSTM LAST Output RCS T/H State RE 50 RCS node mass of steam at last time step Lbm

1170 MASS BUB-LAST Output RCS T/H State RE 50 RCS node mass of bubbles at last time step Lbm

1171 MASS TOT LAST Output RCS T/H State RE 50 RCS node total mass at last time step Lbm

1172 PRES LAST Output RCS _ T/H State RE 50 RCS node pressures from last execution Psia

1173 ENTH LIQ LAST Output RCS T/H State RE 50 RCS node liquid enthalples from last exec. BtuAbm

1174 ENTH STMLAST Output RCS T/H State RE 50 RCS node steam enthalpIes from last exec. Btu/lbm

1175 ENTHLIOSATLAST Output RCS T/H State RE 50 RCS node saturated liquid enthalpy, last step BtuAbm

1176 PFLOWLAST Output RCS T/H State RE 150 RCS path flow rates at last time step Lbm/sec

1177 RCS-COREFLASHLAST Output RCS T/H State RE Core flashing rate at last execution Lbm/sec

1178 RCSSTATUS Partition RE 156 Variables associated with RCS abort Partition

1179 FATALINPUT ERROR Output RCS Flag LO RCS model abort on input data error(s) True False

1180 FATAL._OUTPUT ERROR Output RCS Flag LO RCS model abort on calculation error(s) True False

1183 MASS BUBSPRED Output RCS T/H State RE 50 Predicted bubble masses for path props. Lbm

1185 RCSSEARCHITER Output RCS IN 50 Number of iterations In pressure search. Counts

1186 RCSSEARCH TYPE Output RCS Flag IN 50 Pressure search used. Pointer

1187 CORESURFAREALAST Output R0CS T/H State RE Vessel flow area at two-phase boundary. Ft2

1188 RCS VALVES Partition RE 25 Variables associated with RCS valves Partition

1189 RCS.VLVLAREA Partition RE 25 RCS valve areas _Fte

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Index Long Variable Name Input/ System System System Variable's Tvve Dlmen- Definition Units No. Output Alt. 1 Alt. 2 Function _ slons 1190 AREAVALVEUHEAD Output RCS Dimension RE 3 Array of upper head vent valve areas. This array Is a CENTS Ft2

calculated output. The 1st valve in the array is the vent to containment. The next two are the vent(s) to the OT. Related variables are vlv_uhead_cont & vlv._uheadqt, which are inputs setting the valves' fraction open. Other related vanables are pltvlvarea-uheadcont & pit vvarea-uhead-qt, which are the "full open" valve areas.

1191 AREA-VALVEPRZR Output PZR RCS Dimension RE 15 Array of presssurizer relief valve areas. This array is a CENTS Ft2 calculated output. The first 4 valves in the array are the PORVs, the next 4 valves are for PSVs, the third set of 4 are for PORV MOV block valves, next is the vent valve to containment and the last two are for vents to the OT. Related variables are vlv.przr.porv, vlvjprzr..safety, vlv...przr..mov, vlv_przrcont & vlv_przrqt, which are inputs setting the valves' fraction open for those valves without controllers(vents & MOVs) and outputs dictated by controller function for the PORVs and PSVs. Other related variables are pIt vlvarea.przr-porv, pl~tvlvarea_przr._safety, plt~vlvareaprzrmov, pltvlvarea-przr..cont & pltvlvarea_.przr._qt, which are the "full open" valve areas.

1192 AREAVALVE.SPRAY Output PZR RCS Dimension RE 2 Array of presssurizer main spray valves. This array is a CENTS Ft2 calculated output. Related variables are vlv-przrj.mspray, which are outputs dictated by controller action the valves' fraction open. Other related variables are plt...vlvarea_.przrnmspray, which are the "full open" valve areas and vlv..przr..mspraysig which are set by the controllers, if in auto, or by the USER, if the control system is In

_manual. 1193 AREAVALVEQT Output PZR RCS Dimension RE 3 Array of quench tank valve areas. This array is a CENTS calculated Ft2

output. The 1st valve in the array is the vent from the QT to GWS. the 2nd valve is the vent to containment and the last is the nitrogen supply valve. Related variables are vlvqtgws, viv._qLcont & vlv._uheadnsupply, which are inputs setting the valves' fraction open. Other related variables are pltyvlvarea.qLgws, plLvlvarea.qLcont & plt vivarea.qt-nsupply, which are the "full open" valve areas. Note that the OT model Is normally deactivated for safety analysis events by setting MODOFFQT = T or by zeroed inputs.

1194 RCSMALFUNCTION Partition RE 30 Malfunction flags and variables Partition 1198 P_AREALEAK Output RCS RE 17 Leak flow path areas. This is the CENTS calculated output array of Fet

leak flowpath areas generated from USER supplied input cues as to the size and source of the leaks. Reference 1, Section 7.5.1.

1199 RCS PRZRFLOW VALVES Partition T/H State RE 10 Pressurizer valves flow Partition 1200 RCSPFLOWPORV Output PZR RCS T/H State RE 4 PORVs mass flow rate. This plant independent output variable is Lbm/sec

always used, as long as RCSNUMPORVS > 0. Flow is based on system differential pressures across the valve, fluid conditions at the

I I_ _valve and valve opening.


Table G.I: Dictionary Listing

Index Long Variable Name InDut System System System Variable's T ype Dimen- Definition -2 - , .Units No. Output Alt. 1 Alt. 2 Function sions

1201 RCS_P_FLOW_SAFETY Output PZR RCS T/H State RE 4 Pressurizer safety valves mass flow rate. This plant Independent Lbm/sec output variable is always used. Flow is based on system differential pressures across the valve, fluid conditions at the valve and valve opening.

1202 PFLOWPRZRCONT Output PZR RCS T/H State RE Pressurizer to containment vent flow rate. This is a scenario Lbm/sec dependent output, based on system differential pressures across the valve, fluid conditions at the valve and valve opening.

1203 RCS_P_FLOWPRZROTi Output PZR RCS OT T/H State RE Pressurizer to quench tank vent flow rate. This Is a scenario Lbm/sec dependent output, based on system differential pressures across the valve, fluid conditions at the valve and valve opening. Note that the OT model must be "on' (MODOFFQT=F) for any flow to exit the pressurizer via these vents.

1204 RCPCOMMON Partition RE 100 Coolant pump model global common Partition

1205 RCP INTERNAL Partition RE 88 Pump model Internal variables Partition

1206 RCP_ELECTRIC Partition RE 28 Coolant pump motor electrical vanables Partition

1207 RCPVOLT Output RCP RCS Pump Prop. RE 4 Pump motor input voltages. This Output variable is set through Volts rcpivoltfrac * rated bus voltage. It is always used In determining pump motor parameters. Reference 1, Section 4.11

1208 RCPFREQ Output RCP RCS Pump Prop. RE 4 Pump motor electrical frequencies. This output mirrors the Input Hertz parameter rcp-jreqjrated. It is always used in determining pump motor parameters.

1211 RCPSLIP Output RCP RCS Pump Prop. RE 4 Coolant pump motor slip. Reference 1, Section 4.11 Fraction 1213 RCP_-MECHANICAL Partition RE 40 Coolant pump mechanical variables Partition

1214 RCPTJORQ_HYD Output RCP RCS Pump Prop. RE 4 Coolant pump hydraulic torques. This output parameter is always Ft-lbf used. Reference 1, Section 4.11

1215 RCP_TORQELEC Output RCP RCS Pump Prop. RE 4 Coolant pump electrical torques. This output parameter Is always Ft-lbf used. Reference 1, Section 4.11

1216 RCPTORQFRIC Output RCP RCS Pump Prop RE 4 Coolant pump friction torques. This output parameter is always Ft-lbf used. Reference 1, Section 4.11

1217 RCPHEAT Output RCP RCS T/H State RE 4 Coolant pump fluid heat rates. This output parameter is always Btu/sec used. Reference 1, Section 4.11

1218 RCPVIBR Output RCP RCS Pump Prop. RE 4 Coolant pump vibrations G's vibration

1219 RCPSPEEDPUMP Output RCP RCS Pump Prop. RE 4 Coolant pump impeller speed. This output parameter Is always Radians/seco I used. Reference 1, Section 4 11 nd

1220 RCPSPEED_MOTOR Output RCP RCS Pump Prop. RE 4 Coolant pump motor speed. This output parameter Is always used. Radians/seco Reference 1, Section 4.11 nd

1221 RCP VIBR AMP Output RCP RCS Pump Prop. RE 4 Pump vibration amplitude at rated speed G's vibration

1222 RCP_SPEED_DERIV Output RCP RCS Pump Prop. RE 4 Coolant pump speed derivatives Composite Units

1223 RCPMALFUNCTION Partition RE 12 Coolant pump malfunction variables Partition 1227 RCP RCS LEAK Partition RE 4 RCP seals leak partition Partiion


Table G.1: Dictionary Listing

Index Lona Variable Name inoUt System System System Variable's Typ Dlmen-!! Definition Units-' No. Output Alt. 1 Alt. 2 Function slons -__

1228 RCPSEALS.LEAK Input RCP RCS T/H RE 4 RCP seals leakage rated cond. This variable Is set in the basedeck GaVmln Dimension for normal RCP seal leakage. Rcp-sealsileak is set to a nominal

value of x.x gpm/pump This is the difference between the nominal steady state charging and letdown. For accident conditions, it can be set by the USER to any desired leakrate. Reference 1, Table 7.25

1229 RCS OPTIMIZATION Partition RE 820 RCS optimization partition Partition

1230 RCS NSTEP CALCULATIONS Partition RE 160 Partition vars updated every n steps Partition

1231 RCSICOUNTMUKPRP Output RCS IN Counter mu-k-Pr calculations. CENTS counts the number of time Counts steps since the last recalculation of properties. This output indicates the number of time steps since the last recalculation.

1232 RCSNUM_MUKPRP Input RCS Model IN Number steps between each mu-k-Pr calculation. This Is the Counts Design maximum number of time steps that the RCS model may execute

before forcing a recalculation of the kinematic properties. This was introduced into CENTS in order to save execution time. If this is no longer a concern, then continuous recalculation of properties is

I__ II preferable (RCSNUMMUKPRP = 1).

1233 RCS_P_VISCOS Output RCS T/H State RE 100 RCS momentum path liquid viscosity. This kinematic parameter is Lbm/ft-sec calculated every RCSNUMMUKPR_P time steps, except every

_time step if the RCS pressure changes very rapidly.

1234 RCSPCONDUCT Output RCS T/H State RE 100 RCS momentum path liquid conductivity. This kinematic parameter Btu/sec-ftis calculated every RCS._NUMMUKPR_P time steps, except every degF time step if the RCS pressure changes very rapidly.

1235 RCSP_.PRANDTL Output RCS T/H State RE 100 RCS momentum path liquid Prandti number. This kinematic Dimensionless parameter is calculated every RCS_NUMMUKPRP time steps, except every time step if the RCS pressure changes very rapidly.

1236 RCSJCOUNTFLOWLIMP Output RCS Flag IN Counter for critical flow calculations. CENTS counts the number of Counts time steps since the last recalculation of cntical flows in the momentum paths. This output indicates the number of time steps since the last recalculation.

1237 RCS_.NUMFLOWLIMP Input RCS Model IN Number of time steps between each momentum paths cntical flow Counts Design calculation. Used when the input flag RCSCRIT_FLOWCHECK

is True. This is the maximum number of time steps that the RCS model may execute before forcing a recalculation of the critical flows for choking check in the RCS momentum paths.

1238 RCS MORE VARIABLES A Partition RE 153 RCS-more variables A Partition

1239 RCS MORE VARIABLESI Partition RE 20 RCS more variables partition I Partition

1242 RCSPRZlCONTIHEATMULT Input PZR RCS Multiplier RE Multiplier on wall heat transfer from the pressurizer to containmenL Dimensionless This is a scenario dependent input, available to the code USER to vary the heat loss from the pressunzer to containment. This multiplier would be applied to N HEATXFERCONT.

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Index Long Variable Name Input System System System Variable's Type Dimen- Definition Units. '7 No., Output Alt. 1 Alt. 2 Function slons "

1243 CHT_H_SUPER_MULT Input RCS Multiplier RE Supercritical heat transfer coefficient multiplier. Used always. Used Dimensionless in conjunction with CHT_PRESS_SUPERCRIT, which is the "supercdtical pressure" for the purpose of calculating heat flux. When vessel pressure exceeds this value (typically 2700 psla), CENTS does the following: (1) it forces the heat transfer mode to be in "forced convection", even if other conditions call for the "pool boiling" mode, and (2) it calculates the heat flux coefficient as CHT H SUPERMULT - CHTjHTCOF._SUB, where the latter is the calculated heat transfer coefficient to subcooled liquid. These parameters are independent of plant design.

1244 CHTHEATFRAC Output CORE RCS T/H State RE Total core heat transfer to coolant, as a fraction of the total power Fraction _rating.

1254 RCSPRZR_FLASH_TAU Input PZR RCS T/H RE Time constant for pressurizer flashing. It Is always used. Fraction Dimension It is a time constant for flashing In the pressurizer The flashing rate

is calculated when the pressure drops. Then, the flashing rate is lagged with a small time constant in order to assure stability In a process that will otherwise responds Instantaneously to pressure fluctuations.

This variable is independent of plant design.

1255 RCSUHEADCONTHEAT MULT Input RCS Multiplier RE _ Multiplier on upper head heat loss to containment. Dimensionless 1256 RCS_CRIT_MODEL Input RCS Flag IN LIq/2-phs choked flow model: O=HEM, 1 =HF. This plant Pointer

independent, scenario dependent flag Is normally set to Homogeneous Equilibrium Flow model. This choke flow correlation provides the best representation for steam or two phase flow from the PSVs. If a SBLOCA or SGTR is simulated the USER may consider switching to Henry-Fauske flow model for depicting sub_cooled critical flow.

1257 RCS MORE_VARIABLES II Partition PZR_ RE 28 RCS more variables partition ii -- Partition

1258 RCSSPRAYEFF Output PZR RCS RE Spray efficiency, calculated based on the local conditions. Fraction 1259 RCSSPRAY_EFFMULT Input PZR RCS Multiplier RE Spray efficiency multiplier. This plant independent variable is Dimensionless

normally set to 1.0 For testing or tuning purposes the user may wish to adjust this variable to achieve more or less rate of change in pressurizer pressure during spray flow situations.

1260 RCSLEFFSPR Input PZR RCS T/H RE 2 Levels for spray efficiency calculation. The absolute values for this Feet Dimension variable Is dependent upon the height of the spray nozzle head

within the pressurizer. By running sensitivity cases on various CE plant models, the spray efficiency varies from nil to full efficiency at levels approximately 0 0 to 5 0 ft below the spray nozzle.

_ Reference: Plant Basedeck Calculation, Hand Calc. #8.

1261 RCS"TSURGEfTAU Input PZR RCS T/H RE Time constant for surge line temperature. Always used, but only for Dimensionless Dimension calculating the simulator output TEMPPRZR.SURGE, which is not

referenced anywhere else in CENTS. Usually set to a small value [7_ _ _ 1_ _ (1 to 2 sec.), it Is Independent of plant design. I



Index Long Variable Name Input System Svstem System Variable's Type Dimen- Definition Units

No, -. IOutput Alt. 1 Alt 2 Function .. slons

1279 RCSSPRAYPRESDEG Input PZR T/H LO Sprays pressure dependent degradation. Used always, in True False

Dimension conjunction with RCSSPRAYPDEG_TERM & RCSSPRAY_DELHJERM, as long as the pressurizer is in thermal nonequilibrium and there Is pressurizer main spray flow. CENTS determines a spray condensation efficiency based on

steam height, steam pressure and subcooling of the liquid inventory.

CENTS calculates three efficiency factors for those three effects. The spray condensation rate is then given by the standard condensation formulation multiplied by all three factors. If

RCS_SPRAYPRESDEG is True, the efficiency factor due to pressure Is: RCSSPRAY_PDEG_TERM + (1. RCS_SPRAY_PDEGTERM) * PRESS(I)/1000. bounded by the range [0.05, 1.0]. If the flag is False, then there Is no low-pressure

induced degradation, I.e. the factor Is 1.0. The efficiency factor due to subcooling introduces degradation of the condensation due to spray when the pressurizer's liquid inventory Is close to saturation -L.e., within RCSSPRAY_DELHDEG (Btu/lbm) of the saturation line. The efficiency factor Is: (ENTH_SLIQAT(l) - ENTHLIO(l)) I RCS_SPRAYDELHDEG bounded by the range [0 0, 1.0]. If RCSSPRAYDELH-DEG is zero, then there is no degradation near the saturation curve. The flag RCSSPRAY_PRESDEG Is a

model flag, used to disable the calculation for testing purposes It is independent of plant design. This flag should always be True during realistic transients. RCSSPRAY_PDEG_TERM is a model constant which has been found to work best when set to 0 0. It Is independent of plant design. RCS_SPRAY_DELHDEG is a model constant which has been found to work best when set to 5.0

_ BtuAbm. It is Independent of plant design.

1280 RCSSPRAY.EFF2 Output PZR RE Spray efficiency term, calculated as a condensation degradation Fraction

term at low pressure.

1282 RCSQUALMINNE Input RCS T/H RE Minimum quality for non equilibrium calculation. Used always. To Fraction

Dimension be considered for thermal nonequilibrium, a node must contain both

liquid and steam. That Is, the quality must be less than 1.0 and greater than RCS_QUAL_MIN_NE. RCSQUALMINNE should

be set to a small number (1.E-3 to 1.E-2), but not zero. (A value of

0 0 may send the node into nonequilibrium with just a miniscule

amount steam present, and the condensation model may then condense more steam than is available, causing a pressure spike.). IRCSQUAL_MINNE is Independent of plant design.



Index Lona Variable Name Input System System System Variable's Typ~ Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

1293 RCS_PRZRJREFTAU Input PZR RCS T/H RE 2 Pressurizer reference leg time constants. Used to calculate a Seconds Dimension temperature that is used only in an instrument signal to the

simulator panels The temperature of the pressurizer's reference leg is dnven by the local containment temperature, by applying a lag function to the temperature, with the lag being RCS_PRZR_TREF_TAU(1) if the leg temperature is decreasing and RCS_PRZRTREFTAU(2) if it is increasing The temperature, TEMPPRZRREF, determines the enthalpy, density, liquid column head in the leg, and the instrument pressure difference. The latter is LEVLPRZR_DP. None of those quantities are used anywhere else in CENTS, but LEVLPRZR_DP is sent to a simulator instrument display. NOTE: The vanables for instrument-calculated measured level, CTL_PRZR_ILEVEL and CTLPRZR_LEVEL_INST are used by the CENTS control system, but are calculated in a separate algorithm. They are not affected by RCS PRZR TREF TAU

1295 RCS MORE VARIABLES IIIB Partition RE 4 RCS more variables IliA Partition

1297 RCS PRZR LEVEL Output PZR RCS T/H State RE RCS pressunzer level (inch from ref.leg bot) Inches

1298 RCS MORE VARIABLES-IV Partition RE 10 RCS more variables IV Partition

1300 RCS_PRZR_DT_SUBC Input PZR RCS T/H State RE Pressurizer delta-temperature for flashing Used in conjunction with Del-DegF RCS_PRZR_DT_SUBH, RCS_PRZR_LVLDT_SUBC(2), and RCS_PRZR_TAUDTSUB. See RCS PRZR DT SUBH for a full description.

1302 RCPDELSPEED_LOCKED Input RCP RCS Component RE RCP locked rotor delta speed (rad/sec). Used only during a Radians/seco Design "locked RCP rotor' malfunction transient, during the time that the nd

pump shaft speed decelerates to zero. This variables specifies the rate at which the pump speed decelerates, in rad/sec per time step. I e, at each time step, subprogram RCP does: RCP_SPEEDPUMP = AMAX1 (RCRPSPEEDPUMP RCP_DELSPEEDLOCKED, 0.0). Since the rate of pump shaft deceleration is impossible to predict in a locked-rotor situation, the value of RCPDELSPEEDLOCKED just needs to be reasonable. It is therefore independent of plant design

1303 RCPFRICCOEFF Input RCP RCS Component RE RCP windage and fnction coefficient. This variable is defined as the Composite Design (pump friction torque)/(motor speed [in radians/sec] 2 ) Units

1307 RCSITERDPL Input RCS RE Dp for convergence at low pressure(equilibrium). Used whenever Psig the system pressure is below 200 psia. This is a convergence critenon for the iterative pressure search. I.e , the solution converges when the pressure change from the last iteration is less than RCSITERDPL It is used whenever a node's pressure is below 200 psia AND the node is in equilibrium. (At higher pressures in equilibrium, the convergence dP Is RCSITERDP, and In nonequilibrium it is RCSJTER_DP_NE.). This parameter is numerical in nature, and is independent of plant design. Reference 1, Section 4.4

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Index Long Variable Name - - n System System System Variablefs Type Dlmen- Definition', ' -. Units.

No. .,.Output Aft. 1 AIL 2 Function slons

1309 RCS MOREVARIABLESV Partition RE 8 RCS more variables V Partition

1313 RCS_PRZRMASSSTM Output PZR RCS RE Pressurizer steam mass Lbm

1314 RCSPRZRMASSAIR Output PZR RCS RE Pressurizer air mass Lbm

1315 RCS-MORE-VARIABLES-VI Partition I RE 14 RCS more variables VI Partition

1320 RCSWPRZRCONT Output PZR RCS RE Mass flow from pressunzer to containment. Lbm/sec

1321 RCSWPRZROT Output PZR RCS RE Mass flow from pressurizer to quench tank (valves). Lbm/sec

1322 RCS PRZRQUALRELIEF Output PZR RCS Initial Cond. RE Pressurizer relief valve flow quality. Fraction

1327 RCSPRZRFRACAIR Output PZR RCS Initial Cond. RE Air mass fraction in pressurizer. Fraction

1328 RCSPRZRKHSTM Input PZR RCS Initial Cond. RE K for enthalpy degradation of the heat transfer coefficient of steam. Dimensionless Used always, in conjunction with RCS-PRZRKP_STM. These are

parameters for the degradation function used in calculating steam condensation on the pressurizer wall. The condensation heat transfer Is calculated based on the various physical parameters (temperatures, steam height, air fraction, heat transfer coefficients),

and is then multiplied by a degradation: 1 - (1 - RCSPRZRKHSTM) * (2250 - PRESS) / (2250 RCSPRZRKPSTM), where PRESS is steam pressure, and the degradation is limited to (0,1]. Typical values for these parameters are KH--0.2 and KP--0.0, respectively, independently of plant design.

1329 RCSPRZRKPSTM Input PZR RCS Initial Cond. RE K for pressure degradation of the heat transfer coefficient for steam. Psia Used always, in conjunction with RCSPRZRKH_STM. These are parameters for the degradation function used in calculating steam condensation on the pressurizer wall. The condensation heat transfer is calculated based on the various physical parameters (temperatures, steam height, air fraction, heat transfer coefficients), and is then multiplied by a degradation: 1 - (1 - RCSPRZRKHSTM) * (2250 - PRESS) / (2250 RCSPRZR_KPSTM), where PRESS is steam pressure, and the degradation is limited to [0,1]. Typical values for these parameters are KH=0.2 and KP=0 0, respectively, independently of plant _design.

1330 RCSMoRE.VARIABLES 504_SR Partition RE 58 RCS more variables partition Partition

1332 RCS PRZRDTSUBBOIL Input PZR RCS T/H RE Pressurizer delta-temperature for boiling. Used always. Del-DegF

Dimension RCSPPRZR_DTSUBBOIL is the amount of subcooling (degF) above which all boiling/flashing ceases and below which the surface condensation stops, In the pressurizer. (See RCSPRZRDTSUBH, RCSPRZRDTSUBC).

1333 RCSRCPVOIDF Output RCP RCS T/H State RE 4 RCP void fraction Fraction

1337 RCS_PRZRCONDSURF Output PZR RCS T/H State RE Pressurizer steam condensation on liquid surface. Lbm/sec

1338 RCSPRZRLEVL LAST Output PZR RCS T/H State RE Pressurizer level last step Feet

1339 RCS PRZRTWALL Output PZR RCS T/H State RE 2 Pressurizer walls temp. 1:hiq, 2: stm Degree F

1340 RCSPRZR 0 CONT Output PZR RCS T/H State RE 2 Pressurizer walls heat to containment Btu/sec

G-112WCAP- 15996-NP, Revision 0

Table G.I: Dictionary Listingi

Index Lona Variable Name input System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function sions

1341 RCS_PRZRQAXWALL Output PZR RCS T/H State RE Pressurizer walls axial heat transfer. This output variable is the Btu/sec heat transferred from the wall region exposed to steam to that exposed to liquid (as determined by the water level at the last time step).

1342 RCS_PRZR_DT_SUBSS Output PZR RCS T/H State RE Pressurizer measure of subcooling to start boiling, in a steady-state Del-DegF mode

1343 RCSPORING Output RCS T/H State RE Inner 0-ring region pressure. If the o-ring has not failed, then Psia pressure is the minimum of the core node & upper head nodal pressures x rtrv._head seal_mult, set by the USER. If the 0-ring has failed (reached RCSORINGFAIL=T, where pressure at the oring is .ge. RCS_P_ORING_FAIL set by the USER), then RCSPORING is the maximum of the(failure pressure) and (the minimum pressure in the upper head and core nodes)

1344 RCSORING_FAIL Input RCS Flag LO Vessel O-nng failure flag. CENTS sets to true when pressure in True False both the core and upper head nodes are .ge. the USER set failure pressure, RCSP_ORING FAIL. Otherwise it is always False

1347 RCSRCP SVOL Output RCP RCS T/H State RE 4 Specific volume in the flow path going through each RCP. Ft3Abm 1354 RCSFAILURESTATUS Partition LO 3 RCS failure status partition Partition 1356 RCS_STEPJAILURE Output RCS Flag LO RCS step failure flag Indicates failure of the flow solution matrix True False

inversion 1358 RCS TIME CONTROL Partition RE 45 Time control partition Partition 1359 RCSTIME SCALE Output RE Time scale for RCS Dimensionless 1362 RCSDELTA T Output RE RCS integration delta t Seconds 1390 RCSMODOUTPUTS Partition RE 60 RCS model global common outputs Partition 1396 RCS MOD OUTPUTS CORE Partition RE 3 CS outputs to 1 -D core Partition 1397 CHTTCOOLAV Output CORE RCS T/H State RE Core coolant average temperature Degree F 1398 CHT SVOLCOOL AV Output CORE RCS T/H State RE Core coolant average specific volume Ft3 Abm 1399 RCS BORON CORE Output CORE RCS Solutes RE Core node boron concentration Parts/million 1400 RCS_MOD_OUTPUTSCHT Partition RE 53 RCS outputs to Core Heat Transfer. These are copies of the values Partition

I_ calculated in the RCS models 1401 RCSCHT PRESS Output CORE RCS T/H State RE Core node pressure Psia 1402 RCS CHT ENTHLIQ Output CORE RCS T/H State RE Core node liquid enthalpy Btu/lbm 1403 RCSCHT ENTHSTM Output CORE RCS T/H State RE Core node steam enthalpy BtuAbm 1404 RCSCHT QUAL Output CORE RCS T/H State RE Core node quality Fraction 1405 RCSCHT FLOWIN Output CORE RCS T/H State RE Core node inlet flow (total minus bypass) Lbm/sec 1406 RCSCHTENTHIN Output CORE RCS T/H State RE Core node inlet enthalpy Btu/Ibm 1407 RCSCHT QUALIN Output CORE RCS T/H State RE Core node Inlet quality Fraction 1408 RCS CHT LEVMIX Output CORE RCS T/H State RE _ Core node mixture height Feet 1409 RCS CHT LEVSAT Output CORE RCS T/H State RE Core node saturation line height Feet 1410 RCSCHTOWALL Output CORE RCS T/H State RE _Core node lower plenum wall heat Btu/sec 1411 RCSCHT TWALL Output CORE RCS _ T/H State RE _ Core node lower plenum wall temperature Degree F 1412 RCS CHT MASSLIQ Output CORE RCS T/H State RE _ Core node liquid mass Lbm



Index Long Variable Name- ,, Input/ System System System Variable's, Type Dimen- Definition .. , Units_ No• . , • .'-.• "IOutput Alt. 1 Alt. 2 Function slons

1413 RCSCHTMASSBUB Output CORE RCS T/H State RE 22 RCS bubble mass in core (sections) Lbm 1414 RCS_MODINPUTS Partition RE 205 RCS modified inputs Partition

1415 RCSMODJNPUTSBOP Partition RE 50 RCS modified inputs from BOP systems Partition

1416 CHGS_RCSFLOW Output RCS CVCS T/H State RE 4 Charging system flows (RCS connections). This output parameter Lbmnsec from the charging system model supplies the flow from the charging system to the RCS. In the absence of a detailed CVCS model, this flow Is calculated by the Control System model.

1417 CHGS_RCS_ENTH Output RCS CVCS T/H State RE Charging system enthalpy (RCS connection). This output Btu/Ibm parameter from the charging system model supplies the enthalpy of flow from the charging system to the RCS. In the absence of a detailed CVCS model, this enthalpy is calculated by the Control System model.

1418 CHGSRCS-BORON Input / RCS CVCS Solutes RE Charging system boron concentration (RCS connection). In the Partstmillion Init absence of a detailed CVCS model, this parameter is set =RBINIT

dunng INITIALization, and then remains constant, unless changed by the USER during a transient.

1419 CHGSRCSHYD Input I RCS CVCS Solutes RE Charging system hydrogen concentration (RCS connection). In the Lbm/lbm Init absence of a detailed CVCS model, this parameter is set =0 0

during INITIALization, and then remains constant, unless changed by the USER during a transient.

1420 CHGS_RCS_IOD Input / RCS CVCS Solutes RE Charging system iodine conc (RCS connection). In the absence of Mlcrocurlellbm Init a detailed CVCS model, this parameter Is set =0.0 during

INITIALization, and then remains constant, unless changed by the I USER during a transient.

1421 CHGSRCSPART Input / RCS CVCS Solutes RE Charging sys particulate cone (RCS connection). In the absence of Mlcrocurle/Ibm Init a detailed CVCS model, this parameter is set =0 0 during

INITIALization, and then remains constant, unless changed by the USER during a transient.

1422 CHGSRCSXEN Input I RCS CVCS Solutes RE Charging system xenon conc (RCS connection). In the absence of Mlcrocurie/lbm Init a detailed CVCS model, this parameter Is set =0 0 during

INITIALIzation, and then remains constant, unless changed by the _USER during a transient.

1423 CHGS.ASPRAY-FLOW Output RCS CVCS TIH State RE Auxiliary spray flow rate. In the absence of a detailed CVCS model, Lbm/sec _this flow Is calculated by the Control System model.

1424 LDNSRCSFLOW Output RCS CVCS T/H State RE 4 Letdown system flow (RCS connections). This output parameter Lbm/sec from the CVCS model indicates the flow to the letdown line from the RCS. In the absence of a detailed CVCS model, this flow Is calculated by the Control System model.

1425 RCW_RCSFLOW Input RCS RCW TIH State RE 1 Drain flow to waste system (RCS connection). In the absence of a Lbm/sec RCW model, this parameter remains constant, unless changed by

_the USER during a transient. I



Index Long Variable Name Input/ System System System Variable's Type Dimen- Definition Units No Output Alt. 1 AIt. 2 Function slons 1426 SDCRCSFLOW Input / RCS T/H State RE 2 Shutdown cooling out-flow (RCS connection). In the absence of a Lbm/sec

Ind detailed SDC model, this parameter is set --0.0 during INITIALization, and then remains constant, unless changed by the USER during a transient

1427 SIS_RCSFLOW Output RCS SIS TiH State RE 8 SIS flows (RCS connections) This output parameter from the SIS Lbm/sec model indicates the flow from the SI lines to the RCS. This flow for each SI line is the combination of the HPSI, LPSI and SIT flow contributions.

1428 SIS_RCS_ENTH Output RCS SIS T/H State RE 8 SIS enthalpy (RCS connectons). This output parameter from the Btu/lbm SIS model indicates the enthalpy of flow from the SI lines to the RCS. This enthalpy is calculated from the inputs CTLHLPSI_H and CTLSISSITH, weighted by the flow rates from each source (HPSI, LPSI and SITs)

1429 SIS_RCSBORON Output RCS SIS Solutes RE 8 SIS boron concentration (RCS connection). This output parameter Parts/million from the SIS model indicates the boron concentration of flow from the Si lines to the RCS. This boron concentration is calculated from the inputs CTLHLPSI_BC and CTLSIS_SITfBC, weighted by the flow rates from each source (HPSI, LPSI and SITs).

1430 SITANKFLOW Output RCS SIS T/H State RE 4 Safety injection tank flow. This output parameter from the SIS Lbm/sec model indicates SIT flow based upon relative RCS and SIT pressures, flow area, k factors, etc. When added to HPSI and LPSI flow rates, this output becomes a part of SIS RCS FLOW

1431 RCSMODINPUTS VLVCONTR Partition RE 30 RCS mod inputs from valve controllers Partition 1432 VLV RCS_POS Partition Valves RE 24 RCS valve positions (fraction) Fraction 1433 VLVUHEADCONT Input UH RCS Valves Hardware RE Upper head to contain valve position. This input parameter is set by Fraction

Vent State the USER to vent the upper head of the RV to the containment This vent path may be used anytime, though its primary intent is for use during shutdown, cooled down conditions

1434 VLV_UHEAD_QT Input UH RCS Valves Hardware RE 2 Upper head to quench tank valve position. This Input parameter is Fraction Vent State set by the USER to vent the upper head of the RV to the quench

tank. This vent path may be used anytime, though its primary intent is for use during shutdown, cooled down conditions. It requires that the quench tank inputs be developed for a given plant basedeck and the OT model is "on' (MOD OFF QT=F).

1435 VLV_PRZR_PORV Output PZR RCS Valves Hardware RE 4 Pressunzer PORV position In Automatic mode, the position is Fraction State determined by the controller logic, which sets the valve signal as a

function of pressunzer pressure, and operates the valve. In Manual mode, the USER sets the PORV signal via VLVPRZRPORVSIG, and the model operates the PORV accordingly.

1436 VLVPRZRSAFETY Output PZR RCS Valves Hardware RE 4 Pressurizer safety valves position This parameter is determined Fraction State by the PSV controller for each safety valve as a function of the

I____ I__ I•_ I pressurizer pressure and the PSV setpoints. _



Index Long Variable Name Input/ System System System Variable's ]Type Olmen. Definition , - . -, Units. No. Output Alt. 1 Alt. 2 Function ;slons __ ___

1437 VLVPRZRMOV Input PZR RCS Valves Hardware RE 4 Pressurizer Motor-Operated Valve positions, In series with the Fraction State PORVs. This valve position is normally set to 1.0 if PORVs are

modeled. If set to any other position < 1.0, each valve will partially or completely Isolate Its PORV.

1438 VLVPRZRCONT Input PZR RCS Valves Hardware RE Vent valve position, pressurizer to containment. This Input Fraction State parameter Is set by the USER to vent the pressurizer to the

containment. This vent path may be used anytime, though Its _pnmary intent is for use during shutdown, cooled down conditions.

1439 VLVPRZROQT Input PZR RCS OT Hardware RE 2 Pressurizer to quench tank vent valves position. This Input Fraction State parameter Is set by the USER to vent the pressurizer to the quench

tank. This vent path may be used anytime, though ts primary intent Is for use during shutdown, cooled down conditions. It requires that the quench tank inputs be developed for a given plant basedeck and the OT model Is "on" (MODOFFOT=F).

1440 VLV_PRZR_MSPRAY Output PZR RCS Valves Hardware RE 2 Main spray control valves. This parameter provides valve position Fraction State information. In Automatic mode, the position is determined by the

controller logic, which sets the valve signal as a function of pressurizer pressure, and operates the valve. In Manual mode, the USER sets the spray valve signal via VLVPRZRMSPRAY._SIG, and the model operates the spray valve accordingly.

1441 VLVQT_GWS Input PZR RCS OT Hardware RE Quench tank to GWS vent valve position. This Input is required iff Fraction State the quench tank inputs are developed for a given plant basedeck

and the OT model is *on" (MODOFF OT=F). 1442 VLVQT_CONT Input PZR RCS OT Hardware RE Quench tank to containment vent valve position. This Input Is Fraction

State required iff the quench tank Inputs are developed for a given plant I_ basedeck and the QT model is "on" (MODOFFQT=F).

1443 VLV_QTNSUPPLY Input PZR RCS OT Hardware RE Nitrogen supply to WTank valve position. This input is required iff Fraction State the quench tank inputs are developed for a given plant basedeck

land the QT model is "on" (MODOFFOT=F). %

1444 VLVRCSSIG Partition RE 6 RCS valve signals Partition

1445 VLV_PRZRMSPRAYSIG I/O PZR RCS Control Sig RE 2 Pressurizer main spray valve signals. Calculated by the Control Fraction System in Auto mode. Set by the user or remain constant in Manual mode.

1446 VLVPFRZR_PORVSIG I/O PZR RCS Control Sig RE 4 Pressurizer PORV signals. Calculated by the Control System In Fraction Auto mode. Set by the user or remain constant in Manual mode.

1447 RCSMODINPUTSVOLTCONTR Partition RE 20 RCS mod Inputs voltage controllers Partition

1448 PRSIHEATERVOLTFRAC Output PZR RCS Heater Prop RE 6 Pressurizer heaters voltage (fraction). Calculated by the Control Fraction System.

1449 RCPI-VOLT FRAC Input RCP RCS Pump Prop. RE 4 RCP voltage (fraction). Set by USER to 00 to trip RCP. Fraction

1450 RCSHEATERVOLT-BUS Input PZR RCS RE 6 Heater bus voltages. This is the Input which dictates the full bus Volts voltage available for each heater bus.

1451 RCPI_ FREQFRAC Input RCP RCS RE 4 RCP electric motor frequency (fraction) Fraction

1452 RCSMODINPUTS MALFUNCTIONS Partition RE 52 RCS modified malfunctions Partition

1453 MAL SB LOCA Input RCS RE 4 Small break LOCA areas Ft2



Index Lona Variable Name Input/ System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

1454 MAL LB LOCA Input RCS RE Large break LOCA area Ft2

1455 MALSGTR Input RCS RE 4 SG tube rupture (SGTR) indicator - number of ruptured tubes. For Pointer each tube ruptured, there are two broken ends CENTS treats these two ends as separate breaks, with different flow enthalpies and flow fluxes, and with each presenting a break area SG_TUBEAREA * RCS_SGTR_FLOWMULT. Reference: CECES-0198-P, Rev 004, Section 8

1457 MALROD_EJECT Input RCS RE Rod ejection plus CEDM rupture (fraction of the area Fraction P_AREARODEJ). This creates a SBLOCA without the reactivity effect, which can be done separately.

1458 MAL_RCS_VALVE Input RCS Valves Malfunction RE 25 RCS valves malfunction. This partition/array of malfunction valve Fraction Partition positions is used to fail-open the valves The resulting valve area

used in the calculation is the greater of PLT_RCS_VLVAREAO ) VLVRCS_POS()

and PLT RCSVLVAREA() * MAL RCS VALVE() 1459 MALVLVUHEADCONT Input UH RCS Valves Malfunction RE Upper head to containment fail-open malfunction valve position. Fraction

Vent The valve area used in the calculation is the greater of, PLT_VLVAREA_UHEADCONT * VLV_UHEAD_CONT

and PLT VLVAREA UHEAD CONT *MAL VLV UHEAD CONT 1460 MALVLVUHEADOT Input UH RCS Valves Malfunction RE 2 Upper head to quench tank fail-open malfunction valve position Fraction

Vent The valve area used in the calculation is the greater of: PLTVLVAREAUHEADQT * VLVUHEADQT

land PLT VLVAREA UHEADQT *MAL VLVUHEAD OT 1461 MAL_VLV_PRZR_PORV Input PZR RCS Valves Malfunction RE 4 Pressurizer PORV fail-open malfunction valve position. The valve Fraction

area used in the calculation is the greater of: PLT_VLVAREA_PRZR_PORV * VLV_PRZRPORV

and PLT_VLVAREA PRZR PORV *MAL VLV PRZR PORV 1462 MALVLVPRZRSAFETY Input PZR RCS Valves Malfunction RE 4 Pressunzer safety valves fail-open malfunction valve position. The Fraction

valve area used in the calculation is the greater of: PLT_VLVAREA_PRZR_SAFETY - VLV_PRZRSAFETY

and PLT VLVAREA PRZR SAFETY * MAL VLV PRZR SAFETY 1463 MAL_VLV_PRZR_MOV Input PZR RCS Valves Malfunction RE 4 Pressurizer MOV fail-open malfunction valve position. The valve Fraction

area used in the calculation is the greater of. PLT_VLVAREA_PRZR_MOV * VLVPRZRMOV

and PLT VLVAREA PRZR MOV* MAL VLV PRZR MOV 1464 MALVLVPRZRCONT Input PZR RCS Valves Malfunction RE Pressurizer to containment vent valve fail-open malfunction valve Fraction

position The valve area used in the calculation is the greater of: PLT_VLVAREAPRZR_CONT * VLVPRZRCONT

and PLT VLVAREA PRZR CONT * MAL VLV PRZRCONT 1465 MALVLV_PRZRQT Input PZR RCS OT Malfunction RE 2 Pressurizer to quench tank vent valves fail-open malfunction valve Fraction

position The valve area used in the calculation is the greater of. PLT_VLVAREAPRZR_QT * VLVPRZRQT

and PLTVLVAREAPRZR_QT * MAL VLV_PRZRQT



Index Long Variable Name Input/ System System System Variable's , T Dlmen- Definition Units No.__=. : Outt, ut Alt. 1 Alt. 2 Function slons

1466 MAL_VLV_PRZRMSPRAY Input PZR RCS Valves Malfunction RE 2 Main spray control valves fail-open malfunction valve position. The Fraction valve area used in the calculation is the greater of:

PLTVLVAREAYPRZRMSPRAY - VLV_PRZR_MSPRAY and PLTYLVAREAPRZRMSPRAY 'MAL VLV PRZRMSPRAY

1467 MALVLV.QTGWS Input PZR RCS OT Malfunction RE Quench tank to GWS vent valve fail-open malfunction valve Fraction position. The valve area used in the calculation Is the greater of:

PLT_VLVAREA_QT_GWS * VLV_QTGWS and PLT_VLVAREA_QT_GWS * MAL_VLV_QTGWS

1468 MAL_VLV_QT_CONT Input PZR RCS QT Malfunction RE Quench tank to containment vent valve fail-open malfunction valve Fraction position. The valve area used in the calculation is the greater of:

PLTVLVAREAQTCONT - VLV-_QT_CONT -,

_and PLT-_VLVAREA-QT1CONT * MAL_VLVQTCONT 1469 MALVLVQT_NSUPPLY Input PZR RCS QT Malfunction RE Nitrogen supply to QTank valve fail-open malfunction valve position. Fraction

The valve area used in the calculation Is the greater of: PLTLVLVAREAQTNSUPPLY * VLV._QT._NSUPPLY

and PLTJVLVAREA-QTLNSUPPLY * MALVLV_QT_NSUPPLY

1470 MAL RCP SHAFTBREAK Input RCP RCS Malfunction LO 4 RCP shaft break malfunction True False

1471 MAL.RCPLOCKED Input RCP RCS Malfunction LO 4 RCP locked rotor malfunction True False

1474 RCSMOD INPUTS CONT Partition RE 2 RCS modified inputs from containment Partition 1475 CONT PRES Input RCS RE Containment pressure Psia

1476 QT MOD INPUTS Partition RE 5 Quench tank modified Inputs Partition

1477 DMW_QTFLOW Input PZR RCS RE Demineralized water flow to quench tank. This Input is used iff the Lbm/seoc quench tank inputs are developed for a given plant basedeck and the OT model is "on" (MODOFFQT=F).

1478 DMWOT_ENTH Input PZR RCS RE Demineralized water enthalpy. This Input is used iff the quench Btu/Ibm tank inputs are developed for a given plant basedeck and the OT model Is "on" (MOD_OFF QT=F).

1479 RCW_QT_FLOW Input PZR RCS RE Mass flow QT to RCW. This input Is used iff the quench tank Lbm/sec Inputs are developed for a given plant basedeck and the QT model is "on" (MODOFFQT=F).

1480 GWS_QT_PRES Input PZR RCS RE GWS pressure. This Input Is used iff the quench tank Inputs are Psia developed for a given plant basedeck and the OT model Is "on" (MODOFFQT=F).

1481 GWS_QTFLOW Input PZR RCS RE Gas flow quench tank to GWS. This input Is used iff the quench Lbm/sec tank inputs are developed for a given plant basedeck and the QT model is "on" (MODOFFQT=F). I

1482 RCSINPUTS PRZR RELIEF Partition RE 33 Pressurizer relief valves discharge model Partition

WCAP-15996-NP, Revision 0 G-1 18


Index Lonq Variable Name - Input System Systen. System Variable's . Type Dimen- Definition -. Un.ts.. .

No. Output Ait. 1 Alt. 2 Function slons '2

1486 VLV_PRZR_FLOWTABLE Input PZR RCS Przr RE 15 Pressurizer relief valve flow table: dependent variable. Used when Undefined

Relief the relief flow quality > VLV_PRZRQUALDF and VLV\IPRZR_FLOWOPTION = 2 or 3:

2 - A Bemouli formulation for orifice type flow Is applied

independently of throat pressure. It Is multiplied by a discharge

coefficient Cd that is given by this table VLV_PRZR_FLOW_TABLE (Cd) vs. VLV_PRZR_PROPTABLE (subcooling, DegF). 3 - The flux is given directly by this table of VLVPRZRFLOWTABLE (flux, Ibmlsec-ft2) vs. VLV_PRZR_PROPTABLE (upstream pressure, Psla).

The table contains VLVPRZRNPOINTSTAB points.

1487 VLVPRZRPROPTABLE Input PZR RCS Przr RE 15 Pressunzer relief valve flow table: independent variable. Used Undefined

Relief when the relief flow quality > VLV_PRZR_QUALDF and VLVPRZRFLOWOPTION = 2 or 3

2 - A Bemouli formulation for orifice type flow is applied independently of throat pressure. It is multiplied by a discharge

coefficient Cd that Is given by the table VLVPRZR_FLOW_TABLE (Cd) vs. this table VLV_PRZRPROPTABLE (subcooling, DegF).

3 - The flux is given directly by the table of VLV_PRZR_FLOW_TABLE (flux, Ibm/sec-ft2) vs. this table VLV_PRZR_PROPTABLE (upstream pressure, Psla).

The table contains VLVPRZRNPOINTSTAB points.

1488 RCSINITIALCONDITIONS Partition I RE 15 RCS initial conditions Partition

1489 RPINIT Input RCS Initialization RE New initial pressunzer pressure (psla, in steam space). This Is a Psla

case dependent variable set by the USER to determine the initial conditions. CENTS uses this input as one of the required parameters to initialize the code. It Is used in conjunction with

RLINIT(pressurizer level), RWINIT(RCS total flow), RTCLIN(RCS cold leg temperature), RBINIT(RCS initial boron concentration), kfrain(initial power fraction), SLINIT(SG water level), CTL_FWS_.H(initial FW enthalpy). These variables dictate the initial

T/H conditions required by CENTS to calculate an overall plant heat

and flow balance. Reference 1, Appendix D.

1490 RLINIT Input RCS Initialization RE New Initial pressurizer level (feet, actual level). This Is a case Feet

dependent variable set by the USER to determine the initial

conditions. CENTS uses this input as one of the required parameters to Initialize the code. It Is used in conjunction with

RPINIT(pressurlzer pressure), RWINIT(RCS total flow), RTCLIN(RCS cold leg temperature), RBINIT(RCS Initial boron

concentration), kfrain(initial power fraction), SLINIT(SG water level),

CTL_FWS_H(initial FW enthalpy). These variables dictate the Initial T/H conditions required by CENTS to calculate an overall plant heat

I _ land flow balance. Reference 1, Appendix D. .... )_n

WCAP-1599o-iNI, Revision u U'L•U


Index Long Variable Name Input System System System Variable's Tiype Dimen- Definition ., Units No. Output Alt. 1 Alt. 2 Function slons° - _ _ _ _ _ _ _

1499 RCS_SG_SECTDH Input RCS SG Model RE Tolerance for SG node saturation hysteresis. Typical value = 10.. BTU/LbM Design Used in switching logic for number of sections. In positive, single

phase flow, the requested number of sections from NUMSG-SECT is used. However, in two-phase or reverse flow, the code reduces the number of sections to 1 per node, since the sectioning scheme is not guaranteed to match the overall nodal state under those conditions. Thus, as an example, if each of 4 tube nodes had 10 sections in the sectioning scheme, the number of sections comprising the entire tube length of each SG can vary between 4 and 40. The actual (dynamic) number of sections employed in each node is stored In the array RCS_SG_NSECT. The switching logic Is that the number of sections collapses to one per node if that node reaches saturation enthalpy. It stays at one section unless the node becomes subcooled by at least the value of RCSSGSECT_DH. Usually the User will make this value sufficiently large to keep the node from erratic switching in the number of sections. Reference 1, Section 5.3.

1500 RCSSGSECT_DW Input RCS SG Model RE Tolerance for SG node flow hysteresis. Used In switching logic for Lbm/sec Design number of sections. Typical value = 2000. In positive, single-phase

flow, the requested number of sections from NUMSGSECT is used. However, in two-phase or reverse flow, the code reduces the number of sections to 1 per node, since the sectioning scheme is not guaranteed to match the overall nodal state under those conditions. Thus, as an example, if each of 4 tube nodes had 10 sections In the sectioning scheme, the number of sections comprising the entire tube length of each SG can vary between 4 and 40. The actual (dynamic) number of sections employed in each node is stored in the array RCSSGNSECT. The switching logic is that the number of sections collapses to one per node if that node's fluid flow reverses direction. It stays at one section unless the node flow Increases to the value of RCSSG_SECT_DW. Usually the User will make this value sufficiently large to keep the node from erratic switching in the number of sections. Reference 1, Section

15.3

1501 RCS_SG_SECTLH Output RCS SG T/H State LO 16 State of SG node saturation hysteresis. Used In switching logic for True False number of sections. Reference 1, Section 5.3.

1502 RCS_SGSECT_LW Output RCS SG T/H State LO 16 State of SG node flow hysteresis. Used in switching logic for True False number of sections. Reference 1, Section 5 3.



Index Lona Variable Name Input System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

1503 RCSSGSECTTEMP Output RCS SG T/H State RE 20, 8 Primary coolant temperatures of tube sections. Note: The (20,8) Degree F dimensions are interfaces to the SGS model The second dimension is keyed to SG "sides". Each SG has 2 "sides" - a hot side and a cold side - for up to 4 steam generators. The order of the second dimension is: SG #1 hot side, SG #1 cold side, etc. The first dimension is the RCS node sections, with the pair of vertically stacked nodes being lumped into a single column of up to 20 sections. The order of the first dimension is bottom to top Reference, Reference 1, Sections 5 3 and 7 3 2

1504 RCS_SGSECTQP Output RCS SG T/H State RE 20, 8 Primary side heat transfer rates of tube sections Note: The (20,8) Btu/sec dimensions are interfaces to the SGS model. The second dimension is keyed to SG "sides". Each SG has 2 "sides" - a hot side and a cold side - for up to 4 steam generators The order of the second dimension is: SG #1 hot side, SG #1 cold side, etc. The first dimension is the RCS node sections, with the pair of vertically stacked nodes being lumped into a single column of up to 20 sections. The order of the first dimension is bottom to top Reference Reference 1, Sections 5 3 and 7.3.2.

1505 RCS_SGSECTQS Output RCS SG T/H State RE 20, 8 Secondary side heat transfer rates of tube sections. Note: The Btu/sec (20,8) dimensions are interfaces to the SGS model. The second dimension is keyed to SG "sides". Each SG has 2 "sides" - a hot side and a cold side - for up to 4 steam generators. The order of the second dimension is: SG #1 hot side, SG #1 cold side, etc. The first dimension is the RCS node sections, with the pair of vertically stacked nodes being lumped into a single column of up to 20 sections The order of the first dimension is bottom to top Reference: Reference 1, Sections 5 3 and 7 3 2.

1506 RCSSGSECT_-TTUBE Output RCS SG T/H State RE 20, 8 Tube metal temperatures of tube sections Note: The (20.8) Degree F dimensions are interfaces to the SGS model. The second dimension is keyed to SG "sides". Each SG has 2 "sides" - a hot side and a cold side - for up to 4 steam generators. The order of the second dimension is. SG #1 hot side, SG #1 cold side, etc. The first dimension is the RCS node sections, with the pair of vertically stacked nodes being lumped into a single column of up to 20 sections. The order of the first dimension is bottom to top. Reference- Reference 1, Sections 5 3 and 7 3 2.

1507 RCSSGSECTPRESS Output RCS SG T/H State RE 20, 8 Primary pressures of tube sections Note: The (20,8) dimensions Psia are interfaces to the SGS model. The second dimension is keyed to SG "sides". Each SG has 2 "sides" - a hot side and a cold side for up to 4 steam generators. The order of the second dimension is. SG #1 hot side, SG #1 cold side, etc. The first dimension is the RCS node sections, with the pair of vertically stacked nodes being lumped into a single column of up to 20 sections. The order of the first dimension is bottom to top. Reference 1, Sections 5 3 and

1 1_732



Index Long Varable Name Input System System System Variable's Tyej DImen- Definition - Units

No. ___--______Output AIL t - Alt. 2 Function, sons

1508 SGSNSECT Output RCS SG T/H State IN 8 Number of sections in each SG side (I e. hot side & cold side). If Counts there are four tube nodes per SG, then the two hot side nodes' sections are added together and the two cold side nodes' sections

are added together for each SG. Reference 1, Section 5.3.

1509 RCSSGSECTTOPT Input RCS SG Model IN Optional primary temperature model for heat transfer. 0 => Exit Pointer

Design temp. 1 => LMTD-based temperature. The 0 option is included to allow the previous code model to be duplicated. Usually, the USER

will choose LMTD based temperature as the most realistic representation of the fluid temperature. For Option 1 (LMTD) TEMPI = TSEC + (Tim - Ti) / in [(Tim - TSEC) / (Ti - TSEC)], where,

TEMPI = Mean temperature of section i; TSEC = Temperature of the SG evaporator region; Tim = Temperature at bottom of section; "lTi = Temperature at top of section. Reference 1, Section 5.3.

1510 RCSSGSECTENTH Output RCS SG T/H State RE 11, 16 Section-bottom enthalples (section.node). Reference 1, Section 5.3. Btu/'bm

1511 SGTR DATA Partition RCS SG SGTR 28 Data for SGTR Model

1512 SGTR TUBELENGTH Input RCS SG SGTR RE 8 SGTR tube length. 2 values per generator. The first value is for the Feet hot side, the second for the cold side. Reference 1, Section 5.7 and 7.5.

1513 SGTRJTUBEENTRANCEK Input RCS SG SGTR RE 8 SGTR Entrance K factor. Normally set to 0.5. Provide 2 values per Dimensionless

steam generator. The first value is for the hot side, the second for the cold side. Reference 1, Section 5.7 and 7.5..

1514 SGTRBREAKELEV Input RCS SG SGTR RE 4 SGTR elevation above tube sheet. Provide 1 value per steam Feet

generator. Reference 1, Section 5.7 and 7.5.

1515 SGTR SLOTBREAKOPT Input RCS SG SGTR LO 4 SGTR Option to calculate SGTR break flow using a slot break flow Dimensionless model rather than double ended guillotine break. Reference 1,

Section 5.7 and 7.5.

1516 SGTRSLOTBREAK AREA Input RCS SG SGTR RE 4 SGTR Slot area per tube, used only when the flag FtA2

SGTRSLOTBREAKOPTION is true. Reference 1, Section 5.7

and 7.5.

1517 SB LOCAPIPEDATA Partition RCS SBLOCA RE 20 Data for SBLOCA pipe loss model Partition

1518 SBPIPEAREA Input RCS SBLOCA RE 4 SBLOCA pipe flow area between RCS and break. Reference 1, FtA2

Section 4.21.2 and 7.5.

1519 SBPIPELOD Input RCS SBLOCA RE 4 SBLOCA pipe length/diameter from RCS to break. Reference 1, Dimensionless

-__-_•_Section 4 21.2 and 7.5.

1520 SB1PIPE-KGEOM Input RCS SBLOCA RE 4 SBLOCA pipe geometric loss k-factor from RCS to break, excluding Dimensionless

entrance loss Reference 1, Section 4.21.2 and 7.5.

1521 SBYPIPE-KENT Input RCS SBLOCA RE 4 SBLOCA pipe entrance loss k-factor at the RCS connection. Dimensionless

Reference 1, Section 4.21.2 and 7.5.

1522 SBDELTAELEV Input RCS SBLOCA RE 4 SBLOCA break elevation above RCS connection Reference 1, Feet

-_ _Section 4.21.2 and 7.5.

1523 CVCSDATA Partition RCS CVCS Piping Def RE 50 CVCS model data Partition

1524 LDNPIPEDATA Partition RCS CVCS Piping Def RE 20 Input data for letdown line loss model. Reference 1, Section 4.21.1 Partition

and 7.5. 1_____


Table G.I: Dictionary Listing Index Long Variable Name Input System System System Variable's Type Dlmen- Definition Units

No. Output AIt. 1 Alt 2 Function sions 1525 LDN_PIPEAREA Input RCS CVCS Piping Def RE 2 Letdown line flow area FtA2

(1) = line from RCS to regenerative heat exchanger (RHX) (2) = line from RHX to the break, if any Reference 1, Section 4.21.1 and 7 5

1526 LDNPIPELOD Input RCS CVCS Piping Def RE 2 Letdown line length/diameter. Dimensionless

(1) = line from RCS to regenerative heat exchanger (RHX) (2) = line from RHX to the break, if any. Reference 1, Section 4.21.1 and 7 5

1527 LDN_PIPEKGEOM Input RCS CVCS Piping Def RE 2 Letdown line geometric loss factor, excluding entrance losses. Dimensionless

(1) = line from RCS to regenerative heat exchanger (RHX) (2) = line from RHX to the break, if any.

Reference 1, Section 4 21 1 and 7 5 1528 LDNPIPEKENT Input RCS CVCS Piping Def RE 2 Letdown line entrance loss k-factor. Dimensionless

(1) =at RCS connection (2) = at entrance to regenerative heat exchanger. Reference 1, Section 4 21 1 and 7.5.

1529 LDNPIPE_DELTAELEV Input RCS CVCS Piping Def RE 2 Letdown line elevation rise Feet (1) = line from RCS to regenerative heat exchanger (RHX) (2) = line from RHX to the break, if any Reference 1, Section 4 21 1 and 7 5

1530 MALLDNBREAK Input RCS CVCS Break RE Letdown line break area FtA2

When MALLDNBREAK > 0, the break is located in the letdown line downstream of the regenerative heat exchanger (RHX) When MALLDNBREAK < 0, the break is located in the first letdown line upstream of the RHX. (The number of active letdown lines from the RCS to the RHX is RCS NUMOUTLDNS < 4) Reference 1, Section 4 21 1 and 7 5

1531 CVCSRHXDATA Partition RCS CVCS State RE 30 CVCS model calculated data Partition 1532 CVCSRHXTLDN Output RCS CVCS State RE 2 Letdown temperature at regenerative heat exchanger (1) inlet DegreeF

1 1 _ (2) exit. 1533 CVCSRHXTCH Output RCS CVCS State RE 2 Charging temperature at regenerative heat exchanger (1) inlet DegreeF

(2) exit 1534 CVCS RHX HLDN Output RCS CVCS State RE 2 Letdown enthalpy at regenerative heat exchanger (1) inlet (2) exit BtuAbm 1535 CVCS RHX HCH Output RCS CVCS State RE 2 Charging enthalpy at regenerative heat exchanger (1) inlet (2) exit BtuA/bm 1536 CVCS RHX WLDN Output RCS CVCS State RE Letdown mass flow rate Lbrn/sec 1537 CVCS RHX WCH Output RCS CVCS State RE Charging mass flow rate Lbm/sec 1538 CVCSRHXHEAT Output RCS CVCS State RE Regenerative heat exchanger heat load Btu/sec 1539 LDNRCS ENTH Output RCS CVCS State RE 4 Enthalpy at letdown line RCS connections BtuAbm 1540 LDN_RCS_PRES Output RCS CVCS State RE 4 Pressure at letdown line RCS connections Psia 1541 SGSCOMMON Segment RE 1536 SG secondary global common variables Segment 1542 SGS INTERNAL Partition RE 400 SG secondary internal variables Partition 1543 SGS BOT P Output SG T/H State RE 4 Fluid pressure at SG tube sheet Psia



Index Long Variable Name, Input System System System Variable's Type Dlmen- Definition . ... ,Unts

,No.- . Output AIlt1 Alt. 2 Function slons

1544 SGS CON 101 Output SG Solutes RE 4 SG steam node Iodine concentration Microcude/Ibm 1545 SGS-CON 102 Output SG Solutes RE 4 SG evaporator and downcomer nodes iodine concentration Microcude/lbm 1546 SGSCONPT1 Output SG Solutes RE 4 SG steam node particulates concentration Microcurle/lbm 1547 SGS CON PT2 Output SG Solutes RE 4 SG evaporator and downcomer nodes particulates concentration Microcure/lbm 1548 SGSCON_XE1 Output SG Solutes RE 4 SG steam node xenon concentration Microcudeflbm 1549 SGS_CON XE2 Output SG Solutes RE 4 SG evaporator and downcomer nodes xenon concentration Microcudeflbm 1550 SGSCONBORONi Output SG Solutes RE 4 SG steam node boron concentration Parts/million 1551 SGSCONBORON2 Output SG Solutes RE 4 SG evaporator and downcomer nodes boron concentration Parts/million 1552 SGS_DELTV Input SG Model RE 4 Multiplier on steam velocity. This is an adjustment multiplier on the Dimensionless

Design calculated steam separation velocity in the steam generator evaporator. It Is a tuning factor available to tune for steady state, but is normally not used for this purpose. This Is an array of tuning factors, independent of plant design. SGS DELTV should normally be 1.0.

1553 SGSDP Output SG T/H State RE 3, 4 Level Instrum. delta press (refleg, sg) Psid

1554 SGSDVDP Output SG T/H State RE 4 Slope of volume(pressure) curve. Used always, and recalculated Feet3/ Psi always. This Is the slope of the volume-vs-pressure curve, used in the steam generator Iterative pressure solution. It is used as the initial guess for the slope, and is recalculated dynamically during the iterative solution. The Initial slope will have no effect on the

____solution, as long as it is *in the ballpark*. (Typical initial value: 20.)

1555 SGSENTHI Output SG T/H State RE 4 SG steam node average specific enthalpy Btu/lbm

1556 SGSENTH2 Output SG T/H State RE 4 SG evaporator node average sp. enthalpy BtuAbmr

1557 SGS ENTH3 Output SG T/H State RE 4 SG downcomer node average sp. enthalpy Btu/Ibm

1560 SGS El Output SG T/H State RE 4 SG steam dome node total energy. Btu

1561 SGS E2 Output SG T/H State RE 4 SG evaporator node total energy Btu

1562 SGS_E3 Output SG T/H State RE 4 SG downcomer node total energy Btu

1565 SGS HF Output SG T/H State RE 4 SG saturated liquid specific enthalpy Btu/Ibm

1566 SGS HG Output SG T/H State RE 4 SG saturated steam specific enthalpy Btu/lbm

1567 SGSHLEVEL Output SG T/H State RE 4 SG downcomer coolant level Feet

1568 SGSHT2 Output SG T/H State RE 4 SG evaporator coolant level. This is the 2-phase level calculated by Feet CENTS form the evaporators masses, specific volumes and volume to height dependency. Normally, until lower power levels (steaming rates), evaporator volume Is full of 2-phase flow to the separators.

1569 SGSHT3 Output SG T/H State RE 4 SG downcomer coolant level. This Is the actual 2-phase level in the Feet downcomer calculated by CENTS.

1570 SGS_HTI Output SG T/H State RE 4, 3 Instrument-measured water levels (SG,Ieg) This is calculated by Feet CENTS from the actual SG water level, and the known specific volumes and reference leg and calibration information for the instruments.

1571 SGSM1 Output SG T/State RE 4 SG steam node total mass Lbm

1572 SGSM2 Output SG I _ T/H State RE 4 SG evaporator node total mass ILbm



Index Lona Variable Name Input/ System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons 1573 SGS M3 Output SG T/H State RE 4 SG downcomer node total mass Lbm 1576 SGS P Output SG T/H State RE 4 SG steam node pressure Psia 1577 SGS RECIRC Output SG T/H State RE 4 SG evaporator to downcomer flow ratio Dimensionless 1578 SGS RHO1 Output SG T/H State RE 4 SG steam node density Lbml/ft 3

1579 SGS RHO2 Output SG T/H State RE 4 SG evaporator node density Lbm/ft3

1580 SGS RHO3 Output SG T/H State RE 4 SG downcomer node density Lbrm/ft 3

1583 SGS SV1 Output SG T/H State RE 4 SG steam node average specific volume Ft 3 /Ibm 1584 SGSSV2 Output SG T/H State RE 4 SG evaporator node average spec volume Ft3 Abm 1585 SGS SV3 Output SG T/H State RE 4 SG downcomer node average spec. volume Ft3 /Ibm 1588 SGS TREFLG Output SG T/H State RE 4 SG reference leg water temperature Degree F 1589 SGS TWALL Output SG T/H State RE 4 SG wall metal temperature Degree F 1590 SGS T1 Output SG T/H State RE 4 SG steam node temperature Degree F 1591 SGS T2 Output SG T/H State RE 4 SG evaporator node temperature Degree F 1592 SGS T3 Output SG T/H State RE 4 SG downcomer node temperature Degree F 1595 SGS USTM Output SG T/H State RE 4 Steam velocity leaving separators Ft/sec 1596 SGS VF Output SG T/H State RE 4 SG saturated liquid specific volume Ft3 /Abm 1597 SGS VF2 Output SG T/H State RE 4 SG evaporator node liquid spec. volume Ft3 Abm 1598 SGS VF3 Output SG T/H State RE 4 SG downcomer node liquid specific volume Ft3 /Abm 1601 SGS VG Output SG T/H State RE 4 SG saturated steam specific volume Ft3 /Abm 1602 SGS V1 Output SG T/H State RE 4 SG steam node total volume Ft3

1603 SGS V2 Output SG T/H State RE 4 SG evaporator node total volume Ft3

1604 SGS V3 Output SG T/H State RE 4 SG downcomer node total volume Ft 3

1607 SGS WF1 Output SG T/H State RE 4 SG steam node liquid mass Lbm 1608 SGS WF2 Output SG T/H State RE 4 SG evaporator node liquid mass Lbm 1609 SGS WF3 Output SG _T/H State RE 4 SG downcomer node liquid mass Lbm 1612 SGS WG1 Output SG T/H State RE 4 SG steam node steam mass Lbm 1613 SGS WG2 Output SG T/H State RE 4 SG evaporator node steam mass Lbm 1614 SGS WG3 Output SG T/H State RE 4 SG downcomer node steam mass Lbm 1617 SGS W13 Output SG T/H State RE 4 Steam node to downcomer flowrate Lbm/sec 1618 SGS W21 Output SG T/H State RE 4 SG evaporator to steam node flow rate Lbm/sec 1619 SGS W23 Output SG T/H State RE 4 Evaporator to downcomer circulation flow Lbm/sec 1620 SGS W31 Output SG I T/H State RE 4 Downcomer to steam node vaporization flow rate Lbmlsec 1621 SGS W32 Output SG T/H State RE 4 SG downcomer to evaporator flow rate Lbm/sec 1626 SGS WOUTSG Output SG T/H State RE 8 SG steam outlet nozzle flow Lbm/sec 1627 SGS_Xl Output SG T/H State RE 4 SG steam node quality Fraction 1628 SGS X2 Output SG T/H State RE 4 SG evaporator node quality Fraction 1629 SGS_X3 Output SG T/H State RE 4 SG downcomer node quality Fraction 1632 SGSFLOWCHOKED Output SG TiH State LO 8 Flag" steam flow choked at restrictor True False 1633 SGS HEAT Partition RE 60 SG heat transfer variables Partition 1634 SGT_RCSQHOT Output SG RCS T/H State RE 4 SG hot side RCS-to-tube heat transfer Btu/sec

G- 127WCAP- 15996-NP, Revision 0


Index Long Variable Name - Input System System System Variable's Type Dlmen- Definition , Units •,< No. OutDut AIt. 1 Alt 2 Function sions ,.

1635 SGTSGQHOT Output SG T/H State RE 4 Hot side tube-to-secondary heat transfer Btu/sec

1636 SGT RCS_0COLD Output SG RCS T/H State RE 4 SG entire cold side RCS-to-tube heat tr. Btu/sec

1637 SGTSGOQCOLD Output SG T/H State RE 4 Entire cold side tube-to-secy heat trans Btulsec

1640 SGTTEMP HOT Output SG T/H State RE 4 SG hot side tube metal temperature Degree F

1641 SGTTEMPCOLD Output SG T/H State RE 4 SG cold side tube metal temp, evaporator Degree F

1643 SGSHEATLOAD Output SG T/H State RE Total secondary side heat load Btu/sec

1644 SGS_0_CONT Output SG T/H State RE 4 SG wall-to-containment heat rate Btulsec

1645 SGSOWALLI Output SG T/H State RE 4 SG steam node steam-to-wall heat rate Btu/sec

1646 SGS_Q0WALL3 Output SG T/H State RE 4 SG downcomer node lig-to-wall heat rate Btu/sec

1647 SGSSTEAMLINE Partition RE 390 SG steam line vanables Partition

1648 MSLHSTATE Partition RE 40 Steamllne header vanables Partition

1649 MALMSLBOUT Input MSL Malfunction IN Steamline break in MSLH flag: 0=>no 1-->yes. The break area is Flag:; MSLB •AREA. Reference 1, Section 7.5.2.

1650 MSLBOUTFLOW Output MSL RE Steamline break outside containment flow rate. Reference 1, Lbm/sec Section 7.5.2.

1651 MSLH CON_1O Output MSL Solutes RE MSLH node Iodine concentration. This variable refers to the Mlcrocurle/ibm concentration in the header (I e. the volume downstream of the MSIVs). Reference 1, Sections 5 6 and 7.3.3.

1652 MSLHCONPT Output MSL Solutes RE MSLH node particulates concentration. This variable refers to the Microcurle/ibm concentration in the header (I.e. the volume downstream of the MSIVs). Reference 1, Sections 5 6 and 7.3.3.

1653 MSLHCONXE Output MSL Solutes RE MSLH node xenon concentration. This variable refers to the Mlcrocurle/lbm concentration In the header (I.e. the volume downstream of the MSIVs). Reference 1, Sections 5.6 and 7.3.3.

1654 MSLH-DVDH Output MSL TMH State RE MSLH node partial derivative of sp. vol. with respect to enthalpy. Composite Reference 1, Sections 5.6 and 7.3 3. Units

1655 MSLHDVDP Output MSL T/H State RE MSLH node partial sp. vol. with pressure. This variable refers to the Composite parameter value in the header (I e. the volume downstream of the Units MSIVs). Reference 1, Sections 5.6 and 7.3.3.

1656 MSLHH Output MSL T/H State RE MSLH node enthalpy. This variable refers to the parameter value Btu/lbm In the header (I e. the volume downstream of the MSIVs). Reference 1, Sections 5 6 and 7.3.3.

1657 MSLH_HF Output MSL T/H State RE MSLH node saturated liquid enthalpy. This variable refers to the BtuAbm parameter value in the header (I e. the volume downstream of the MSIVs). Reference 1, Sections 5 6 and 7.3.3.

1658 MSLHHG Output MSL T/H State RE MSLH node saturated steam enthalpy. This variable refers to the Btu/lbm parameter value In the header (I e. the volume downstream of the MSIVs). Reference 1, Sections 5_6 and 7.3.3.

1659 MSLH_M Output MSL T/H State RE MSLH node mass. This variable refers to the parameter value in Ibm the header (I e. the volume downstream of the MSIVs). Reference

1 _1, Sections 5 6 and 7.3 3


Table G.1: Dictionary Listing!

Index Long Variable Name Input System System System Variable's TYie Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

1660 MSLHML Output MSL T/H State RE MSLH node liquid mass. This variable refers to the parameter Lbm value in the header (i.e. the volume downstream of the MSIVs). Reference 1, Sections 5.6 and 7 3 3

1661 MSLHP Output MSL T/H State RE MSLH node pressure. This variable refers to the parameter value Psia in the header (I e. the volume downstream of the MSIVs). Reference 1, Sections 5 6 and 7 3 3

1662 MSLHQ Output MSL T/H State RE MSLH coolant-to-wall heat rate. This variable refers to the Btu/sec parameter value in the header (I.e. the volume downstream of the

I_ MSIVs). Reference 1, Sections 5.6, 7 3 3 and 7.4 1663 MSLH_0_ATM Output MSL T/H State RE MSLH wall-to-atmosphere heat rate. This variable refers to the Btulsec

parameter value in the header (I.e. the volume downstream of the MSIVs) Reference 1, Sections 5.6, 7.3 3 and 7 4.

1664 MSLHSV Output MSL T/H State RE MSLH node specific volume. This variable refers to the parameter Ft3/Ibm value in the header (I.e. the volume downstream of the MSIVs) Reference 1, Sections 5 6 and 7 3 3

1665 MSLHSVF Output MSL T/H State RE MSLH node saturated liquid specific vol This variable refers to the FtA/bm parameter value in the header (I e. the volume downstream of the MSIVs) Reference 1, Sections 5 6 and 7.3.3.

1666 MSLH_SVG Output MSL T/H State RE MSLH node saturated steam specific vol. This variable refers to Ft3 Albm the parameter value in the header (I.e. the volume downstream of _the MSIVs) Reference 1, Sections 5 6 and 7 3 3

1667 MSLHT Output MSL T/H State RE MSLH node temperature This variable refers to the parameter Degree F value in the header (I e. the volume downstream of the MSIVs). Reference 1, Sections 5.6 and 7.3 3.

1668 MSLHTWALL Output MSL T/H State RE MSLH node pipe metal temperature. This variable refers to the Degree F parameter value in the header (I.e. the volume downstream of the MSIVs) Reference 1, Sections 5 6 and 7.3.3.

1669 MSLH WIN Output MSL T/H State RE 8 Steamline steam flow into the header Lbm/sec

1670 MSLHX Output MSL T/H State RE MSLH node quality. This variable refers to the parameter value in Fraction the header (I e. the volume downstream of the MSIVs)

1671 STEAMLINE STATE Partition RE 350 Steamlines & stmline ext. valves Partition 1672 MALMSLBIN Input MSL Malfunction IN 8 Steamline Break. The break area is MSLBAREA The precise Flag

break location along the steamline is determined by the K-factor MSLHFKBRK. For steam line i, MALMSLBINQ) = 0, No break = 1, Break before the MSIV, discharging to the containment. = 2, Break before the MSIV, discharging to the atmosphere. = 3, Break after the MSIV, before the MSLH-side flow restrictor and

the steamline check valve, discharging to the atmosphere. Reference 1 Section 7.5.2.

1673 MSLB-IN-FLOW Output MSL T/H State RE 8 Steamline break inside containment flowrate Reference 1, Section Lbrn/sec 1_ 1_ _752 1



Index Long Variable Name Inut/ System system system variable's Twye Dlmen- Definition Units No. Output Alt. I Alt. 2 Function slons

1674 MSLH_.HSL Output MSL T/H State RE 8 SG steamline enthalpy. This is the CENTS calculated parameter Btu/ibm value in the steam line section between the SG and the MSIV.

1675 MSLHPSL Output MSL T/H State RE 8 SG steamline pressure. This is the CENTS calculated parameter Psia value in the steam line section between the SG and the MSIV.

1676 MSLHTSL Output MSL T/H State RE 8 SG steamhine temperature. This Is the CENTS calculated Degree F parameter value in the steam line section between the SG and the __ MSIV.

1677 MSLH_ISL Output MSL Solutes RE 8 SG steamline iodine concentrations. This Is the CENTS calculated Microcude/lbm parameter value In the steam line section between the SG and the _ _MSIV.

1678 MSLHCSL Output MSL Solutes RE 8 SG steamline partic concentrations. This Is the CENTS calculated Microcurie/bm parameter value in the steam line section between the SG and the

__ MSIV. 1679 MSLHXSL Output MSL Solutes RE 8 SG steamline xenon concentrations This is the CENTS calculated Microcurle/Ibm

parameter value In the steam line section between the SG and the __MSIV.

1680 MSLHMSIV_POS Output MSL Hardware RE 8 MSIV fraction open. Fraction I _State

1681 MSLHMSIV_SIG I/O MSL Hardware RE 8 MSIV signal to the valve actuator. This is normally an output from Fraction State the valve controller, when MSIS is in automatic control. If MSIS Is

In manual, then the USER can shut the MSIV by setting the parameter value to 0.0. In this case it is an input. Usually, the Ivalue for this parameter Is 0 0 or 1.0.

1682 MSLHMSIVBYPASSPOS Input MSL Hardware RE 8 MSIV bypass fraction open. For safety analysis, this parameter is Fraction State set to zero. It should be used only for special testing scenarios of

plant warmup.

1683 MSLHVALVEPOS Output MSL Hardware RE 50 Steamline external valves fraction open. This output array Is Fraction State calculated by the CENTS valve actuator controllers. The array

includes the ADVs, MSSVs, SDBCS valves, etc.

1684 MSLHVALVESIG I/O MSL Hardware RE 50 Steamline external valves signal. This Is normally an output array of Fraction State valve signals calculated by the CENTS controllers, when their

associated control systems are in automatic. When a particular system (e g. SDBCS) is in manual, then the valve signals can be USER controlled input which drives the valve actuator controllers to

_vary valve position. 1685 SLP_FLOW Output MSL T/H State RE 50 Steamline external valves flow rates This output array Is calculated Lbm/sec

by CENTS using the appropriate flow correlation, which Is normally the CRITCO critical flow correlation when the plant Is hot and at power.

1686 MSLHAOUT Partition MSL Hardware RE 9, 4 Steamline external valves combined areas Partition I_ _ I_ _ I_ _ _ State I II


Table G.1: Dictionary Listing!

Index Long Variable Name Input System System System Variable's Type DImen- Definition Units No. Output Alt. 1 Alt. 2 Function slons 1687 MSLHAOUTATM Output MSL Hardware RE 9 External valves flow area, steamlines to atmosphere. This array Ft2

State represents the combined open area of all valves discharging to atmosphere for each steam line, plus the last entry is for the SL header. (Note, the array allows for up to 4 SGs, each with 2 SUs and one header. For a 2 SG plant with one SL each, only the first three values in the array are used )

1688 MSLH_AOUTCOND Output MSL Hardware RE 9 External valves flow area, steamlines to condenser. This array Fte State represents the combined open area of all valves discharging to

condenser for each steam line, plus the last entry is for the SL header. (Note, the array allows for up to 4 SGs, each with 2 SL's and one header. For a 2 SG plant with one SL each, only the first

f _ three values in the array are used ) 1689 MSLHAOUTCONT Output MSL Hardware RE 9 External valves flow area, steamlines to containment This array Ft2

State represents the combined open area of all valves discharging to containment for each steam line, plus the last entry is for the SL header. (Note, the array allows for up to 4 SGs, each with 2 SL2s and one header. For a 2 SG plant with one SL each, only the first three values in the array are used )

1690 MSLH.AOUTTURB Output MSL Hardware RE 9 External valves flow area, steamlines to turbine. This array Fe State represents the combined open area of all valves discharging to

turbine for each steam line, plus the last entry is for the SL header. (Note, the array allows for up to 4 SGs, each with 2 SL's and one header. For a 2 SG plant with one SL each, only the first three values in the array are used )

1691 MSLH WOUT Partition T/H State RE 9, 4 Steamline ext valves combined flowrates Partition 1692 MSLHWOUTATM Output MSL T/H State RE 9 External valves flow rate, steamlines to atmosphere This array Lbrn/sec

represents the combined flow rate through all valves discharging to atmosphere, separately from each steam line and from the SL header. The array allows for up to 4 SGs, each with 2 SLs, plus one header. If 2 headers are modeled (NUMMSLH=2), then the flows from both header nodes are combined in one array element (E.g., For a 2 SG plant with one SL per SG, only the first 3 values in the array are used, regardless of the number of header nodes )

1693 MSLHWOUTCOND Output MSL T/H State RE 9 External valves flow rate, steamlines to condenser. This array Lbm/sec represents the combined flow rate through valves discharging to condenser, separately from each steam line and from the SL header. The array allows for up to 4 SGs, each with 2 SLs, plus one header. If 2 headers are modeled (NUMMSLH=2), then the flows from both header nodes are combined in one array element. (E g, For a 2 SG plant with one SL per SG, only the first 3 values in the array are used, regardless of the number of header nodes ) I___

WCAP- 15996-NP, Revision 0 G- 131


Index Long Variable Name, Inut/ System System System Variable's Type Dlmen- Definition , Units No. , Output Alt.1 Alt. 2. Function slons _________

1694 MSLHWOUTCONT Output MSL T/H State RE 9 External valves flow rate, steamlines to containment. This array Lbm/sec represents the combined flow rate through all valves discharging to containment, separately from each steam line and from the SL header. The array allows for up to 4 SGs, each with 2 SLs, plus one header. If 2 headers are modeled (NUMMSLH=2), then the flows from both header nodes are combined In one array element. (E.g, For a 2 SG plant with one SL per SG, only the first 3 values in the array are used, regardless of the number of header nodes.)

1695 MSLHWOUTTURB Output MSL T/H State RE 9 External valves flow rate, steamlines to turbine. This array Lbm/sec represents the combined flow rate through all valves discharging to turbine, separately from each steam line and from the SL header. The array allows for up to 4 SGs, each with 2 SLs, plus one header. If 2 headers are modeled (NUMMSLH=2), then the flows from both header nodes are combined in one array element. (E.g, For a 2 SG plant with one SL per SG, only the first 3 values in the array are used, regardless of the number of header nodes.)

1696 MSLH OUTFLOW Partition T/H State RE 5, 4 Steamline outflow quantities, inc. break Partition 1697 MSLH_FLOW-ATM Output MSL T/H State RE Total flow rate, steamline to atmosphere. This parameter Is the Lbm/sec

combined flow from all steam line valves which exit to the atmosphere. Hence, it equals SUM(MSLH_ WOUTATM(I))

1698 MSLHENTHATM Output MSL T/H State RE Total flow enthalpy, steamline to atmosphere. This parameter Is the BtuAbm weighted average enthalpy of all the steam flow from the steam line valves which exit to the atmosphere.

1699 MSLHI0_ATM Output MSL Solutes RE Tot flow Iodine concentration, steamline to atmosphere. This Microcude/lbm parameter is the weighted average Iodine concentration of all the

_ steam flow from all steam line valves which exit to the atmosphere. 1700 MSLH_PTATM Output MSL Solutes RE Tot flow particulate concentration, steamline to atmosphere. This Microcurle/ibm

parameter is the weighted average particulate (cesium) concentration of all the steam flow from all steam line valves which exit to the atmosphere.

1701 MSLHXEATM Output MSL Solutes RE Total flow xenon concentration, steamline to atmosphere. This Microcurde/bm parameter Is the weighted average Xenon concentration of all the steam flow from all steam line valves which exit to the atmosphere.

1702 MSLHFLOW-COND Output MSL T/H State RE Total flow rate, steamline to condenser. This parameter Is the Lbm/sec combined flow from all steam line valves which exit to the condenser. Hence, It equals SUM(MSLHWOUTCOND(I))

1703 MSLHENTHCOND Output MSL T/H State RE Total flow enthalpy, steamline to condenser. This parameter Is the BtuA/bm weighted average enthalpy of all the steam flow from the steam line valves which exit to the condenser.

1704 MSLHIOCOND Output MSL Solutes RE Total flow iodine concentration, steamline to condenser. This Microcude/Ibm parameter Is the weighted average Iodine concentration of all the steam flow from all steam line valves which exit to the condenser. I



Index Long Variable Name Input I System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

1705 MSLHPTCOND Output MSL Solutes RE Total flow particulate concentration, steamline to condenser. This Microcurie/lbm

parameter is the weighted average particulate (cesium) concentration of all the steam flow from all steam line valves which exit to the condenser.

1706 MSLHXECOND Output MSL Solutes RE Total flow xenon concentration, steamline to condenser. This Microcurie/lbm parameter is the weighted average Xenon concentration of all the steam flow from all steam line valves which exit to the condenser.

1707 MSLHFLOW_CONT Output MSL T/H State RE Total flow rate, steamline to containment. This parameter is the Lbm/sec

combined flow from all steam line valves which exit to the containment Hence, it equals SUM(MSLH WOUT CONT(l))

1708 MSLHENTHCONT Output MSL T/H State RE Total flow enthalpy, steamline to containment. This parameter is BtuAbm

the weighted average enthalpy of all the steam flow from the steam hline valves which exit to the containment.

1709 MSLHIOCONT Output MSL Solutes RE Total flow iodine concentration, steamline to containment. This Microcurie/Ibm parameter is the weighted average Iodine concentration of all the

_steam flow from all steam line valves which exit to the containment 1710 MSLHPTCONT Output MSL Solutes RE Total flow particulate concentration, steamline to containment This Microcurie/lbm

parameter is the weighted average particulate (cesium) concentration of all the steam flow from all steam line valves which exit to the containment.

1711 MSLH_XECONT Output MSL Solutes RE Total flow xenon concentration, steamline to containment. This MicrocurieAbm parameter is the weighted average Xenon concentration of all the

I_ isteam flow from all steam line valves which exit to the containment 1712 MSLHFLOWTURB Output MSL T/H State RE Total flow rate, steamline to turbine. This parameter is the Lbm/sec

combined flow from all steam line valves which exit to the containment. Hence, it equals SUM(MSLHWOUTTURB(I)) Usually this involves only the TAV.

1713 MSLHENTHTURB Output MSL T/H State RE Total flow enthalpy, steamline to turbine. This parameter is the BtuAbm weighted average enthalpy of all the steam flow from the steam line valves which exit to the turbine.

1714 MSLH_I10_TURB Output MSL Solutes RE Total flow iodine concentration, steamline to turbine. This Microcurie/Ibm parameter is the weighted average Iodine concentration of all the steam flow from all steam line valves which exit to the turbine

1715 MSLHPTTURB Output MSL Solutes RE Total flow particulate concentration, steamline to turbine. This Microcurie/bm parameter is the weighted average particulate (cesium) concentration of all the steam flow from all steam line valves which exit to the turbine

1716 MSLHXETURB Output MSL Solutes RE Total flow xenon concentration, steamline to turbine. This Microcurie/lbm parameter is the weighted average Xenon concentration of all the steam flow from all steam line valves which exit to the turbine.

1717 MSI-HIOINTFLOW Partition Solutes RE 10 Integrated iodine flows Partition 1718 MSLH 10 INT ATM Output MSL Solutes RE Integrated iodine flow to atmosphere Curie 1719 MSLH IO INT COND Output MSL Solutes RE _ Integrated iodine flow to cond (w/o DF) Curie 1720 MSLH 10 INT CONT Output MSL Salutes RE r_ IIntegrated iodine flow to containment Curie


Table G.A: Dictionary Listin2

Index Long Variable Name in.. t I System System System Variable's Type Dimen- Definition - , Units No...... , ", " .•' Output Alt. I Alt 2 Function -., sions

1721 MSLH IOINT TURB Output MSL Solutes RE Integrated iodine flow to turb (w/o DF) Cune

1722 MSLHIOCONTLEAK Output MSL Solutes RE Iodine leak rate from containment. Microcurlelsec

1723 MSLH_10_CONTINTLEAK Output MSL Solutes RE Integrated iodine leak from containment. Curie 1724 MSLHFLOWCHOKED Output MSL T/H State LO 8 Flag: Flow Is choked between the steamline header and the True False

I_ __III steamline break.

1725 SGSFWS Partition RE 180 SG feedwater system variables Partition

1726 FWSPUMPPIN Output FW RE Main FW pumps suction pressure Psla

1727 FWSPUMPP P Output FW RE 4 Main feedwater pump discharge pressure. Psia

1729 FWSVALVEPRESSURES Partition RE 4, 2 Main FW valve discharge pressure. Psia

1730 FWSVALVEP Output FW RE 4 FW downcomer valve discharge pressure. Psia

1731 FWSECON VALVE P Output FW RE 4 FW economizer valve discharge pressure. Psia,

1734 FWSPUMP FLOW Output FW RE 4 Main feedwater pump delivered flow. Galmmn

1735 FWSLINE FLOWS Partition RE 4, 2 Flow through main FW control valves. Lbm/sec

1736 FWS_FLOW I/O FW T/H State RE 4 Main FW flow rate at downcomer valves. With the current simplified Lbm/sec FWS controllers In auto, this parameter is the CENTS calculated output of flow to the downcomer feed ring of the SG. If the FWS controllers are in manual, then this variable becomes an Input, controlled by the USER to manually dictate flow rate.

1737 FWSECONFLOW i/O FW T/H State RE 4 Main FW flow rate at economizer valves. With the current Lbm/sec simplified FWS controllers in auto, this parameter Is the CENTS calculated output of flow to the economizer (Sys 80 design) of the SG. If the FWS controllers are In manual, then this variable becomes an Input, controlled by the USER to manually dictate flow rate.

1738 FWSFLOWTOT Output NW I T/H State RE 4 Total MFW flow to SG through downcomer and economizer valves. Lbm/sec

1739 FWSENTH Output FW T/H State RE 4 Main feedwater flow spec. enthalpy. Btu/Ibm

1740 FWS LINEENTHALPIES Partition RE 4, 2 Inventory enthalples in main FW lines Btu/bmn

1741 FWS_LINEH Output FW T/H State RE 4 Downcomer feedwater line enthalpy. This output parameter = Btu/lbm FWS ENTH.

1742 FWSECONLINEH Output FW T/H State RE 4 Economizer feedwater line enthalpy. This output parameter = Btu/lbm FWS__ENTH, for those systems with an economizer line.

1743 FWS..CONJO Input MW Solutes RE 4 Main feedwater supply Iodine concentration. This Is USER defined Microcurle/lbm input, normally set to 0 0.

1744 FWS_CONPT Input FW Solutes RE 4 Main feedwater supply particulate concentration. This is USER Microcurie/bm defined Input, normally set to 0.0.

1745 FWS__CONXE Input FW Solutes RE 4 Main feedwater supply xenon concentration. This is USER defined Microcurde/bm input, normally set to 0.0.

1746 FWS NOZZLEFLOW Partition T/H State RE 4, 2 Main FW flow rates at SG feed nozzles Lbm/sec

1747 FWSNOZFLOW Output 'WN T/H State RE 4 Main FW flow rate at downcomer nozzle. With the current simplified Lbm/sec

I__ I_ _ _MFW model, this output parameter = FWSFLOW(I). 1_ 7_



Index Long Variable Name Input System System System Variable's Type Dimen- Definition Units No. Output AIt. 1 AIt. 2 Function slons 1748 FWSECONNOZFLOW Output FW T/H State RE 4 Main FW flow rate at economizer nozzle With the current Lbm/sec

simplified FW model, this output parameter = FWSECONFLOW(l).

1749 FWS NOZZLE ENTHALPY Partition T/H State RE 4, 2 Main FW flow enthalpy at SG feed nozzles Btu/Ibm 1750 FWS NOZ ENTH Output FW T/H State RE 4 Main FW flow enthalpy at downcomer nozzles. Btu/lbm 1751 FWSECONNOZENTH Output FW T/H State RE 4 Main FW flow enthalpy at economizer nozzles Btu/lbm 1752 FWS NOZZLE QUALITY Partition _T/H State RE 4, 2 Main FW flow quality at SG feed nozzles Fraction 1753 FWSNOZQUAL Output FW _T/H State RE 4 Main FW flow quality at downcomer nozzle Fraction 1754 FWSECONNOZ QUAL Output FW T/H State RE 4 Main AN flow quality at economizer nozzle Fraction 1755 FWSNOZZLE TEMP Partition T/H State RE 4, 2 Main FW flow temp at SG feed nozzles Degree F 1756 FWS NOZ T Output FW T/H State RE 4 Main FA flow temp at downcomer nozzle Degree F 1757 FVSECONNOZ T Output FW T/H State RE 4 Main FW flow temp at economizer nozzle Degree F 1758 FWLBIN Partition T/H State RE 4, 2 Cues for feedline break inside chk valve Fraction 1759 MAL FNLB IN Input FW T/H State RE 4 Feedline break inside chk valve, DC line Fraction 1760 MALFWLBECONIN Input FW T/H State RE 4 Feedline break inside chk valve, EC line Fraction 1761 FWLB OUT Partition T/H State RE 4, 2 Cues for feedline brk outside chk valve Fraction 1762 MAL FWLB OUT Input FW T/H State RE 4 Feedline brk outside chk valve, DC line Fraction 1763 MAL FWLB ECON OUT Input FW T/H State RE 4 Feedline brk outside chk valve, EC line Fraction 1764 FWLB LOCATION Partition T/H State RE 4, 2 Feedline break locations, 0=valve 1 =nozz Fraction 1765 FWLB F Input I T/H State RE 4 Feedline break location, downcomer line Fraction 1766 AFNLB ECONF Input T/H State RE 4 Feedline break location, economizer line Fraction 1767 FALB W Partition T/H State RE 4, 2 Feedline break flow rates Lbm/sec 1768 FWLB FLOW Output FW T/H State RE 4 Downcomer feedline break flow rate Lbrn/sec 1769 FWLB ECONFLOW Output FW T/H State RE 4 Economizer feedline break flow rate. Lbm/sec 1770 FWLB H Partition T/H State RE 4, 2 Feedline break flow enthalpies Btu/lbm 1771 FWLB ENTH Output FW T/H State RE 4 Downcomer feedline break flow enthalpy BtuAbm 1772 FWLB ECON ENTH Output AFW I T/H State RE 4 Economizer feedline break flow enthalpy Btu/lbm 1773 FWLB QUALITY Partition T/H State RE 4, 2 Feedline break flow qualities Fraction 1774 FWLB-QUAL Output FW T/H State RE 4 Downcomer feedline break flow quality Fraction 1775 FWLB ECON QUAL Output AN T/H State RE 4 Economizer feedline break flow quality Fraction 1776 FWLB IODINE Partition Solutes RE 4, 2 Feedline break flow iodine concentrations Microcune/Ibm 1777 FWLB_10 Output FW Solutes RE 4 Downcomer feedline break flow iodine concentrations Microcurielbm 1778 FWLB ECONIO Output FW Solutes RE 4 Economizer feedline break flow iodine concentrations Microcurie/lbm 1779 FWLB PART Partition Solutes RE 4, 2 Feedline break flow particulate concentrations Microcurie/lbm 1780 FWLB PT Output FW Solutes RE 4 Downcomer feedline brk flow partic concentration Microcune/lbm 1781 FWLBECONPT Output FW Solutes RE 4 Economizer feedline brk flow partic concentration Microcurie/lbm 1782 FWLB XENON Partition _ _ Solutes RE 4, 2 Feedline break flow xenon concentration Microcurie/Ibm 1783 FWLB XE Output FW Solutes RE 4 Downcomer feedline brk flow xenon concentration Microcurieilbm 1784 FWLBECONXE Output FW _Solutes RE 4 Economizer feedline brk flow xenon concentration Microcune/lbm 1785 AFWS NOZ FLOW I/O FW AFW _ T/H State RE 4 Auxiliary feedwater flow rate to separate steam generator nozzle Lbm/sec


Table G.1: Dictionary Listing Index Long Variable Name- . Input-I Sytem System System Variable's -• 1 Dimen- Definition - -_ .:>- • , . ii, ,"

No.-, Output' - Alt. 1 Alt. 2i', Function ", - -slons. , . : ,%. V'... o. . - '.'

1786 AFWSENTH i/O FW AFW T/H State RE 4 Auxiliary feedwater flow spec. enthalpy. This input is set by the Btuflbm USER if the feedwater model is turned off, otherwise it is calculated. Often it is set to the FWS enthalpy until a sweep volume of hot FW

is "pushed' into the SG by the AFW system. Then, the AFW enthaipy is reduced to CWST enthalpy. This can be accomplished

I I using a CEER command WHEN statement.

1787 SGSSGBD Partition RE 100 SG blowdown system variables Partition

1788 SGBD-CON-1O Output SG SGBD Solutes RE SGBD tank Iodine concentration. This output is used IFF all the Microcudellbm blowdown system inputs have appropriate values and the blowdown

system Is activated by setting MOD_OFF_SGBD ^. F.

1789 SGBD_.CONPT Output SG SGBD Solutes RE SGBD tank particulates concentration. This output is used IFF all Microcurle/Ibm the blowdown system inputs have appropriate values and the

I blowdown system Is activated by setting MODOFF_SGBD =. F.

1790 SGBD_.CONXE Output SG SGBD Solutes RE SGBD tank xenon concentration. This output is used IFF all the MicrocurdeAbm

blowdown system Inputs have appropriate values and the blowdown system is activated by setting MODOFFSGBD =. F.

1791 SGBD_DVDH Output SG SGBD T/H State RE SGBD tank partial sp. vol with enthalpy. This output is used IFF all Composite

the blowdown system inputs have appropnate values and the Units _ _ _blowdown system is activated by setting MODOFFSGBD =. F.

1792 SGBDDVDP Output SG SGBD T/H State RE SGBD tank partial sp. vol. with pressure. This output is used IFF Composite - all the blowdown system inputs have appropriate values and the Units

_blowdown system Is activated by setting MODOFFSGBD =. F.

1793 SGBDH Output SG SGBD T/H State RE SGBD tank specific enthalpy. This output is used IFF all the ý Btu/Ibm blowdown system Inputs have appropriate values and the blowdown system is activated by setting MOD OFF SGBD =. F.

1794 SGBD.HF Output SG SGBD T/H State RE SGBD tank saturated liquid enthalpy. This output Is used IFF all Btu/lbm

the blowdown system inputs have appropriate values and the blowdown system is activated by setting MODOFF SGBD =. F.

1795 SGBDHG Output SG SGBD T/H State RE SGBD tank saturated steam enthalpy. This output is used IFF all Btu/lbm

the blowdown system Inputs have appropriate values and the

_blowdown system Is activated by setting MODOFFSGBD =. F.

1796 SGBDQL Output SG SGBD T/H State RE SGBD tank water level. This output is used IFF all the blowdown Feet

system Inputs have appropriate values and the blowdown system Is

activated by setting MODOFFSGBD =. F.

1797 SGBDM Output SG SGBD T/H State RE SGBD tank total mass. This output Is used IFF all the blowdown Lbm

system inputs have appropriate values and the blowdown system is


1798 SGBDML Output SG SGBD T/H State RE SGBD tank liquid mass. This output Is used IFF all the blowdown Lbm

system Inputs have appropriate values and the blowdown system Is

activated by setting MODOFF._SGBD =. F.

1799 SGBDP Output SG SGBD TM State RE SGBD tank pressure. This output is used IFF all the blowdown Psia system Inputs have appropriate values and the blowdown system is

----------- activated by setting MODOFFSGBD =. F. I



Index Long Variable Name Input/ System System System Variable's Type Dimen- Definition Units No.. Output Alt. 1 Alt. 2 Function slons

1800 SGBDSV Output SG SGBD T/H State RE SGBD tank specific volume. This output is used IFF all the Ft3Abm blowdown system inputs have appropriate values and the blowdown system is activated by setting MODOFFSGBD = F

1801 SGBDSVF Output SG SGBD T/H State RE SGBD tank sat. liquid specific volume. This output is used IFF all FteAbm the blowdown system inputs have appropriate values and the blowdown system is activated by setting MOD OFF SGBD =. F.

1802 SGBDSVG Output SG SGBD T/H State RE SGBD tank sat steam specific volume. This output is used IFF all Ft3aIbm

the blowdown system inputs have appropriate values and the _blowdown system is activated by setting MOD OFF SGBD = F

1803 SGBDT Output SG SGBD T/H State RE SGBD tank fluid temperature. This output is used IFF all the Degree F blowdown system inputs have appropriate values and the blowdown system is activated by setting MOD OFF SGBD = F

1804 SGBDrWALL Output SG SGBD T/H State RE SGBD tank wall metal temperature. This output is used IFF all the Degree F blowdown system inputs have appropriate values and the blowdown

system is activated by setting MODOFFSGBD =. F. 1805 SGBDX Output SG SGBD T/H State RE SGBD tank quality. This output is used IFF all the blowdown Fraction

system inputs have appropriate values and the blowdown system is activated by setting MOD OFF SGBD = F.

1806 jSGBDSGPOS Partition Hardware RE 8 SG blowdown line valves. Partition State

1807 SGBDSURFPOS Input SG SGBD Hardware RE 4 Surface blowdown lines valve positions. Used IFF all the Fraction State blowdown system inputs have appropriate values and the blowdown

system is activated by setting MOD OFFSGBD =. F.

1808 SGBDBOTPOS Input SG SGBD Hardware RE 4 Bottom blowdown lines valve positions. Used IFF all the blowdown Fraction State system inputs have appropriate values and the blowdown system is

activated by setting MOD-OFFSGBD = F

1809 SGBD SG FLOW Partition _T/H State RE 8 SG blowdown line flow rates Partition

1810 SGBDSURFFLOW I/O SG SGBD T/H State RE 4 Surface blowdown line flow rates. This is normally an output, but Lbm/sec with the SGBD system model deactivated, the USER may set blowdown flow rates with this variable as an input.

1811 SGBD.BOT_FLOW I/O SG SGBD T/H State RE 4 Bottom blowdown line flow rates. This is normally an output, but Lbm/sec with the SGBD system model deactivated, the USER may set blowdown flow rates with this variable as an input

1812 SGBD SG ENTH Partition _T/H State RE 8 SG blowdown line flow enthalpies Partition

1813 SGBDSURFENTH i/O SG SGBD T/H State RE 4 Surface blowdown line flow enthalpies This is normally an output, BtuAbm but with the SGBD system model deactivated, if the USER inputs the blowdown flow rates, then this variable is also input for the flow enthalpy

_ 1814 SGBD_BOTENTH I/O SG SGBD T/H State RE 4 Bottom blowdown line flow enthalpies. This is normally an output, BtuAbm

but with the SGBD system model deactivated, if the USER inputs the blowdown flow rates, then this variable is also input for the flow enthalpy.

1815 SGBD-SG-10 Partition SG SGBD Solutes RE 8 SG blowdown line flow iodine concs Partition

1816 SGBD SURF 10 Output SG SGBD Solutes RE 4 Surface blowdown line flow iodine concentrations Microcurie/lbm



Index Lon Variable Name - Inut System System System Variable's Type Dimen- Definition Units

NO. . Output Aft. 1 Alt 2 Function slons "

1817 SGBD BOT 1O Output SG SGBD Solutes RE 4 Bottom blowdown line flow Iodine concentrations Microcure/lbm

1818 SGBDSGPT Partition SG SGBD Solutes RE 8 SG blowdown line flow partic concentrations Partition

1819 SGBDSURFPT Output SG SGBD Solutes RE 4 Surface blowdown line flow partic concentrations Microcurde/bm

1820 SGBDBOTPT Output SG SGBD Solutes RE 4 Bottom blowdown line flow partic concentrations Microcude/lbm

1821 SGBD_SGXE Partition SG SGBD I Solutes RE 8 SG blowdown line flow xenon concentrations Partition

1822 SGBDSURFXE Output SG SGBD Solutes RE 4 Surface blowdown line flow xenon concentrations Microcude/lbm

1823 SGBDBOTXE Output SG SGBD Solutes RE 4 Bottom blowdown line flow xenon concentrations Microcune/lbm

1824 SGBDSINKPOS Partition SG SGBD Hardware RE 3 SGBD tank discharge line valves Partition

State

1825 SGBDOUTPOS Input SG SGBD Hardware RE 2 SGBO tank outlet lines valve positions. Used 1FF all the blowdown Fraction

- State system inputs have appropriate values and the blowdown system Is

activated by setting MOD.OFFSGBD =. F.

1826 SGBD-RELIEFPOS Input SG SGBD Hardware RE SGBD tank relief line valve position. Used IFF all the blowdown Fraction

State system inputs have appropriate values and the blowdown system is


1827 SGBDSINKFLOW Partibon T/H State RE 3 SGBD tank discharge line flow rates Partition

1828 SGBD. OUTFLOW Output SG SGBD T/H State RE 2 SGBD tank outlet lines flow rates. Used 1FF all the blowdown Lbm/sec system inputs have appropriate values and the blowdown system Is


1829 SGBDORELIEFLFLOW Output SG SGBD T-I State RE SGBD tank relief line flow rate. Used IFF all the blowdown system Lbm/sec

inputs have appropriate values and the blowdown system Is

activated by setting MODOFF_SGBD =. F.

1830 SGBD SINKENTH Partition T/H State RE 3 SGBD tank discharge line flow enthalples Partition

1831 SGBD OUTENTH Output SG SGBD T/H State RE 2 SGBD tank outlet lines flow enthalpies. Used IFF all the blowdown Btu/bm

system inputs have appropriate values and the blowdown system Is

I activated by setting MODOFFSGBD =. F.

1832 SGBD-RELIEF..ENTH Output SG SGBD T/H State RE SGBD tank relief line flow enthalpy. Used IFF all the blowdown Btu/lbm system Inputs have appropriate values and the blowdown system is


1833 SGBDSINK 10 Output SG SGBD Solutes RE 3 SGBD tank discharge line flow iodine concentrations Partition

1834 SGBDOUT_1O Output SG SGBD Solutes RE 2 SGBD tank outlet lines flow Iodine concentrations Microcure/lbm

1835 SGBDRELIEF 10 Output SG SGBD Solutes RE SGBD tank relief line flow Iodine concentration Microcurde/bm

1836 SGBDSINKPT Output SG SGBD Solutes RE 3 SGBD tank discharge line flow partic concentrations Parition

1837 SGBDOUTPT Output SG SGBD Solutes RE 2 SGBD tank outlet lines flow partic concentrations Microcude/ibm

1838 SGBDRELIEFPT Output SG SGBD Solutes RE SGBD tank relief line flow partic concentrations Mlcrocurie/bm

1839 SGBDSINKXE Output SG SGBD Solutes RE 3 SGBD tank discharge line flow xenon concentrations Partition

1840 SGBDOUT XE Output SG SGBD Solutes RE 2 SGBD tank outlet lines flow xenon concentrations Microcurle/lbm

1841 SGBDRELIEF.XE Output SG SGBD Solutes RE SGBD tank relief line flow xenon concentration Microcure/lbm

1842 SGBDSINKP Partition I - T/H State RE 3 SGBD tank disch. line dwnstrm pressures Partition

1843 SGBDOUT_P Input SG SGBD T/H State RE 2 SGBD tank outlet lines downstream pressures. Used IFF all the Psia

blowdown system Inputs have appropriate values and the blowdown

system is activated by setting MODOFFSGBD =. F.



Index Long Variable Name Input/ System System System Variable's Type Dimen- Definition Units NO. "Output Alt. 1 AIt. 2 Function sions 1844 SGBDRELIEFP Input SG SGBD T/H State RE SGBD tank relief line downstream pressure. Used IFF all the Psia

blowdown system inputs have appropriate values and the blowdown system is activated by setting MODOFFSGBD = F 1845 MOD_OFFSGBD Input SG SGBD Model LO Turns off SGBD model, when set to True. True False

Desiqn 1846 SGS TUNE Partition RE 50 SG adjustable constants Partition 1847 CONTSG_TEMP Input SG RE 4 Containment temperature at SGS. This input parameter provides Degree F

the same function as a SG boundary condition as does CONT TEMP(I) for the RCS nodes. 1849 PCONDENSER Input MSL RE Condenser pressure. This input parameter is normally set to a Psia typical low sub-atmospheric value. It is normally not of major importance for safety analysis, but would be of interest during cooldowns of the SG to pressures/temperatures below atmospheric _conditions

1850 SGSASEPTUNE Input SG RE SGS steam separator area tuning factor. This is one of the major Dimensionless tuning factors used during initial setup of a plant basedeck to referenced conditions This parameter effects the bubble rise velocity or steam separation rate, which in turn, dictates the fluid density in the evaporator, and to a lesser extent, the SG recirculation ratio. Often, at the completion of the tuning, ASEPSG is adjusted so that ASEP SGTUNE can be set to a value of 1.0.

1852 SGS_FK3_TUNE Input SG RE SGS downcomer flow coeff tuning factor. This is one of the major Dimensionless tuning factors used during initial setup of a plant basedeck to referenced conditions. This parameter effects the SG recirculation ratio, and to a lesser extent, the fluid density in the evaporator. Often, at the completion of the tuning, ASEP_SG is adjusted so that I I_ ASEP SG TUNE can be set to a value of 1 0.

1855 SGSHASUBOPTION Input SG LO Option for calculating subcooled region in the SG evaporator. Used True False always This is a Logical flag to activate/disable the subcooled layer model in the steam generator heat transfer calculation. This flag should be True in all realistic calculations, to activate the model, independently of plant design

1856 SGS_PCNVRG Input SG RE Pressure convergence criterion. Used always These is a Psia convergence criterion for the iterative steam generator pressure search. This parameter is numerical in nature, independent of plant

I_ Idesign. 1857 SGSPMIN Input SG RE Minimum secondary-side pressure. Used always. This is the Psia

minimum pressure allowed in the steam generator, for model I_ I_ integrity. This parameter is independent of plant design



Index Long Variable Name lnrut I Sstem Syter Sytem Variable's Typ Dlmen- Definition . - Units No. Output Alt. 1 Alt 2 Function slons

1858 SGS_RECIRCDELVOL Input SG RE Delta volume for adjusting reclrc flow. Used always, In conjunction Ft3

with SGS_RECIRCMIN. CENTS uses these two parameters to dynamically calculate the steam generator recirculation ratio (RCR = SGSW23 / FWSFLOW100) as a function of the coolant volume In the evaporator. CENTS calculates a volume defect, which Is the difference between the current evaporator coolant volume and the maximum volume to reach the can deck. If the volume defect is less than SGS_RECIRCDELVOL, then RCR is calculated as a function of the volume defect. If the volume defect exceeds SGSRECIRCDELVOL, then a minimum RCR Is Imposed, RCR = SGSRECIRC.MIN. (The coolant level may be lower, if the volume defect exceeds 2 * SGSRECIRCDELVOL, then RCR = 0.5* SGSRECIRCMIN, and If the volume defect exceeds 4 SGSRECIRCDELVOL, then RCR = 0 0.). SGS_RECIRC_DELVOL Is dependent on plant design, within its definition In the RCR model. If sufficient dynamic data Is available, then SGSRECIRCDELVOL may be determined by tuning it along with the other steam generator model tuning factors. Otherwise, typical values are used, ranging from 120 to 200 Mt3. SGSRECIRCMIN Is a numerical minimum, Independent of plant

I_ I design.

1859 SGS_RECIRCMIN Input SG RE Minimum recirculation for crossflow. Used always, in conjunction Dimensionless with SGS_-RECIRC._DELVOL CENTS uses these two parameters to dynamically calculate the steam generator recirculation ratio (RCR = SGS_W23 / FWSFLOW100) as a function of the coolant volume In the evaporator. CENTS calculates a volume defect, which is the difference between the current evaporator coolant volume and the maximum volume to reach the can deck. If the volume defect is less than SGSRECIRCDELVOL, then RCR Is calculated as a function of the volume defect. If the volume defect exceeds SGSRECIRCDELVOL, then a minimum RCR is imposed, RCR = SGSRECIRCMIN. (The coolant level may be lower: if the volume defect exceeds 2 * SGS_RECIRCDELVOL, then RCR = 0.5 * SGSRECIRCMIN, and if the volume defect exceeds 4 * SGS_RECIRC_DELVOL, then RCR = 0 0.). SGS_RECIRCDELVOL Is dependent on plant design, within Its definition in the RCR model. If sufficient dynamic data is available, then SGS.RECIRCDELVOL may be determined by tuning it along with the other steam generator model tuning factors. Otherwise, typical values are used, ranging from 120 to 200 ff3. SGSRECIRC_MIN Is a numerical minimum, Independent of plant

I __design.



Index Long Variable Name Input/ System System System Variable's Tipe Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

1861 SGS_TAURCI_TUNE Input SG RE SG recirculation flow time constant tuning factor Used in Dimensionless conjunction with TAURC1. Used always. CENTS applies a time constant to the SG recirculation flow (SGSW23). TAURCI is the time constant, and SGSTAURC1JUNE is a multiplying tuning factor on that time constant The time constant formed by the product TAURC1 * SGSTAURCITUNE is dependent on plant data, within the definition of the overall model. Its best value is usually determined by tuning. This is usually done by comparing the SG downcomer level trace immediately following scram against available plant data, and tuning this and other parameter until a good match is obtained (The SGS model has more tuning factors that affect the circulation and recirculation flows than is necessary. Therefore, the usual practice is to tune SGS_TAURC1_TUNE and SGSFK3_TUNE together, and SGS_TAURC2_MAX to a lesser extent )

1862 SGSTAURC2_MAX Input SG RE SG downcomer flow, maximum time constant. Used always. This Seconds is an upper limit on the lag time constant that is applied to the SG circulation flow (SGSW32). This time constant is weakly dependent on plant data, within the definition of the overall model. That is, its typical value is between 0 5 and 5.0, and a best value is usually determined by tuning. This is usually done by comparing the SG downcomer level trace immediately following scram against available plant data, and tuning this and other parameter until a good match is obtained. Note, however, that the SGS model has more tuning factors that affect the circulation flow than is necessary, and the other parameters have a considerably more pronounced effect than SGS_TAURC2_MAX. Therefore, the usual practice is to select a mid-range value (2 0 to 3 0) and tune the other parameters (SGS TAURC1 TUNE and SGSFK3_TUNE).

1864 SGSUADROPPERIM Input SG RE Perimeter of the feedring. Note that this input parameter is the Feet perimeter of the feednng around the SG, not the feedring pipe cross

_sectional penmeter dimension. 1865 SGS_UADROP_WFDMIN Input SG RE Minimum feedflow below which condensation efficiency = 1. Used Lbm/sec

when the SG downcomer water height is below the main feedwater nozzle. This parameter is used to determine an efficiency of condensation of steam on the incoming cold feedwater, as the water falls through the steam space The parameter is the minimum feedwater flowrate, above which a condensation efficiency is calculated as a function of the feed flow rate and steam region height. Below this feed flow rate, the condensation efficiency is 1 0 (i.e., any feed water that is injected into the steam space condenses enough steam to become saturated by the time it reaches the water below). This is a model parameter that is independent of plant design. The value that is typically used was determined from engineering judgment to be between 0 and 100 Ibm/sec, and its effect on transient results is minimal within that range.



Index Long Varable Name Input System System System Variable's Tvye Dlmen- Definition .. -Units

No.• Output Alt. 1 Alt. 2 Function slons _

1866 SGS-USTMMIN Input SG RE Minimum steam separation velocity. Used always. This is a Ft/sec minimum steam separation velocity Imposed on the Wilson correlation. The appropriate value for this parameter is dependent on the plant design, and Is determined by tuning the model to available plant data for shrink and swell in low power conditions. The value that Is typically used was determined from engineering judgment and from experience In tuning the model to be between 0 05 and 0.50 ft/sec.

1867 SGS_VCNVRG Input SG RE Volume convergence criterion. Used always. This Is a convergence Fraction criterion for the SG pressure search iterative solution. The iteration is converged when the change in SG volume from the last iteration (due to a change in pressure from the last iteration) is less than SGS_VCNVRG * VOLSGS. (VOLSGS is the total physical volume.) SGSVCNVRG Is also used the same way in SGFEED In the iterative solution for feedwater flow as a function of feedline junction pressure. Note, however, that SGFEED is called only if NUMFWSPUMPS > 0. SGS_VCNVRG Is strictly a numerical, dimensionless, convergence criterion, and is therefore Independent of plant design.

1868 SGS_WFMIN Input SG RE Region 2(evaporator) liquid mass for single-region switch. Used Lbm always. This Is the minimum liquid mass in the downcomer or the evaporator region that can be accommodated by the SGS model without instability. When downcomer liquid mass Is below SGSWFMIN/2, it Is immediately transferred to the evaporator region. When the evaporator region liquid mass Is below SGSWFMIN, the model combines all the regions into one and employs the one-region formulation. When the liquid mass exceeds 2*SGSWFMIN, the model reverts back to the multi-region formulation. This is a model-switch parameter whose appropriate value depends on the multi-region model's stability in low Inventory conditions, and is Independent of plant design in the range of typical

steam generator sizes.

1869 SGSX2_I Input SG RE Region 2 (evaporator) quality necessary to re-establish region 1 Fraction (steam dome). Used only when steam Is introduced into the steam generator after It filled solid with water. When the steam generator goes solid, region 1 (dome steam region) disappears. When steam reappears In the evaporator region, region 1 will be re-established. To prevent this from happening prematurely, possibly resulting in cycling or pressure spikes, CENTS waits until the evaporator region quality exceeds SGS_X2_1. Since It Is designed to prevent cycling or pressure spikes, this parameter Is numencal in nature.

I_ iTherefore, it is independent of plant design.



Index Lona Variable Name ;InU. System System System Variable's Type Dimen- Definition Units

No. Output Alt. 1 Alt. 2 Function sions

1884 SPINIT I/O SG Initialization RE Initial steam generator pressure. This is the USER specified input Psia

for the SG dome pressure which CENTS uses during initialization. It is used as input only if SGSJNIT_OPTION = 0.0, in which case CENTS adjusts the effective SG tube heat transfer area to obtain the desired SG pressure SPINIT. If SGS_INIT_OPTION = 1, then CENTS calculates SPINIT as the appropnate SG dome pressure from known input parameters, including tube heat transfer area

1885 SLINIT Input SG Initialization RE Initial SG secondary side mixture level. This is a USER specified Feet input for SG downcomer level, as measured from the top of the tube sheet. CENTS uses this parameter during code initialization as a needed input in the determination of SG secondary masses and other T/H conditions

1886 FHINIT Output FW SG Initialization RE Initial feed water enthalpy. This output parameter indicates the FW BtuAbm enthalpy at time of initialization. The USER defined input which dictates this value is CTL_FWSH(I'2)

1888 SGS TUBE AREA DEGRAD Partition RE 10 Secondary tube area degradation model Partition

1889 SGSTUBEAREAOPTION Input SG LO Option flag to degrade SG secondary side tube heat transfer, as a True False "CESEC compatibility model". Used in conjunction with SGSMASSFULLJUBE-AREA and SGSMASSZERO_TUBEAREA. This flag is always tested. Normally (this flag is False), the model calculates the degradation of heat transfer as a function of the void fraction in the SG evaporator However, if this flag is True, then an alternate, CESEC compatibility model computes the degradation as a function of the total liquid mass in the steam generator, as follows. When the total mass is < SGSMASSZEROTUBEAREA, then the heat transfer is completely degraded (zero). When the total mass is > SGS_MASSFULL.TUBEAREA, there is no degradation. When the total mass is between these two masses, the degradation is linearly interpolated. This model should not be used in realistic calculations, but only when it is required to match the CESEC methodology. Therefore, SGS_TUBEAREAOPTION should be False in the basedeck, independently of plant design. If it is True, then the two mass parameters are dependent on the SG design but in reality they are assigned the values used in CESEC Reference 1, Appendix E



Index Long Variable Name -, Input System System System Variable's, T±fe Dlmen- Definition , --. . No. Output Alt. 1 Alt. 2 Function _ slons - -. .,____

1890 SGS_MASSFULLTUBEAREA Input SO RE 4 Minimum mass for full SG secondary-side tube heat transfer. Used Lbm in conjunction SGS_MASS_ZERO_TUBE_AREA, but only if the flag

SGSTUBEAREA_OPTION is True. In that case, a "CESEC compatibility" model computes the degradation of SG heat transfer as a function of the total liquid mass in the steam generator, as follows. When the total mass is < SGS_MASS_ZERO_TUBEAREA, then the heat transfer Is completely degraded (zero). When the total mass Is > SGS_MASS_FULLTUBEAREA, there is no degradation. When the total mass is between these two masses, the degradation is linearly interpolated. This model should not be used in realistic calculations, but only when it Is required to match the CESEC methodology. Therefore, SGSTUBEAREAOPTION should be False in the basedeck, Independently of plant design. If it is True, then the two mass parameters are dependent on the SO design but In reality they are assigned the values used in CESEC. Reference 1, Appendix E.

1891 SGSMASSZERO_TUBEAREA Input SO RE 4 Mass for zero SO secondary-side tube heat transfer. Used In Lbm conjunction SGS_.MASSFULLTUBEAREA, but only If the flag SGSTUBE_AREAOPTION Is True. In that case, a "CESEC compatibility" model computes the degradation of SO heat transfer as a function of the total liquid mass In the steam generator, as follows. When the total mass Is < ' SGSMASSZEROTUBEAREA, then the heat transfer is completely degraded (zero). When the total mass Is > SGS_MASS_FULL_IUBE_AREA, there is no degradation. When the total mass is between these two masses, the degradation is linearly interpolated. This model should not be used In realistic calculations, but only when it is required to match the CESEC methodology. Therefore, SGSTUBE_AREAOPTION should be False In the basedeck, independently of plant design. If it Is True, then the two mass parameters are dependent on the SG design but in reality they are assigned the values used In CESEC. 1 Reference 1, Appendix E.

1892 FWS-ENTHTABLE Partition RE 50 Table of main feedwater enthalpy vs load Partition

1893 FWSHTABLEENTH Input SO FW RE 20 Table: MFW norm enthalpy, (h-H1)/(H2-H1), where H1 & H2 refer to Dimensionless CTL.FWSJ_H(1,2). Used for NUMFWSPUMPS--0 only. Reference 1, Section 6.7.3

1894 FWSHTABLELOAD Input SG FW RE 20 Table: turbine normalized load, WlWrated. Used In conjunction with Dimensionless FWSHTABLEENTH. Used for NUM_FWS_PUMPS=0 only. Reference 1, Section 6.7.3.

1895 FWS_HTABLENUM Input SO FW IN Table: number of entries for the FW enthalpy vs. load table. Used Counts

I__P ___for NUM FWSPUMPS--- only. Reference 1, Section 6.7.3. 1 1

1905 MSLH2 STATE Partition MSLH RE 40 Steamline Header, node 2, state output variables. Partition



index Long Variable Name Input System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

1906 MSLH2_CONIO Output MSLH Solutes RE Steamline Header, node 2, Iodine concentration. Reference 1, Microcurie/bm Sections 5 6 and 7 3 3

1907 MSLH2_CONPT Output MSLH Solutes RE Steamline Header, node 2, particulates concentration. Reference 1, Microcune/libm I_ I Sections 5 6 and 7.3 3

1908 MSLH2_CONXE Output MSLH Solutes RE Steamline Header, node 2, xenon concentration. Reference 1, Microcune/Ibm Sections 5.6 and 7.3.3.

1909 MSLH2_DVDH Output MSLH T/H State RE Steamline Header, node 2, partial derivative of specific volume wrt Composite enthalpy Reference 1, Sections 5 6 and 7 3 3 Units

1910 MSLH2_DVDP Output MSLH T/H State RE Steamline Header, node 2, partial derivative of specific volume wrt Composite pressure Reference 1, Sections 5.6 and 7 3 3 Units

1911 MSLH2 H Output MSLH T/H State RE Steamline Header, node 2, enthalpy. Reference 1, Sections 5.6 BtuAbm and 7 3 3.

1912 MSLH2_HF Output MSLH T/H State RE Steamline Header, node 2, saturated liquid enthalpy. Reference 1, Btu/lbm Sections 5 6 and 7.3 3.

1913 MSLH2_HG Output MSLH T/H State RE Steamline Header, node 2, saturated steam enthalpy Reference 1, Btu/lbm ,Sections 5 6 and 7.3 3

1914 MSLH2_M Output MSLH TIH State RE Steamline Header, node 2, mass. Reference 1, Sections 5 6 and Lbm 733

1915 MSLH2_ML Output MSLH TIH State RE Steamline Header, node 2, liquid mass Reference 1, Sections 5 6 Lbm and 73 3

1916 MSLH2_P Output MSLH T/H State RE Steamline Header, node 2, pressure Reference 1, Sections 5.6 Psia and 7 3 3

1917 MSLH2_Q Output MSLH T/H State RE Steamline Header, node 2, coolant-to-wall heat rate. Reference 1, Btu/sec Sections 5 6, 7 3 3 and 7 4

1918 MSLH2_0_ATM Output MSLH T/H State RE Steamline Header, node 2, wall-to-atmosphere heat rate. Btu/sec Reference 1, Sections 5 6, 7.3.3 and 7.4.

1919 MSLH2_SV Output MSLH T/H State RE Steamline Header, node 2, specific volume Reference 1, Sections Ft3 Abm 1 ._ 5 6 and 7.3 3

1920 MSLH2_SVF Output MSLH T/H State RE Steamline Header, node 2, saturated liquid specific volume Ft3/Ibm Reference 1, Sections 5.6 and 7 3 3

1921 MSLH2SVG Output MSLH T/H State RE Steamline Header, node 2, saturated steam specific volume. Ft3 /bm Reference 1, Sections 5 6 and 7 3 3

1922 MSLH2_T Output MSLH T/H State RE Steamline Header, node 2, temperature Reference 1, Sections 5.6 Degree F and 7.3.3.

1923 MSLH2_TWALL Output MSLH T/H State RE Steamline Header, node 2, pipe metal temperature. Reference 1, Degree F

I__II Sections 5 6 and 7 3.3

1924 MSLH2YX Output MSLH T/H State RE Steamline Header, node 2, quality. Reference 1, Sections 5.6 and Fraction 7.3 3

1925 CONTROL COMMON Segment RE 5120 Control, protective, and bop systems Segment

1926 CTL TIME STEP Output Control CTL SETPT RE Time step length available to controllers. Seconds

1927 CTL CORE CONTROL Partition RE 110 Core control partition Partition 1928 CTL CORE SETPOINTS FORTRIP Partition , I RE 45 Partition for RPS setpoints Partition


Table G.A: Dictionary Listingi IVmInput Sytem System System Variable's ; Type Dlmen- Definitionunis : .- ,..

Index Long Variable Name,,...... Definition,!--,, • ... ,:'i

SNo. o , Output . AIt. 1 Alt. 2 Function .. slons

1929 CTLCOREHI_POWER_FRACTRIP Input Control RPS RE Hi power fraction scram setpoint. Reference 1, Section 6.1. Fraction CTLSETPT _

1930 CTLCORE-HI-POWERSURTRIP Input Control RPS RE High power SUR scram setpoint. Reference 1, Section 6.1. Decades/min

I CTLSETPT 1931 CTLCORELOWPRZRPRESTRIP Input Control RPS RE Low pressurizer pressure scram setpoint. Reference 1, Section 6.1. Psia

CTLSETPT 1932 CTLCORE_HI_PRZR_PRES_TRIP Input Control RPS RE High pressurizer pressure scram setpoint. Reference 1, Section 6.1. Psla

CTLSETPT 1933 CTLCORE_HI_PRZRLEVELL_TRIP Input Control RPS RE High pressurizer level scram setpoint. Reference 1, Section 6.1. Fraction

CTL.SETPT

1934 CTLCOREOVER_TEMPMRGNTRIP Input Control RPS RE Thermal margin setpts for over temp trip. Reference 1, Section 6.1. Del-degF CTLSETPT --_

1935 CTLCOREOVERPOWERMRGNTRIP Input Control RPS RE Thermal margin setpts for over pwr trip. Reference 1, Section 6.1. Del-degF CTLSETPT

1936 CTLCORERCSFLOW_FRACTRIP Input Control RPS RE Low loop flow scram setpoint. Reference 1, Section 6.1. Fraction CTLSETPT

1937 CTLCORESIAS_TRIP Input Control RPS RE Scram due to SIAS - general purpose setpolnt. Reference 1, Fraction I 1 _ _, _ _ , -__ 1 _ I CTLSETPT Section 6.1. 1, j

1938 CTLCORELOWSG_PRES_TRIP Input Control RPS RE Low SG pressure scram setpoint. Reference 1, Section 6.1. Psia CIL SETPT I11

1939 CTLCORELOWSGLEVELTRIP Input Control RPS RE Low SG level scram setpolnt. Reference 1, Section 6.1. Fraction CTLSETPT

1940 CTLCOREHISG_LEVELTRIP Input Control RPS RE High SG level scram setpoint. Reference 1, Section 6.1. Fraction

_CTLSETPT _

1941 CTL_STEAMFEEDMISMATCHTRIP Input Control RPS RE Steam-feed flow mismatch scram setpoint. Reference 1, Section Lbm/sec CTLSETPT 6.1.

1942 CTLCORE_TURB_TRIP..DELAY Input Control RPS RE Scram due to turb trip: time delay. Reference 1, Section 6.1. SecondsCTLSETPT

1943 CTLCOREHI_CONT_PRES_TRIP Input Control RPS RE High containment pressure scram setpoint. Reference 1, Section Psia

CTLSETPT _6.1.

1944 CTLCOREUSERFDEFINED_TRIP Input Control RPS RE 10 Space for other scram setpoints. Reference 1, Section 6.1. Undefined

CTL SETPT 1

1945 CTLRCP_.FLOWSTPOINT Output Control RPS RE 5 Low primary flow scram setpoints. These are calculated setpoints: Lbm/sec CTL.SETPT for each RCP, this is CTLCORE_RCSFLOW_FRAC_TRIP * rated

volumetric flow * rated density. The last value in this array (at NUMPUMPS+1) is the sum of the RCPs' flow setpotnts. Reference 1, Section 6.1.

1946 CTLCOREHIPOWER_..SURBYPS Input Control RPS RE 2 HI power SUR scram-inhibit setpoints. Reference 1, Section 6.1. Fraction

I__ I_ CTLSETPT 1

1947 CTLCOREPOWERRATIO Output Control RPS RE Logarithmic rate of power change. Independent of plant design. Dimensionless

CTL SETPT Reference 1, Section 6.1.

1948 CTLSTEAMFEED_MISMATCHBYPS Input Control RPS RE Scram on flow mismatch: Inhibit setpoint. Reference 1, Section 6.1. Fraction

I__ _CTLSETPT_



Index Long Variable Name Input System System System Variable's Type Dimen- Definition Units., , No. Output Alt. I Alt. 2 Function sions

1949 CTLCORETURB_TRIPBYPS Input Control RPS RE Scram on turbine trip. inhibit setpoint. Reference 1, Section 6.1. Lbm/sec CTL SETPT

1950 CTLCOREUSERDEFINEDBYPS Input Control RPS RE 10 Space for other scram inhibit setpoints. Reference 1, Section 6.1. Undefined CTL SETPT

1951 CTLCORE TRIP OR Partition I RE 25 Partition for scram overrides Partition 1952 CTLCORE_HIPOWERFRACTRIPOR Input Control RPS RE Hi power fraction scram override. 0=Normal; 1 -Ovemde. User Overnde

CTL_SETPT determines based on trips desired to be active. Reference 1, Normal Section 6 1

1953 CTLCOREHI_POWERSURTRIPOR Input Control RPS RE High power SUR scram override. 0=Normal; I=Override. User Override CTL_SETPT determines based on trips desired to be active. Reference 1, Normal

Section 6.1. 1954 CTLCORELOW_PRZR_PRES_TRIPOR Input Control RPS RE Low pressunzer pressure scram override. O=Normal; 1=Override. Override

CTLSETPT User determines based on tnps desired to be active. Reference 1, Normal _Section 6 1.

1955 CTLCORE_HIPRZRPRESTRIPOR Input Control RPS RE High pressurizer pressure scram override. O=Normal; 1 =Override. Override CTLSETPT User determines based on trips desired to be active. Reference 1, Normal

I_ _Section 6.1. 1956 CTLCOREHIPRZRLEVELTRIPOR Input Control RPS RE High pressurizer level scram overrides. O=Normal, 1 =Override. Override

CTL_SETPT User determines based on trips desired to be active Reference 1, Normal I_ ISection 6 1

1957 CTLCOREOVER_TEMPMRGN-TRIPOR Input Control RPS RE Over-temp thermal margin scram override. O=Normal, 1=Override Override CTLSETPT User determines based on trips desired to be active. Reference 1, Normal

Section 6 1. 1958 CTLCOREOVERPOWERMRGNTRIPOR Input Control RPS RE Over-power thermal margin scram override. 0=Normal, Override

CTLSETPT I =Override. User determines based on trips desired to be active. Normal I Independent of plant design Reference 1, Section 6 1.

1959 CTL._CORERCSFLOW_FRACTRIPOR Input Control RPS RE Low loop flow scram override. 0=Normal, 1 =Override. User Override CTL_SETPT determines based on trips desired to be active. Independent of Normal

plant design Reference 1, Section 6.1 1960 CTL_CORE_SIASTRIPOR Input Control RPS RE Scram due to SIAS override 0=Normal; 1 =Override. User Override

CTLSETPT determines based on trips desired to be active. Independent of Normal I__ plant design. Reference 1, Section 6.1.

1961 CTLCORELOWSGPRESJRIPOR Input Control RPS RE Low SG pressure scram override. 0=Normal; 1=Override. User Override CTL_SETPT determines based on trips desired to be active. Independent of Normal

plant design Reference 1, Section 6 1. 1962 CTLCORELOWSGLEVELTRIPOR Input Control RPS RE Low SG level scram override O=Normal; I=Override. User Override

CTL_SETPT determines based on trips desired to be active. Independent of Normal plant design. Reference 1, Section 6.1.

1963 CTL_CORE_HI_SG_LEVEL_TRIP_OR Input Control RPS RE High SG level scram override. 0=Normal, 1=Override. User Override CTLSETPT determines based on trips desired to be active. Independent of Normal

I _plant design. Reference 1, Section 6.1. 1964 CTLSTEAM_FEEDMISMATCHTRIPOR Input Control RPS RE Steam-feed flow mismatch scram override. 0=Normal; 1 =Override. Override

CTLSETPT User determines based on trips desired to be active Independent Normal ____ I__ _of plant design. Reference 1, Section 6.1.



Index Long Variable Name , Input System System System Variable's. Tvlye Dimen- Definition Unlts-,:,"__ . ..... " Output Alt. 1 Alt. 2 Function sions

1965 CTLCORETURBTRIPDELAYOR Input Control RPS RE Scram due to turb trip: override. 0=Normal; 1 =Override. User Override CTLSETPT determines based on trips desired to be active. Independent of Normal

_ _plant design. Reference 1, Section 6.1.

1966 CTLCORE_HICONTPRESTRIP_OR Input Control RPS RE Hi cont. pressure scram override. O=Normal; 1=Override. User Override CTLSETPT determines based on trips desired to be active. Independent of Normal

plant design. Reference 1, Section 6.1.

1967 CTLCOREUSERDEFINEDTRIPOR Input Control RPS RE 10 Space for other scram overrides. O=Normal; 1=Override. User Override CTLSETPT determines based on trips desired to be active. Independent of Normal

plant design. Reference 1, Section 6.1.

1968 CTLTIMECORETRIP Output Control RPS RE Time elapsed after scram. Always used. Independent of plant Seconds CTLSETPT design.

1969 CTLCOREPOWER Output Control RPS RE Core power. Always used. Independent of plant design. Btu/sec CTLSETPT "___

1970 CTLQCORETRIP Output Control RPS RE Core power at time of trip. Always used. Independent of plant Btufsec _CTL SETPT design.

1971 CTLCOREPOWERFRACTION Output Control RPS RE Core power, fraction of rated. Always used. Independent of plant Fraction _CTLSETPT design.

1972 CTLCOREPOWER_FRACLAST Output Control RPS RE Core power fraction, at last time step. Always used. Independent Fraction CTLSETPT of plant design.

1973 CTLNUMRPS Input Control RPS IN Number of RPS channels. Always used. Independent of plant Counts CTLSETPT _ design. Reference 1, Section 6.1.

1974 CTLCORECONTROLAUTO Input Control RPS LO Flag: automatic control of core. This flag is set by the User. True Auto Manual CTLSETPT (Auto) indicates that the RPS controllers are actively set to provide

a trip, if a trip conditions develops. False (Manual) is used to override all RPS trip function controllers. Only a manual trip is available In that case (User sets CTLCORETRIP= T). Always used. Independent of plant design. Reference 1, Section 6.1.

1975 CTLCORETRIP I/O Control RPS LO Core tnpped flag. This flag Is set by the User or by CENTS. To Trip- Normal CTLSETPT simulate a manual trip the User can set CTLCOREJRIP= T via

the command tile or CENTS can set the flag to True if the RPS controllers indicate a trip condition. Always used. Independent of Ilant design. Reference 1, Section 6.1.

1976 CTL.CORETRIPSIG Output Control RPS LO 25 Scram signals. The scram channel that energizes first becomes Active CTLSETPT True in this array. All other scram channels are prevented from Inactive

becoming True, even if the channel energizing condition exists. Thus, the condition that caused the Scram can be interrogated at a later time. Reference 1, Section 6.1.

1977 CTL_CORE_PTRIP Output Control RPS LO Scram signal at last time step. True False CTLSETPT 1 1

1978 CTLCEACOMMON Partition RE 20 Control-element assembly model Partition

1979 CTLCEASETPOINTS Partition RE 6 Setpoints for reactor regulating system Partition

1980 CTLCEATREF._NO Input Control CEA RE Reference (avg) primary temp at no load. Reference 1, Section 6 8. Degree F

I____ ___CTL-SETPT I II



Index Lonq Variable Name Input / System System System Variable's Type Dimen- Definition Units No. output Alt. 1 Alt. 2 Function slons

1981 CTLCEATREFFULL Input Control CEA RE Reference (avg) primary temp, full load. Reference 1, Section 6.8. Degree F CTL SETPT

1982 CTLCEAGAINEXP Input Control CEA RE Exponent for nonlinear gain=demand'*exp Used always. In the Dimensionless

CTLSETPT Control Rod Regulating System of Westinghouse-designed plants, the temperature error logic contains a nonlinear gain term, CTLTURBDEMAND**CTL_CEA_GAINEXP, where the first factor is the current turbine power demand. The resultant value, CTLCEA_TURBLDGAIN, is used by the modeler via the Generic Control System. CTL_CEAGAIN EXP is dependent on the plant control system design, in many Westinghouse-designed plants. Reference 1, Section 6 8

1983 CTLCEATURBLD-GAIN Output Control CEA RE Nonlinear gain for Control Rod Regulating System of Dimensionless CTL_SETPT Westinghouse-designed plants. Used calculated The temperature

error logic of the CRRS contains a nonlinear gain term, CTLTURBDEMAND*CTL_CEA.GAINEXP, where the first factor is the current turbine power demand. The resultant value, CTLCEATURBLDGAIN, is used by the modeler via the Generic Control System Reference 1, Section 6.8

1984 CTLCEAPOSITIONFRAC Output Control CEA RE Fractional average rod position. 0.0=fully inserted, 1 0= fully Fraction CTL SETPT withdrawn. Always used Independent of plant design

1985 CTLCEALASTTIME Output Control CEA RE CEA motion time - the time at which the rods last moved Seconds CTL SETPT

1986 CTLCEAMAX Input Control CEA RE Maximum CEA withdrawal position. Steps CTL-SETPT

1987 CTL_CEA_MIN Input Control CEA RE Minimum CEA withdrawal position Steps CTL SETPT

1988 CTLCEAPOS Input Control CEA RE CEA withdrawal position Used always CTLCEAPOS is the Steps CTLSETPT current position of the "average" control rod, measured in steps with

zero at the fully inserted point (bottom). When the Reactor Regulating System is active, CTL_CEA_POS is calculated, based on rod speed signal received from the GCS controller. The power algorithm then determines the rod reactivity based on the current rod position CTL.CEAPOS. This variable is dynamic, independent of plant design

1989 CTLCEASPEED I/O Control CEA RE CEA motion speed and direction Reference 1, Section 6.8. Steps/min CTL SETPT

1990 CTLCEASTEP Input Control CEA RE Step size of control rod motion. Used always. This parameter is Inches CTL_SETPT the step size of control rod motion, in inches. This parameter is

dependent on plant design Reference 1, Section 6 8 1991 CTLCEAAUTO Input Control CEA LO Flag, Auto/Manual CEA (reactor regulating) control. If Auto, the True False

I I _CTL SETPT I _I __controller logic dnves the regulating rods. Reference 1, Section 6 8

WCAP- 15996-NP, Revision 0 G- 151

Table G.A: Dictionary Listing Index Lon. Variable Name, T S Sl ype Dimen- Definition Units

No. Output Alt. 1 Alt. 2 - Function , slons .. ,

1992 CTLCEAPERFECT Input Control CEA LO Flag: CEA perfect controller. If True, creates a fictional perfect CEA True False

CTLSETPT controller that continually positions the control rods where they will exactly match the other reactivity components, thus ensuring a

steady power state. Reference 1, Section 6.8.

1993 CTL,_CEAACCUM Output Control CEA RE CEA control accumulated signal. Reference 1. Section 6 8. Steps

CTLSETPT

1994 CTL_CEA.._SPEED._LAST Output Control CEA RE CEA speed and direction, last step. Steps/min

CTLSETPT

1995 CTL CVCSCOMMON Partition RE 85 Chemical & volume control system Partition

1996 CTLPRZRLEVEL.SETPOINTS Partition RE 9 Pressurizer level setpoints Partition

1997 CTLPRZRPLEVELTEMP Input Control CVCS RE 2 Pressurizer level-program temperature setpoints. These Degree F

CTL.SETPT parameters are dependent on plant design. Normally based upon RCS average temperature. These parameter values allow a variable program pressurizer level at different core power levels.

Reference 1, Section 6.2.

1998 CTLPRZR_PLEVEL Input Control CVCS RE 2 -Pressurizer level-program level setpoints. These plant dependent Fraction

CTLSETPT setpoints are determined in conjunction with CTLPRZRPLEVELTEMP. They allow the pressurizer level to vary with power (or average RCS temperature). The units are most often set to a fraction of level span, but that can vary depending on

how the level controller are established. Reference 1, Section 6.2.

1999 CTLPRZRLIQ0SPVOL REF Input Control CVCS RE Pressurizer Instrument reference liquid specific-volume. This plant FteAbm

CTLSETPT dependent variable is based on the pressurizer liquid temperature and pressure at the time of the level instrument calibration. Normally it is set to saturated conditions for normal operating pressure, since this is the most likely state during calibration. Reference 1, Section 6.2.

2000 CTLPRZRSTMSPVOLREF Input Control CVCS RE Pressurizer instrument reference steam specific-volume. This plant Ft3 /lbm

CTLSETPT dependent variable Is based on the pressurizer steam temperature

and pressure at the time of the level instrument calibration. Normally it is set to saturated conditions for normal operating

pressure, since this is the most likely state during calibration.

Reference 1, Section 6.2.

2001 CTLVLETDOWN.SETPOINTS Partition RE 6 Letdown control setpoints Partition

2002 CTLCVCSLDNZSPOINT Input Control CVCS RE 2 Letdown level control setpoints. These plant dependent setpoints Fraction

CTLSETPT are based upon a deviation from the pressurizer program level. The

units may be a fraction of span or In feet, Inches etc., depending on

how the controllers are established. Reference 1, Section 6.2.

2003 CTL.CVCSLDNW_GPM Input Control CVCS RE 2 Letdown flow setpoints. These plant dependent setpomnts are used GaVmin

CTL_SETPT in conjunction with CTLCVCSLDN_ZSPOINT, based upon a

deviation from the pressurizer program level. They set the letdown

flow rate based on the calculated pressurizer level error. Reference

-__ _ 1, Section 6.2.

2004 JCTLS.HARGING SETPOINTS Partition RE 15 Charging pump control setpoints Partition



Index Long Variable Name Input/ System System System Variable's Type. Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function sions

2005 CTLCVCS_CHI_SPOINT Input Control CVCS RE 2 Charging pump 1 control setpoints. Reference 1, Section 6.2. Fraction

CTL SETPT 2006 CTLCVCSCH2_SPOINT Input Control CVCS RE 2 Charging pump 2 control setpoints. These plant dependent Fraction

CTLSETPT setpoints are based upon a deviation from the pressurizer program level. The units may be a fraction of span or in feet, inches etc, depending on how the controllers are established Reference 1, Section 6 2.

2007 CTLCVCSCH3_SPOINT Input Control CVCS RE 2 Charging pump 3 control setpoints. These plant dependent Fraction

CTL SETPT setpoints are based upon a deviation from the pressurizer program level. The units may be a fraction of span or in feet, inches etc, depending on how the controllers are established. Reference 1, Section 6 2.

2008 CTLCVCSCH4_SPOINT Input Control CVCS RE 2 Charging pump 4 control setpoints. These plant dependent Fraction CTLSETPT setpoints are based upon a deviation from the pressurizer program

level. The units may be a fraction of span or in feet, inches etc., depending on how the controllers are established. Reference 1, Section 6 2

2009 CTLCHPUMP_W_RATED Input Control CVCS RE 4 Charging pump rated flow. These plant dependent variables are Gal/mmn CTLSETPT based on pump design. This parameter is established assuming

positive displacement charging pumps, though the controllers may be configured for variable flow is that is the pump design. In that case this array may have a different definition. Reference 1, Section

162 2010 CTLCVCSCONTROL Partition CVCS RE 24 CVCS control vanables Partition

I _CTL SETPT 2011 CTLPRZRPROGLEVEL Output Control CVCS RE Pressurizer programmed level This is the CENTS controller Fraction

CTLSETPT calculated variable based upon controller design and the setpoint values for CTLPRZR_PLEVELTEMP & CTL_PRZR_PLEVEL It is the desired steady state pressurizer level for a given average RCS temperature. The units may be a fraction of span or in feet, inches etc , depending on how the controllers are established. Reference 1, Section 6 2

2012 CTLPRZRLEVELERROR Output Control CVCS RE Pressurizer level error. This is the CENTS controller calculated Fraction CTLSETPT variable measuring the deviation from CTLPRZRPROGLEVEL

The units may be a fraction of span or in feet, inches etc., depending on how the controllers are established. Reference 1, Section 6 2

2013 CTLPRZR_LEVELINST Output Control CVCS RE Pressurizer instrumentation level reading This CENTS calculated Feet CTLSETPT variable is dependent upon plant design and the transient plant

condition. It is calculated based on the tap locations, the time dependent water volume and density (vs. calibration densities), and the pressurizer segment area - height relationship. Reference 1, _Section 6.2.

2014 CTL_T_AVG Output Control CVCS RE Average primary coolant temperature. Calculated by the controller Degree F

_CTL SETPT CTL T AVG CONTROLLER Reference 2, Table 2



Inde.•3xi Long Variable Name Input System System System Variable's T jye Dlmen- Definition " . - Units No. _ _________________.__________ _ Output - Alt. 1 Alt. 2 Function sons

"2015 CTL.T_REF Output Control CVCS RE Demand reference temperature. Calculated by the controller Degree F CTLSETPT CTLTREFCONTROLLER. Reference 2, Table 2.

2016 CTLCH_PUMPFRAC I/O Control CVCS RE 4 Charging pump fractional flow. This variable Is set by the CENTS Fraction CTLSETPT controllers if the charging pumps are in automatic or by the code

User if the pumps are in manual control. Reference 1, Section 6.2; and Reference 2, Table 2.

2017 CTLCHPUMPAUTO Input Control CVCS LO 4 Flags: charging pumps automatic control. This variable array Is Auto Manual CTLSETPT independent of plant design. The code User may establish which of

the charging pumps are operated manually by user input and which pumps operate via the controller system. T = Auto; F = Manual. In manual, the user controls the pumps via CTLCHPUMPFRAC. The results are shown by CTLCH-FLOW. Reference 1, Section 6.2. -

2019 CTLLDNAUTO Input Control CVCS LO Flag: letdown automatic control. This variable Is Independent of Auto Manual CTLSETPT plant design. The code User may establish whether letdown is to

be operated manually by user input or operate via the controller system T = Auto; F = Manual. In manual, the User controls the letdown flow fraction via CTL_LDNFRAC. The results are shown in CTLLDNFLOW. Reference 1, Section 6.2.

2020 CTLCVCSRCSVALVES Partition RE 10 CVCS-RCS valve connections Partition

2021 CTLCHVFRAC Input Control CVCS RE 5 Fractional opening of charging valve. This plant Independent array Fraction CTLSETPT is established by the code User and used by CENTS, in conjunction

with CTL CHVFRAC, to determine where the charging flow enters the RCS. If all lines are of equal size, and the flow Is to be evenly split between the loops then the valve opening fractions would be set to equal fractions, totaling 1.0 Reference 1, Section 6.2.

2022 CTLCHV RAREA Input Control CVCS RE 5 Charging valve relative flow areas. This plant dependent array Is Dimensionless CTL._SETPT used by CENTS In conjunction with CTL_CHV_FRAC to determine

where the charging flow enters the RCS. The all lines are of equal _size then the array would all be set to 1.0 Reference 1, Section 6 2.

2023 CTLCVCSTH VARIABLES Partition RE 15 CVCS thermal-hydraulic variables Partition

2024 CTLHAREGHEATX Input Control CVCS RE Regen. heat exchanger overall ht coeff. This plant dependent heat Btu/sec-degF CTLSETPT transfer variable is calculated In the basedeck calculations. The

equation used is hA = 2*Wch*Cp*(Tchout - Tchin)/(TIdnln + Tidnout Tchout - Tchin). Reference: Individual Basedeck Calculations.

Reference 1, Section 6 2.

2025 CTL_LDN_FLOW Output Control CVCS RE Letdown mass flow rate. This is a CENTS calculated output based Lbm/sec CTLSETPT upon controller operation or User defined Input, if in manual control.

I__J__ Reference 1, Section 6.2.

2026 CTL LDNT Output Control CVCS RE 2 Letdown temperature at RHEX Inlet/exit. These two temperatures Degree F CTLSETPT are CENTS calculated output based upon charging flow, letdown

I_ I _ _ IIflow and CTLHAREGHEATX. Reference 1, Section 6.2.



Index Long Variable Name Input/ System System System Variable's Type Dimen- Definition Units NOutput Alt. 1 Alt. 2 Function slons

2027 CTL_LDN_H Output Control CVCS RE 2 Letdown enthalpy at RHEX inlet/exit These two enthalpies are Btu/lbm CTL_SETPT CENTS calculated output based upon CTLLDN_T and system

_ pressure Reference 1, Section 6 2. 2028 CTLLETDOWNFRAC I/O Control CVCS RE 4 Letdown flow fraction. This is a CENTS calculated output based Fraction

CTLSETPT upon controller operation or User defined input, if in manual control. Reference 1, Section 6 2; and Reference 2, Table 2

2029 CTL_CH_FLOW Output Control CVCS RE Total charging pumps delivery This is a CENTS calculated output Lbm/sec CTLSETPT based upon the number of pumps running due to controller

operation or User defined input, if in manual control. Note that this is the variable which is printed for charging flow in the standard output. However, this value is only correct if CTLCHV_RAREA & CTL_CHV_FRAC contain non-zero values Other charging flow variables are P_FLOW(105.108) or RCSCHGS FLOW. Reference 1, Section 6 2

2030 CTLCHT I/O Control CVCS RE 2 Charging temperature at RHEX inlet/exit. CTL.CH_T(1) is the input Degree F CTLSETPT temperature at the RHEX inlet. CTLCHT(2) is calculated by

CENTS based upon charging flow, letdown flow and CTL HA REG HEAT X Reference 1, Section 6 2.

2031 CTL_CH_H I/O Control CVCS RE 2 Charging enthalpy at RHEX inlet/exit. CTL_CH_.H1) is the input BtuAbm CTLSETPT enthalpy at the RHEX inlet CTLCHH(2) is calculated by CENTS

based upon CTLCHT(2) and system pressure. Reference 1, I Section 6 2

"2032 CTLHEATERSCONTROL Partition RE 18 Heaters control partition Partition 2033 CTL PRZR HEATER SETPOINTS Partition RE 10 Heater control setpoints Partition 2034 CTL PRZRBHLEVELSPOINT Input Control HTR RE 2 Pressurizer heaters high-level on/off setpoints. These plant Fraction

CTL SETPT dependent setpoints establish when pressurizer heaters come on and reset due to a high program level error condition The units may be a fraction of span or in feet, inches etc , depending on how the controllers are established. Reference 1, Section 6 3

2035 CTLLEVEL_HEATER_OFF Input Control HTR RE Heaters low-level cutoff setpoint. This plant dependent setpoint Fraction CTLSETPT establishes when pressurizer heaters come on and reset due to a

low level condition which could uncover the heaters The units may be a fraction of span or in feet, inches etc , depending on how the controllers are established. Reference 1, Section 6 3.

2036 CTLPRES_PHEATEROFF Input Control HTR RE Proportional heaters high pressure setpoint. This plant dependent Psia CTLSETPT pressure setpoint establishes when pressurizer proportional heaters

are totally off due to pressure above CTLPRZRREFPRES. Reference 1, Section 6 3

2037 CTL_PRES_PHEATERON Input Control HTR RE Proportional heaters low pressure setpoint. This plant dependent Psia CTLSETPT pressure setpoint establishes when pressurizer proportional heaters

are fully on due to pressure below CTLPRZRREFPRES. Reference 1, Section 6 3



Index Long Variable Name, Input/ System System System Variable's Type Dlmen- Definition - Units

No. __ __ _ __ __ _Output Alt. 1 Alt 2 Function slons

2038 CTLPRES_BHEATER_OFF Input Control HTR RE Backup heaters high pressure setpoint. This plant dependent Psla

CTLSETPT pressure setpoint establishes when pressurizer backup heaters are off due to pressure above CTL_PRZRREF_PRES. Reference 1,

,__Section 6.3.

2039 CTLPRESBHEATERON Input Control HTR RE Backup heaters low pressure setpolnt. This plant dependent Psia CTLSETPT pressure setpolnt establishes when pressurizer backup heaters are

on due to pressure above CTL_PRZRREF_PRES. Reference 1, _,_ Section 6.3.

2040 CTLPRZRREFPRES Input Control HTR RE Reference pressure for pressurizer pressure control. This plant Psia

CTLSETPT dependent pressure Is the desired steady state reference pressurizer pressure. Heater and spray on/off setpolnts are all based upon pressure deviations from this reference. Reference 1,

I Section 6 3.

2041 CTLVOLTPROP I/O Control HTR RE Proportional heaters voltage. This is the CENTS calculated output Volts CTLSETPT which determines the extent to which the proportional heaters are

energized. If this voltage is compared to CTLPRZRHEATERSVOLT, then the fraction of full heater output can be determined. CENTS uses this voltage in conjunction with

- RESIHEATER to determine the power or heat being generated by the proportional heaters. Reference 1. Section 6.3.

2042 CTLVOLTBACK I/O Control HTR RE Backup heaters voltage. This is the CENTS calculated output Volts

CTL.SETPT which determines whether the backup heaters are energized. Since backup heaters are either full on or off, this voltage is either zero or equal to CTLPRZR_HEATERS_VOLT. CENTS uses this voltage in conjunction with RESIHEATER to determine the power or heat being generated by the backup heaters. Reference 1, Section 6 3

2043 CTLPRZRHEATERSVOLT Input Control HTR RE Pressurizer heaters rated voltage. This plant dependent voltage Is Volts

CTL.SETPT used as the reference voltage for fully energized heaters. Heater voltage and resistance are used by CENTS to calculate the heater power or heat input Into the system. Reference 1, Section 6.3

2044 CTLHEATERSCONTROLAUTO Input Control HTR LO Flag: automatic ctrl of pressurizer heaters. This Is a plant Auto Manual

CTLSETPT independent, User defined input. In T=Auto, the controller output dictates heater operation. In F=Manual, the User controls heater operation via setting CTLVOLT-PROP and CTLVOLTBACK. The results are shown by bank as HEAT_HEATER or as a total of all heaters In HEATPRZR. HEAT_ELEC Is the array which Indicates the electric heat being generated. Reference 1, Section

_____ _____6.3

2045 CTLPRZRSPRAYCONTROL Partition I RE 5 Pressurizer main spray controls Partition

2046 CTLJPRZR SPRAY SETPOINTS Partition RE 4 Pressurizer spray control setpoints Partition



Index Long Variable Name Input/ System System System Variable's Tye Dlmen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

2047 CTLPRZRSPRAYPRESON Input Control SPRY RE Pressurizer spray control high-pressure on-setpoint. This plant Psia CTLSETPT dependent setpoint is based on a deviation from

CTLPRZRREFPRES. It may be used by the controllers as either the setpoint for full open spray valves or as a point where spray valves start to open The exact definition is based entirely on how the spray controller is designed Reference 1, Section 6 3.

2048 CTLPRZRSPRAYPRESOFF Input Control SPRY RE Pressurizer spray control low-pressure off-setpoint This plant Psia CTLSETPT dependent setpoint is based on a deviation from

CTIPRZRREFPRES. It may be used by the controllers as either the setpoint for fully shutting spray valves It may also be the setpoint where spray valves start to open The exact definition is based entirely on how the spray controller is designed Reference 1, Section 6 3

2049 CTLPRZRSPRAYCONTROLAUTO Input Control SPRY LO Flag automatic control of pressurizer spray. This is a plant Auto Manual CTLSETPT independent, User defined input. In T=Auto, the controller output

dictates pressurizer spray operation In F=Manual, the User controls spray operation via setting VLV_PRZR_MSPRAYSIG(J) The results are shown by PFLOW SPRAY Reference 1, Section 6 3

2050 CTL PRESSURIZER RELIEF Partition I RE 26 Pressurizer PORV and SV control variables Partition

2051 CTL PRZR RELIEF SETPOINTS Partition RE 20 Pressurizer relief and safety valve setpoints Partition

2052 CTLPORVPSET Input Control PZRRELIE RE 4 PORV opening pressure setpoints. This is the plant dependent Psia F_SETPT setpoint at which the PORVs just begin opening on an increasing

pressure scenario. Reference 1, Section 6 3 2053 CTLPSVPSETOPEN Input Control PZRRELIE RE 4 Pressunzer safeties full-open setpoints This is the plant dependent Psia

F_SETPT setpoint at which the PSVs are fully open on an increasing pressure scenario. This pressure is usually the opening setpoint plus accumulation pressure. Reference 1, Section 6 3

2054 CTL_PSVPSET_CLOSE Input Control PZR_RELIE RE 4 Pressurizer safeties opening setpoints This is the plant dependent Psia F_SETPT setpoint at which the PSVs just begin opening on an increasing

pressure scenario Reference 1, Section 6.3.

2055 CTLPSVPSETBLDN Input Control PZRRELIE RE 4 Pressurizer safeties re-closing setpoints. This Is the plant Psia F_SETPT dependent setpoint at which the PSVs are fully shut on a

decreasing pressure scenario This pressure is usually the opening pressure minus the amount of the valve blowdown. Reference 1, Section 6 3

2056 CTLPORVAUTO Input Control PZRRELIE LO 4 Flags: automatic control of PORVs This is a plant independent, Auto Manual

F_SETPT User defined input In T=Auto, the controller output dictates PORV operation In F=Manual, the User controls PORV operation via setting VLV_PRZRSIG(J). The results are shown by RCS_P_FLOW_PORV(J). Note that for plant with no PORVs, this variable is always set to F= Manual Reference 1, Section 6 3

2057 CTLSIS COMMON 1Partiton RE 200 Safety injection system Partition

2058 CTLSIASSETPOINTS Partition I II_ IRE 8 Safety injection syst setpoints Partition



Index Long Variable Name .. ""', Input/ SyS•tem Sstem System Variable's Typ Dimen- Definition ,Units , No. - - - 'Output Alt. 1 Alt. 2 Function slons

"2059 CTLSIASPRZRPRESLOW Input Control SIS RE Low pressure setpoint for SIAS. This Is the plant dependent Psla CTLSETPT pressurizer pressure setpoint which initiates a Safety Injection

Actuation Signal. Reference 1, Section 6 5. 2060 CTL_SIAS_SL_SHDP Input Control SIS RE Steamline flow trip setpoint. This plant dependent SIAS trip setpoint Psid

I II _CTLSETPT Is not used by any CE plant. Reference 1, Section 6.5.

2061 CTLSIASHICONTPRES Input Control SIS RE High containment press setpoint for SIAS. This is a plant Psia CTL_SETPT dependent setpoint. Note that CENTS does not model changes in

containment pressure, except as they are input by the user, possibly as a RAMP command In CEER. Reference 1, Section 6.5.

2062 CTLSIASLOWTAVG Input Control SIS RE Low temperature setpoint for SIAS. This plant dependent SIAS trip Degree F CTLSETPT setpoint Is not currently used by any CE plant. Reference 1, Section

6.5. 2063 CTLSIASLOWSLPRES Input Control SIS RE Low steamline pressure setpoint for SIAS. This plant dependent Psia

CTLSETPT SIAS trip setpoint is not currently used by any CE plant. Reference -1 Section 6 5.

2064 CTL SIS CONTROL Partition RE 150 Safety injection syst control variables Partition

2065 CTLHPSINPOINTS_TAB Input Control SiS IN No. of data points in the HPSI flow vs pressure table for each pump Counts CTLSETPT This number is dictated by the number of data points in a given

I___ I__ _lant's HPSI flow data. Maximum 15. Reference 1, Section 6 5. 1


Table G.1: Dictionary Listin2

Index Lonq Variable Name Input System System System Variable's Type Dimen- Definition Units No.___._ Output AIt. 1 Alt. 2 Function -•ons

2066 CTLHPSIFLOWTABLE Input Control SIS RE 45 Flows for HPSI flow-vs-pressure table. This is the plant dependent Gal/min CTLSETPT array of flow delivery values corresponding to the RCS pressures

given in CTLHPSIPRES_TABLE. This array supports multiple sets of flow data points (maximum total 45), with CTLHPSINPOINTSJAB points per set, corresponding to the number of operating HPSI pumps, CTLHPSIPUMPNUM.

If 1 pump, then the HPSI delivery is given by the first set of CTLHPSINPOINTSJAB flow values from this array, versus the pressures from CTLHPSI_PRESTABLE. If 2 pumps, then CENTS uses the second set of flow values from this array, versus the same set of back pressures as for 1 pump However, if this array contains only 1 set of flow values, then CENTS uses this set and multiplies by 2.

In general, for N pumps, CENTS uses the N'th set of flow values from this array, versus the same set of back pressures as for 1 pump However, if this array contains M sets of flow values, where M < N, then CENTS uses the M'th set and multiplies it by N/M.

Each set of flow values must be monotonic in a direction that is opposite to that of CTL_HPSI_PRES_TABLE. This array gives the total flow delivered by the HPSI pump(s) to all the injection points. The actual delivery to the RCS is then determined by the array CTL HPSISPLIT Note that the array of flow values will require adjustment for minimum or maximum HPSI flow, depending upon which set of values has been used in the input Reference 1, Section 6 5

2067 CTLHPSI_PRESTABLE Input Control SIS RE 15 Back pressure for HPSI flow-vs-pressure table. This is the plant Psia CTL_SETPT dependent array of injection point pressure values corresponding to

the HPSI flows given in CTLHPSIFLOWTABLE. Note that this pressure array is used for each of the flow data sets in CTLHPSIFLOWTABLE, dependent on the number of operable HPSI pumps. The pressures in this array must be monotonically increasing or monotonically decreasing. Reference 1, Section 6 5

2068 CTLHPSIPUMPNUM Input Control SIS IN Number of operating HPSI pumps This variable is set by the user, Counts CTLSETPT for the number of HPSI pumps that are available in the scenario

The number of available pumps determines which set of flow variables is used in CTL_HPSIFLOW_TABLE. If set to 1, then the first set of flow variables is used; if set to 2, then the second set is used, etc. However, if set higher than the number of flow sets that exist in CTL_HPSIFLOW_TABLE, then see the discussion for CTLHPSIFLOWTABLE. If set to 0, then the HPSI flow is 00. Reference 1, Section 6 5



Index Long Variable Name -A, Input System Sytem System Variable's Type Dimen- Definition ,.Units No. _ _ _ _ _ __Output Alt. 1 AIlt. 2 Function slons

2069 CTLHPSI_SPLIT Input Control SIS RE 8 HPSI flow split to injection points. This array, set by the user, Fraction CTLSETPT indicates what fraction of the total HPSI flow enters via each of the

SI connection to the RCS. Due to different line geometries and losses, the split fractions need not be equal. The total normally equals 1.0, but that Is not required. For example, If the total Is < 1.0, then the HPSI flow is correspondingly degraded. Reference 1,

___ Section 6.5.

2070 CTLLPSINPOINTSTAB Input Control SIS IN No of data points in the LPSI flow vs pressure table for each pump. Counts CTISETPT This number is dictated by the number of data points In a given

I plant's LPSI flow data. Maximum 15. Reference 1, Section 6 5.

2071 CTLLPSI_FLOW_TABLE Input Control SIS RE 45 Flows for LPSI flow-vs-pressure table. This is the plant dependent Gal/mln CTLSETPT array of flow delivery values corresponding to the RCS pressures

given in CTL_LPSIPRESTABLE. This array supports multiple sets of flow data points (maximum total 45), with CTL_LPSINPOINTSTAB points per set, corresponding to the number of operating LPSI pumps, CTLLPSI_PUMP_NUM:

If 1 pump, then the LPSI delivery Is given by the first set of "CTLLPSI_NPOINTSTAB flow values from this array, versus the pressures from CTL_LPSI_PRES_TABLE. If 2 pumps, then CENTS uses the second set of flow values from this array, versus the same set of back pressures as for 1 pump. However, if this array contains only 1 set of flow values, then CENTS uses this set and multiplies by 2. "In general, for N pumps, CENTS uses the N'th set of flow values from this array, versus the same set of back pressures as for 1 pump. However, if this array contains M sets of flow values, where M < N, then CENTS uses the M'th set and multiplies it by NIM.

Each set of flow values must be monotonic In a direction that is opposite to that of CTL_LPSIPRESTABLE. , This array gives the total flow delivered by the LPSI pump(s) to all the injection points. The actual delivery to the RCS is then determined by the array CTLLPSISPLIT. Note that the array of flow values will require adjustment for minimum or maximum LPSI flow, depending upon which set of values has been used in the

_input. Reference 1, Section 6.5.

2072 CTLLPSIPRESTABLE Input Control SIS RE 15 Back pressure for LPSI flow-vs-pressure table. This is the plant Psia CTLSETPT dependent array of injection point pressure values corresponding to

the LPSI flows given in CTLLPSI_FLOWTABLE. Note that this pressure array is used for each of the flow data sets in CTLLPSIFLOWTABLE, dependent on the number of operable LPSI pumps. The pressures in this array must be monotonically

-increasing or monotonically decreasing Reference 1, Section 6 5.



Index Long Variable Name Input/ System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function sions

2073 CTLLPSI_PUMPNUM Input Control SIS IN Number of operating LPSI pumps. This variable is set by the user, Counts CTLSETPT for the number of LPSI pumps that are available in the scenario.

The number of available pumps determines which set of flow variables is used in CTLLPSI_FLOW_TABLE. If set to 1, then the first set of flow variables is used, if set to 2, then the second set is used; etc. However, if set higher than the number of flow sets that exist in CTL_LPSI_FLOW_TABLE, then see the discussion for CTLLPSIFLOWJABLE. If set to 0, then the LPSI flow Is 0 0 Reference 1, Section 6.5.

2074 CTLLPSISPLIT Input Control SIS RE 8 LPSI flow split to injection points. This array, set by the user, Fraction

CTLSETPT indicates what fraction of the total LPSI flow enters via each of the Sl connection to the RCS. Due to different line geometnes and losses, the split fractions need not be equal. The total normally equals 1 0, but that is not required. For example, if the total is < 1 0, then the LPSI flow is correspondingly degraded Reference 1, Section 6 5

2075 CTLSIASTIME Output Control SIS RE Time elapsed since SIAS This variable is calculated by CENTS. Seconds CTL SETPT

2076 CTLSISDELAY Input Control SIS RE Sl pumps time delay after SIAS This plant dependent input Seconds CTLSETPT dictates the delay from time of SIAS until HPSVLPSI flow is

available. After this delay time has elapsed, then the flow is dictated by the pressure-flow tables. Reference 1, Section 6 5.

2077 CTLSIASCONTROLAUTO Input Control SIS LO Flag: automatic control of SIAS. This is a plant independent, User Auto Manual CTLSETPT defined input In T=Auto, the controller output dictates SIAS

operation In F=Manual, the User controls the SIAS by setting CTL SIAS TRIP. Reference 1, Section 6 5

2078 CTLSIASTRIP I/O Control SIS LO Safety injection actuation signal. This is a plant independent Active CTLSETPT variable This flag Is set by the User or by CENTS. To simulate a Inactive

manual SIAS actuation, the User can set CTLSIAS_TRIP= T via the command file. With SIAS control in Auto, CENTS can set the flag to True if the SIAS controller indicates a SIAS condition. Always used Reference 1, Section 6 5; and Reference 2, Table 2

2079 CTL_SIASPTRIP Output Control SIS LO SI signal at last time step. This plant independent flag variable is True False CTL SETPT set by CENTS. Always used.

2080 CTL SIS FLOW Partition RE 36 Safety injection system flow variables Partition 2081 CTL_SISHLPSIBC Input Control SIS RE HPSVLPSI flow boron concentration This is a plant dependent Parts/million

CTL SETPT input variable, set by the user. Often times set to 0.0 until a "sweep volume" of SI flow has entered the RCS See individual plant basedeck calculation. Reference 1, Section 6 5

2082 CTLSISHLPSIH Input Control SIS RE HPSVLPSI flow enthalpy. This is a plant dependent input variable, Btu/lbm CTLSETPT set by the user. Usually set to the enthalpy of the RWST water. Input _ _ I_ _ I_ _ I_ IReference 1, S ec tion 6 5.



Index Long Variable Name Input / System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

2096 CTLSDCHMIN Input Control SDC SDC RE Shutdown Cooling minimum return enthalpy. When Shutdown Btu/Ibm CTLSETPT cooling is active, it is drawn from the hot leg(s), and returns cooler

to the cold legs via the SI lines The minimum return enthalpy is given by the input CTLSDC H MIN Reference 1, Section 6 5

2097 CTL_SDC_SPLIT Input Control SDC SDC RE 4 SDC flow split to injection points. When Shutdown cooling is active, Fraction CTLSETPT it is drawn from the hot leg(s), and returns cooler to the cold legs via

the SI lines. The SDC flow set by SDCRCSFLOW is returned, via each SI line multiplied by CTLSDCSPLIT0. The sum of the splits need not be 1. Reference 1, Section 6.5.

2098 CTL TURB CONTROL Partition RE 14 Turbine controls Partition

2099 CTL TURB SETPOINTS Partition RE 7 Turbine control setpoints Partition 2100 CTLTURBTRIPVALVETIME Input Control TURB RE TAV full-range closing time on turbine trip. This is a plant Seconds

CTLSETPT dependent input variable It usually represents the shutting time of the Turbine stop valves which are quick shutting valves in a trip condition. CENTS combines the operation of the TSV and TAV into one valve. Note that since the TAV may not be full open at the time of the trip, the closing time may not be equal to CTLTURBTRIPVALVETIME, unless the trip controller is designed specifically to account for this. Reference 1, Section 6 6

2101 CTLTURBAOUTTC Input Control TURB RE Turb admission valve time constant. This is a plant dependent Seconds CTLSETPT input variable, It represents the time for full open to shut or shut to

___ _open operation in a non-trip environment Reference 1, Section 6 6 2102 CTLTURBTRIPTIME Output Control TURB RE Time elapsed since turbine trip. This is a plant independent variable Seconds

CTL SETPT calculated by CENTS Always used


Table G.1: Dictionary Listin2

Index Long Variable Name Input/ System System System Variable's Typle 1men- Definition Units No. Output Alt. I Alt. 2 Function sions

2103 CTLTURB_DEMAND I/O Control TURB RE Turbine steam demand. This is a plant independent variable which Fraction

CTLSETPT represents a steam flow demand to the turbine as a fraction of CTL_TURRBSTEAMRATED. It is established by the CENTS code as an output IFF CTLJURB_CONTROLAUTO and CTL_TURB_CONTROL_LOAD are both T=Auto. In that case, CENTS causes turbine load to follow the heat generation rate of the RCS.

If CTL_TURBCONTROLAUTO = T and CTLTURB_CONTROLLOAD = F=Manual, then User must set CTL_TURBDEMAND to the load fraction required for the power level desired to be maintained. This is the mode of operation most

used In the plants, whereby TAV operation adjusts to maintain constant steam flow rate. However, even In this mode, CENTS Initializes CTL_TURBDEMAND during INITIALization, such that the secondary heat load equals the primary heat generation. Therefore, the User should set CTLJURB_DEMAND immediately after the INITIALization. See CE-CES-0198-p Rev. 004, Section 3 4, for discussion on the proper setting of CTLTURB.DEMAND for other than full power operation.

IFF CTLTURBCONTROLAUTO and CTLTURBCONTROLLOAD are both F=Manual, then the User sets the TAV position via MSLHVALVESIG(J), where J = the TAV In the array of main steam valves. In this last case CTLTURB_DEMAND Is inactive.

Reference 1, Section 6.6

2104 CTL._TURBSTEAM_RATED Input Control TURB RE Rated turbine steam flow. This is a plant dependent Input vanable. Lbm/sec

CTLSETPT It Is set by tuning the basedeck at full power with all the full power "RCS Initial conditions and FW enthalpy. The resulting steam flow to the turbine is then established as CTLTURB_STEAMRATED.

2105 CTL_TURB_CONTROL_AUTO Input Control TURB LO Flag- automatic turbine control This is a plant independent input Auto Manual

CTLSETPT variable set by User. In T=Auto, CENTS controllers calculate the TAV position, based upon CTL_TURBCONTROLLOAD. See CTLTURBDEMAND. Reference 1, Section 6 6.

2106 CTLTURBCONTROLLOAD Input Control TURB LO Flag to match st. demand with heat load. This is a plant Auto Manual CTL_SETPT Independent Input variable set by User. See CTL_TURBDDEMAND

for further discussion. Reference 1, Section 6 6.

2107 CTLTURB_TRIP I/O Control TURB LO Signal: turbine tripped. This Is a plant Independent variable. This Trip Normal

CTLSETPT flag is set by the User or by CENTS. To simulate a manual Turbine trip, the User can set CTLTURB_TRIP= T via the command file. With Turbine trip control in Auto, CENTS can set the flag to True if

the turbine trip controller indicates a trip condition. Reference 1, Section 6 6; and Reference 2, Table 2.



Index Long Variable Name Input/ System System System Variable's Type Dlmen- Definition Units No_ Output Alt. 1 AIt. 2 Function slons

2108 CTLTURBTRIPAUTO Input Control TURB LO Flag. automatic trip of turbine This is a plant independent, User Auto Manual CTLSETPT defined input. In T=Auto, the controller output dictates turbine trip

condition. In F=Manual, the User controls the turbine trip by setting CTL TURB TRIP = T=Trip. Reference 1, Section 6 6

2110 CTL MSIS CONTROL Partition RE 14 Main steam isolation signal controls Partition 2111 CTLMSIS SETPOINTS Partition RE 10 MSIS control setpoints Partition 2112 CTLMSISSGPRES_TRIP Input Control MSIS RE Low SG pressure MSIS trip setpoint. This plant dependent input Psia

CTLSETPT variable is used if CTLMSISCONTROLAUTO = T=Auto. In this case the CENTS controllers compare SG pressure to the trip setpoint to determine if CTLMSISTRIP = T = Active. Reference 1, Section 6 6.

2113 CTLMSISCONTPRESTRIP Input Control MSIS RE Containment pressure MSIS tnp setpoint. This is a plant dependent Psia CTLSETPT setpoint Note that CENTS does not model changes in containment

pressure, except as they are input by the user, possibly via a RAMP. Reference 1, Section 6 6

2114 CTLMSISSGSLFLOWTRIP Input Control MSIS RE 4 High steamline flow MSIS trip setpoint. This array of setpoints is Lbm/sec CTLSETPT plant dependent. It is used only if the plant controllers are designed

with a high steam flow MSIS Reference 1, Section 6 6 2115 CTLMSIS_CONTROLAUTO Input Control MSIS LO Flag: MSIS automatic control. This is a plant independent, User Auto Manual

CTLSETPT defined input. In T=Auto, the controller output dictates an MSIS condition In F=Manual, the User controls the MSIS condition by setting CTL MSIS TRIP = T=Trip Reference 1, Section 6 6

2116 CTLMSISTRIP I/O Control MSIS LO Main steam isolation signal This is a plant independent variable. Active CTLSETPT This flag Is set by the User or by CENTS. To simulate a manual Inactive

MSIS condition, the User can set CTL_MSIS_TRIP= T via the command file With MSIS control in Auto, CENTS can set the flag to True if the MSIS controller indicates a tnp condition. Always used Reference 1, Section 6 6; and Reference 2, Table 2.

2117 CTLATMDUMP CONTROL Partition RE 6 Atmospheric dump valves controls Partition 2118 CTLATMDUMPSETPOINTS Partition RE 4 SG ADVs setpoints Partition 2119 CTLATMDUMPSPOINT Input Control ADV RE 2 Atmospheric dump valves setpoints. These setpoint variables are Psia

CTLSETPT plant dependent Their use is dependent upon the controller design. Normally, the design is such that the valves open to maintain the setpoint pressure Reference 1, Section 6 6

2120 CTLATMDUMPCONTROLAUTO Input Control ADV LO Flag: automatic ctrt of atm-dump valves. This isa plant Auto Manual CTLSETPT independent, User defined input. In T=Auto, the controller output

dictates an ADV operation. In F=Manual, the User controls the ADV operation by setting MSLHVALVESIG(J) to the fraction open, where "J" is the appropriate valve number. Reference 1, Section 6.6.

2121 CTL TURB BYPASS CONTROL Partition I RE 11 Turbine bypass controls Partition 2122 CTL TUR-BYPASS SETPOINTS Partition I RE 10 Turbine bypass valves setpoints Partition



Index Long Vaiable Name , Input/ System System System Variable's Type DImen- Definition Units

No. " • •' • Output Alt. I Alt. 2 Function slons

2123 CTL_TURB_DUMP_OPEN Input Control SDBS RE Pressure to open bypass valves. This setpoint variable Is plant Psla CTL_SETPT dependent. Its use Is dependent upon the controller design.

Normally, this pressure is the lower pressure limit for operation of the SDBC valves. Reference 1, Section 6.6.

2124 CTLTURB_DUMP_DELP Input Control SDBS RE Press. range of turb bypass ctd system. This setpoint variable is Psid

CTLSETPT plant dependent. Its use Is dependent upon the controller design. Normally, this pressure differential is the operational pressure range with the lower pressure limit for operation set by

CTLTURB_DUMP_OPEN. But, for some plant controller designs, this variable is the upper pressure setpoint, in psla. Reference 1,

Section 6 6.

2125 CTLTURB_DUMP_QOPEN Input Control SDBS RE Quick-opening time for turbine bypass valves. This setpoint 1/seconds CTLSETPT variable is plant dependent. Its use is dependent upon the

controller design. Normally it is set to a fraction/second rate. Reference 1, Section 6.6.

2126 CTITURBDUMPNOPEN Input Control SDBS RE Normal-open time for turb bypass valve. This setpoint variable is I/seconds CTLSETPT plant dependent. Its use Is dependent upon the controller design.

Normally It Is set to a fraction/second rate. Reference 1, Section 6.6.

2127 CTLTURBDUMP_QCLOSE Input Control SDBS RE Quick-close time for turb bypass valve. This setpoint variable is 1/seconds CTLSETPT plant dependent.' Its use Is dependent upon the controller design.

____I _Normally it is set to a fraction/second rate. Reference 1, Section 6.6.

2128 CTLJTURB_DUMP_NCLOSE Input Control SDBS RE Normal-close time for turb bypass valve. This setpoint variable is 1/seconds CTL_SETPT plant dependent. Its use is dependent upon the controller design.

I Normally It Is set to a fraction/second rate. Reference 1, Section 6 6.

2129 CTLTURBDUMPMODE Input Control SDBS RE Bypass control mode: O=p-temp, 1=s-pres. This flag variable Is Pointer

CTL.SETPT plant dependent. Its use Is dependent upon the controller design. In many controllers It is not used at all, In which case it is normally set to 0. Reference 1, Section 6 6.

2130 CTL_TURBBYPASS_CONTROLAUTO Input Control SDBS LO Flag: automatic turbine-bypass control. This is a plant Auto Manual

CTLSETPT independent, User defined Input. In T=Auto, the controller output dictates an SDBC operation. In F=Manual, the User controls the Bypass valve operation by setting MSLH_VALVESIG(J) to the fraction open, where VJ is the appropriate valve number. Reference 1, Section 6 6.

2131 CTLSGSAFETIES Partition RE 120 SG safety valves control variables Partition

2132 CTLSG_.SVSETPOINTS Partition RE 120 SG extemal safety valve setpoints Partition

2133 CTL_SGSV_PSET_OPEN Input Control MSSV RE 24 SG safeties design-open pressure setpoints. These setpoint Psla

CTLSETPT variables are plant dependent. Their use is dependent upon the controller and valve design. Normally, the design is such that the safety valves begin to open at this setpoint pressure. Reference 1, Section 6.6.



Index Long Variable Name input/ System System System Variable's Type Dimen- Definition Units No. Output AIt. 1 Alt. 2 Function slons

2134 CTL_SGSV_PSET_FULL Input Control MSSV RE 24 SG safeties full-open pressure setpoints These setpoint variables Psia CTLSETPT are plant dependent Their use is dependent upon the controller

and valve design. Normally, the design is such that the safety valves are full open at this setpoint pressure, or it is CTLSGSVPSETOPEN + accumulation. Reference 1, Section 66

2135 CTL SGSVPSETCLOSE Input Control MSSV RE 24 SG safeties closing pressure setpoints These setpoint variables Psia CTLSETPT are plant dependent Their use is dependent upon the controller

and valve design. Normally, the design is such that the safety valves are close fully at this setpoint pressure, or it is CTL SGSV PSET OPEN - blowdown Reference 1, Section 6.6.

2136 CTLSGSVASET_OPEN Input Control MSSV RE 24 SG safeties design-open fraction. These setpoint variables are Fraction CTLSETPT plant dependent. Their use is dependent upon the controller and

valve design. Normally, the design is such that the safety valves pop open to this fraction at CTLSGSV_PSETOPEN pressure. Reference 1, Section 6 6

2137 CTL FWSCONTROL Partition RE 70 Feedwater system controls Partition 2138 CTLFWS SETPOINTS Partition RE 15 FWS control setpoints Partition 2139 CTLFWSSG LEVELLOAD Input Control FW RE 2 SG level program load setpoints This setpoint is not currently used Fraction

CTLSETPT by CENTS Normally FW flow is set equal to steam flow or altematively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, it is expected that the User will take manual control of FWS to conservatively dictate FW flow. Reference 1, Section 6 7.

2140 CTLFWSSGLEVELLOW Input Control FW RE Main feedwater o-level control setpoint. This setpoint is not Fraction CTLSETPT currently used by CENTS Normally FW flow is set equal to steam

flow or altematively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, it is expected that the User will take manual control of FWS to conservatively dictate FW flow. Reference 1, Section 6.7

2141 CTLFWSSGLEVELHIGH Input Control FW RE Main feedwater hi-level control setpoint This setpoint is not Fraction CTLSETPT currently used by CENTS Normally FW flow is set equal to steam

flow or alternatively a 3-element demand system is used, but a detailed FW system model is not currently available In a safety analysis transient condition, it is expected that the User will take manual control of FWS to conservatively dictate FW flow. Reference 1, Section 6.7.


Table G.A: Dictionary Listing Index Long Variable Name Input System System System Variable's Type Dimen- Definition 2- - _ . Units

No-'. ,•"' • - Output - Alt.1, Alt. 2 Function" s__ lons I "-"•' "" •..

2142 CTLFWS_TURB_TRIP_FRAC Input Control FW RE Main FW rampdown flow frac after trip This setpoint is not currently Fraction CTLSETPT used by CENTS. Normally FW flow is set equal to steam flow or

alternatively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, It Is expected that the User will take manual control of FWS to conservatively dictate FW flow. Reference 1, Section 6.7.

2143 CTL_FWSTURB_TRIPDELAY Input Control FW RE Main FW rampdown time after turb trip. This setpoint is not Seconds CTLSETPT currently used by CENTS. Normally FW flow is set equal to steam

flow or alternatively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, it Is expected that the User will take manual control of FWS to conservatively dictate FW flow. Reference 1, Section 6.7.

2144 CTL_FWS_MAYFLOW Input Control FW RE Maximum feedwater flow to each SG. This plant dependent Lbm/sec CTL_SETPT setpoint places an upper bound on FW flow rate to the SG when In

automatic mode of operation. There is no bound upon what the User can input as FW flow rate In manual operation. Reference 1,

'_ __ _ _ Section 6.7. __III 1 1__

2145 CTLFWSSPEED_MULT Input Control FW RE 4 Multp on FW pump speed signi: -O to trip. This setpolnt is not Dimensionless CTL_SETPT currently used by CENTS. Normally FW flow is set equal to steam

flow or alternatively a 3-element demand system is used, but a , detailed FW system model Is not currently available. In a safety analysis transient condition, it Is expected that the User will take manual control of FWS to conservatively dictate FW flow. Reference

11, Section 6.7.

2146 CTL FWSfTRIPSP Input Control FW RE Feedwater trip setpoint. This setpoint Is not currently used by Undefined

CTL_SETPT CENTS. Normally FW flow Is set equal to steam flow or altematively a 3-element demand system Is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, it Is expected that the User will take manual control of FWS to conservatively dictate FW flow. Reference 1, Section 6.7.

2147 CTLFWSH Input Control FW RE 2 Steady state FW enth: 1 at CST, 2 at SGS. These are plant BtuAbm

CTLSETPT dependent variables set by the User. The original Intended use was to indicate the enthalpy at the condenser and at the entrance to the SG. Then if a trip occurred, the FW enthalpy would drop to the condenser enthalpy at a rate dictated by the time constant CTL_FWS_H_TC. -In current operation, the value for CTLFWS_H(1) = CTLFWSH(2) and is set at the enthalpy required for Initialization. Then the User changes enthalpy as

required during any transient. Reference 1, Section 6.7.

2148 CTL_FWS_HMAX Input Control FWI RE Maximum feedwater enthalpy. Used for NUM_FWS_PUMPS--O Btu/ibm

I III _ CTL SETPT I only. ___



Index Long Variable Name Input System System System Variable's Type Dimen- Definition Units No_, Output Alt. 1 Alt. 2 Function slons

2149 CTLFWS_H_TC Input Control FW RE Feedwater enthalpy time constant. Used for NUMFWSPUMPS=0 Seconds CTL SETPT only. See CTL FWS H

2150 CTL_FWS_TRIP I/O Control FW LO FWS trip signal Reference 1, Section 6.7, and Reference 2, Table Active I CTL SETPT 2 Inactive

2151 CTLFWSAUTO Partition LO 14 Flags for automatic control of FW system Reference 1, Section 6.7. Partition 2152 CTLFWSCONTROLAUTO Input Control FW LO Master FW flag T=separate, F=all manual This is a plant Auto Manual

CTLSETPT independent, User defined input. In T=Auto, the controller output dictates a FW flow rate. In F=Manual, the User controls the FW flow by setting FWS FLOW(J) Reference 1, Section 6 7.

2153 CTLFWSVALVEAUTO Input Control FW LO 4 Flags: auto control of downcmr FW valves. This setpoint is not Auto Manual CTLSETPT currently used by CENTS. Normally FW flow is set equal to steam

flow or alternatively a 3-element demand system is used, but a detailed FW system model is not currently available In a safety analysis transient condition, it is expected that the User will take manual control of FWS to conservatively dictate FW flow AND enthalpy. Reference 1, Section 6.7.

2154 CTLFWS_ECONVALVEAUTO Input Control FW LO 4 Flags, auto control of econmzr FW valves. This setpoint is not Auto Manual CTLSETPT currently used by CENTS. If available, it would only be applicable

to System 80 design plants Reference 1, Section 6 7 2155 CTLFWSPUMPAUTO Input Control FW LO 4 Flags: auto control of main FW pumps This setpoint is not currently Auto Manual

CTLSETPT used by CENTS. Normally FW flow is set equal to steam flow or alternatively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, it is expected that the User will take manual control of FWS to conservatively dictate FW flow AND enthalpy. Reference 1, Section 6 7

2156 CTL_FWS_TRIPAUTO Input Control FW LO Flag. automatic main feedwater trip Reference 1, Section 6.7 Auto Manual CTL SETPT

2157 CTLFWS_VALVESIG Output RE 4, 2 Main FW valve demand signals Fraction Partition

2158 CTLFWS_SIG I/O Control FW RE 4 Main FW downcomer valve demand signal. This setpoint is not Fraction CTLSETPT currently used by CENTS. Normally FW flow is set equal to steam

flow or alternatively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, it is expected that the User will take manual control of FWS to conservatively dictate FW flow AND enthalpy Reference 1, Section 6 7; and Reference 2, Table 2.

2159 CTLFWSECONSIG I/O Control FW RE 4 Main FW economizer valve demand signal. This setpoint is not Fraction CTLSETPT currently used by CENTS If available, it would only be applicable

to System 80 design plants. Reference 1, Section 6 7; and Reference 2, Table 2.

2160 CTLFWSVALVE POS Output RE 4, 2 Main FW valve positions. Fraction _ __Partition I I I I



Index Long Variable Name , lniut/ System SVstem System Varlable's, XType Dimen- Definition ., - -Units

No. . Output Alt. I Alt. 2 Function slons

2163 CTLFWSSPEEDSIG I/O Control FW RE 4 Main FW pumps speed demand signals. Reference 1, Section 6.7; Fraction CTLSETPT and Reference 2, Table 2.

2164 CTL._FWSSPEEDFRAC Output Control FW RE 4 Main FW pumps normalized speed, actual. This setpoint is not Fraction CTLSETPT currently used by CENTS. Normally FW flow is set equal to steam

flow or alternatively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, It Is expected that the User will take manual control of FWS to conservatively dictate FW flow AND enthalpy. Reference 1, Section 6.7.

2165 CTLFWSSPEED_MAX Input Control FW RE Main FW pumps reference speed. This setpoint is not currently Shaft RPM CTL_SETPT used by CENTS. Normally FW flow Is set equal to steam flow or'

altematively a 3-element demand system is used, but a detailed FW system model is not currently available. In a safety analysis transient condition, it Is expected that the User will take manual control of FWS to conservatively dictate FW flow AND enthalpy.

I__I __Reference 1, Section 6.7.

2166 CTLFWSISO_POS Output Control FW FW RE 4 Main FW isolation valve position. Reference 1, Section 6.7. Fraction CTLSETPT

2167 CTLFWSBYPSIG Output Control FW FW RE 4 Main FW bypass valve demand signal. Reference 1, Section 6.7. Fraction _CTLSETPT

2168 CTLAFWSCONTROL Partition RE 25 Aux feed system controls Partition

2169 CTLAFWSSETPOINTS Partition RE 20 AFWS control setpoints Partition

2170 CTL.AFWSSGLEVELLOW Input Control AFW RE 4 Low SG level setpoint for auxiliary feedwater. This setpoint Fraction CTL._SETPT variable is plant dependent. Its use is dependent upon the

controller design. Normally, at this level AFWS is actuated. This setpoint Is compared to either the actual downcomer water level calculated by CENTS, or it can be compared to the indicated water level which is based on the level indication model, complete with

_ calibration conditions, etc. Reference 1. Section 6.7.

2171 CTL AFWSSGLEVELHIGH Input Control AFW RE 4 High level setpoint for auxiliary feedwater. This setpoint variable is Fraction CTLSETPT plant dependent. Its use is dependent upon the controller design.

Normally, at this level AFWS flow Is terminated. This setpoint is compared to either the actual downcomer water level calculated by CENTS, or it can be compared to the Indicated water level which is based on the level Indication model, complete with calibration conditions, etc. Reference 1, Section 6.7.

2172 CTLAFWSTOTFLOW Input Control AFW RE Total aux-feed flow capacity, all SGs. This setpolnt variable is plant Lbm/sec CTLSETPT dependent. Its use Is dependent upon the controller design.

Normally, it Is not used because full flow rate is highly dependent upon SG pressure. Many CENTS control systems use an XTAB YTAB tables of pressure vs. flow with different SG and pump

_combinations included. Reference 1, Section 6.7.



Index Long Variable Name Input System System System Variable's Type Dimen- Definition Units No. __._.Output Alt. 1 Alt. 2 Function slons

2173 CTLAFWSSGDPHIGH Input Control AFW RE SG differential pressure to cutout auxiliary feedwater to one SG. Psid CTLSETPT This setpoint variable is plant dependent Its use is dependent upon

the controller design. Normally, at this differential pressure flow is terminated to the SG with the lower pressure as a means of preventing flow to a ruptured SG Reference 1, Section 6.7.

2174 CTLAFWS DELAY Input Control AFW RE AFW time delay after trip. This setpoint vanable is plant dependent Seconds CTLSETPT Its use is dependent upon the controller design. Normally, this is

the delay from the time an actuation signal is activated until the AFW pumps and valves are operating and open providing flow to

.__ the SG Reference 1, Section 6 7 2175 CTLAFWSFLOWMULT Input Control AFW RE 4 Multiplier on auxiliary feedwater flow rate. This plant independent Dimensionless

CTLSETPT variable is set by the User. Normally it is set to 1 0 for realistic modeling of flow For special test purposes, the User may require some other value for this multiplier. Reference 1, Section 6 7

2176 CTLAFWSTURB_PUMP Input Control AFW RE AFWS turb-driven pump switch. 0=off, I=ok. This setpoint variable Pointer

CTLSETPT is plant dependent. Its use is dependent upon the controller and plant design. Normally, it is used to indicate a possible single failure of the turbine driven pump. Reference 1, Section 6 7.

2177 CTLAFWSMOTORPUMP Input Control AFW RE AFWS motor-drivn pump switch. 0=off,l=ok. This setpoint variable Pointer CTLSETPT is plant dependent Its use is dependent upon the controller and

plant design. Normally, it is used to indicate a possible single failure of the turbine driven pump Reference 1, Section 6 7.

2178 CTLAFWSCONTROLAUTO Input Control AFW LO Flag. automatic control of aux feed. This plant independent Auto Manual CTLSETPT variable is set by the User. In T=Auto, the controller output dictates

AFWS operation. In F=Manual, the User controls the AFWS flow by setting AFWS_.FLOW(J), "JV indicates the SG No Reference 1, Section 6.7.

2179 CTLAFWSSPEEDSIG I/O Control FW AFW AFW RE 4 AFW pumps speed demand signals. Reference 1, Section 6.7; and Fraction _CTL SETPT _ Reference 2, Table 2

2180 CTLRPCSCONTROL Partition RE 15 Reactor power cutback system Partition 2181 CTLRPCSSETPOINTS Partition RE 5 RPCS setpoints Partition 2182 CTLRPCSCONTROLAUTO Input Control RPCS LO Flag automatic RPCS control. Reference 1, Section 6 8. Auto Manual

CTL SETPT 2183 CTL_RPCS_TRIP I/O Control RPCS LO Signal. RPC engaged. Reference 1, Section 6 8, and Reference 2, Trip Normal

CTL SETPT Table 2 2184 CTLRPCSPTRIP Output Control RPCS LO RPC signal at last time step. Reference 1, Section 6.8. Trip Normal

CTL SETPT 2185 CTLRPCSTRIP_TIME Output Control RPCS RE Time elapsed since RP cutback engaged Reference 1, Section 6 8 Seconds

CTL SETPT 2186 CTLTURB SETBACK CONTROL Partition RE 20 Turbine setback and runback systems Partition 2187 CTL TURB SETBACK SETPOINTS Partition RE 10 Turb setback & runback system setpoints Partition 2188 CTLTURBSETBACKAUTO Input Control TURB LO Flag. automatic turbine setback control. Reference 1, Section 6 6. Auto Manual

SETBK SETPT



Index Long Variable Name-_ . - Input/ System System System Variable's Type Dlmen- Definition ,- Units,' ,No...'•, -• - Output Alt. 1 AlL 2 , Function slone 2

2189 CTLTURB_RUNBACKAUTO Input Control TURB LO Flag: automatic turbine runback control. Reference 1, Section 6.6. Auto Manual SETBK SETPT

2190 CTL_TURBSETBACKTRIP I/O Control TURB LO Signal: turbine setback engaged. Reference 1, Section 6.6; and Trip Normal SETBK Reference 2, Table 2. SETPT

2191 CTLJURBRUNBACK I/O Control TURB LO Signal: turbine runback engaged. Reference 1, Section 6.6.; and True False SETBK Reference 2, Table 2. _SETPT ...

2192 CTLMISCSETPOINTS Partition ___RE 200 Miscellaneous user-defined setpoints Undefined 2193 CTLSETTEMP Input Control Model RE 20 Miscellaneous temperature setpoints. These setpoints, df used, are Degree F

Design totally dependent upon the design of the Individual plant CENTS controllers. Many controllers are unique and require constants which may not have a specifically defined setpoint variable. This array provides a place to record these values. Each basedeck

_calculation should define the use of each constant In this array. 2194 CTLSETDELTEMP Input Control Model RE 20 Miscellaneous delta-temp setpoints. These setpoints, if used, are Del-degF

Design totally dependent upon the design of the individual plant CENTS controllers. Many controllers are unique and require constants "which may not have a specifically defined setpoint variable. This array provides a place to record these values. Each basedeck calculation should define the use of each constant In this array.

2195 CTL SETDELTEMPD input Control Model RE 20 Miscellaneous per-delta-temp setpoints. These setpoints, if used, Per-degF Design are totally dependent upon the design of the Individual plant CENTS

controllers. Many controllers are unique and require constants which may not have a specifically defined setpolnt variable. This array provides a place to record these values. Each basedeck

_calculation should define the use of each constant in this array.

2196 CTLSETyPRES input Control Model RE 20 Miscellaneous pressure setpolnts. These setpoints, if used, are Psia Design totally dependent upon the design of the individual plant CENTS

controllers. Many controllers are unique and require constants which may not have a specifically defined setpoint variable. This array provides a place to record these values. Each basedeck calculation should define the use of each constant In this array.

2197 CTL._SET_PRESD Input Control Model RE 20 Miscellaneous per-pressure setpoints. These setpolnts, if used, are Per-psia Design totally dependent upon the design of the individual plant CENTS

controllers Many controllers are unique and require constants which may not have a specifically defined setpoint variable. This array provides a place to record these values. Each basedeck rcalculation should define the use of each constant In this array. I



Index Long Variable Name Inputl System System System Variable's Tlype Dimen- Definition Units No. Output Alt. 1 Alt. 2 Functlon slons

2198 CTLSETNODIM Input Control Model RE 60 Miscellaneous dimensionless setpoints These setpoints, if used, Dimensionless Design are totally dependent upon the design of the individual plant CENTS

controllers. Many controllers are unique and require constants which may not have a specifically defined setpoint variable This array provides a place to record these values. Each basedeck calculation should define the use of each constant in this array.

2199 CTLSETFLOW Input Control Model RE 10 Miscellaneous flowrate setpoints. These setpoints, if used, are Lbm/sec Design totally dependent upon the design of the individual plant CENTS

controllers. Many controllers are unique and require constants which may not have a specifically defined setpoint variable. This array provides a place to record these values Each basedeck

_calculation should define the use of each constant in this array 2200 CTLSETFLOWD Input Control Model RE 10 Miscellaneous per-flowrate setpoints. These setpoints, if used, are SecAbm

Design totally dependent upon the design of the individual plant CENTS controllers. Many controllers are unique and require constants which may not have a specifically defined setpoint variable This array provides a place to record these values. Each basedeck calculation should define the use of each constant in this array.

2201 CTLSETYPERTIME Input Control Model RE 20 Miscellaneous per-time setpoints. These setpoints, if used, are 1/seconds Design totally dependent upon the design of the individual plant CENTS

controllers. Many controllers are unique and require constants which may not have a specifically defined setpoint variable. This array provides a place to record these values. Each basedeck calculation should define the use of each constant in this array.

2202 CTLTIMECONSTANTS Input Control Model RE 150 Miscellan. user-defined time constants. These setpoints, if used, Seconds Design are totally dependent upon the design of the individual plant CENTS

controllers Many controllers are unique and require constants which may not have a specifically defined setpoint variable This array provides a place to record these values Each basedeck calculation should define the use of each constant in this array.

2203 CTLOUTPUT Partition RE 16 Output control partition Partition 2204 CTLOUTPUTINTERVAL Input Output IN Output frequency for line output CENTS produces a one-line Counts

output edit every CTLOUTPUTINTERVAL time steps. The user may change this to reduce the size of the output. Reference 1, Section 7 6 1

2205 CTLOUTPUTOPTION Input Output IN Line output option. CTLOUTPUT_OPTION modifies the one line Pointer output. If CTLOUTPUT_OPTION > 0.0. pressurizer 2-phase level is printed. Otherwise, indicated pressurizer level is printed

I_ I_ Reference 1, Section 7 6 1 2206 CTLOUTPUTCOUNT Input Output IN 4 Output counter- calls/ine/graph/title. CTLOUTPUT.COUNT is the Counts

total number of timesteps since the specified output was generated. The base deck requires initial values which are then updated during the run. Reference 1, Section 7.6.1.



Index Long Variable Name Input System System System Variable's Type Dlmn! Definition .. .. - , o , Units, . No., L . .. Output Alt 1 Alt. 2 Function slons

2207 CTL__OUTPUTNTITLE Input Output IN Une output title frequency. CTLOUTPUT._NTITLE specifies the Counts number of lines which are printed before a new title line Is printed. This should be set so that one title line Is printed on each page of output. The value depends on the printer being used, font size, etc. and must be adjusted by the user for his setup. Reference 1, Section 7.6.1.

2210 CTLOUTPUTLOOP Input Output IN 2 Select loops for the standard output. CTLOUTPUT"_LOOP Dimensionless specifies which 2 coolant loops (and associated steam generators) should be used for the standard output. For CE plants, the choice Is 1,2 because there are only two loops. Reference 1, Section 7.6.1.

2211 CTL_.OUTPUT__OPCL Input Output IN Determines which cold leg's temperature is displayed second in the Dimensionless standard output (Reference 1, Section 7.6.1.). That Is, display the temperatures of cold legs L and M, where: L = CTLOUTPUTLOOP(1)

I M = CTLOUTPUTLOOP(2) + CTL.OUTPUTOPCL 2214 CTL.TIMEBLOCK Partition RE 10 Time step control Information for CENTS Partition

2218 TIME I/O RE Simulation time. This variable is continually updated as CENTS Seconds Increments it by the value of TIME_SCALE. Since TIME is not used "anywhere in the CENTS calculational models, the User may reset or change TIME. However, some of the CEER background operations may be affected, such as SCREEN and RECORD.

2219 TIME-SCALE Input RE Global calculational time step length. Per unit

2220 TSTOP I/O RE Value of time at which to pause. Normally set by CENTS in Seconds accordance with the current TIME and the parameter of the GO command. Placing "TSTOP=0" In a WHEN command will cause the execution to pause when the WHEN Is activated.

2225 CTIINITIALCONDITIONS Partition RE 4 Flags for initial conditions Partition

2230 INITALL Output LO Internal flag set by CENTS when Initializing all the routines. True False

2231 INIT. OFF MODELS Partition LO 7 Off flags for initialization models True False

2232 INITOFFRCS Input LO Initialization of RCS: off flag. The INIT_OFFxxx flags are used to True False defeat the Initialization of each of the major models. These should set to False In the base deck.

2233 INIT_OFF._CHT Input LO Initialization of CHT: off flag. The INIT_OFFmxx flags are used to True False defeat the Initialization of each of the major models. These should

I__II set to False In the base deck.

2234 INITOFFPOW Input LO Initialization of POW: off flag. The INIT_OFFxxx flags are used to True False defeat the initialization of each of the major models. These should set to False in the base deck. _ _ _

2235 INITOFFSGS Input - LO Initialization of SGS: off flag. The INIT _OFF._xxx flags are used to True False defeat the Initialization of each of the major models. These should

-- ____set to False In the base deck. "

2236 INIT_OFFCON Input LO Initialization of CONT: off flag. The INITOFF._xxx flags are used True False to defeat the initialization of each of the major models. These _should set to False In the base deck.


Table G.1: Dictionary Listing Inde.x Long Variable Name Input System System System Variable's Type Dimen- Definition Units

No._ Output Alt. 1 Alt. 2 Function slons 2236 INITITER Input IN Number of initialization passes. This is a plant independent variable Counts

set by the User to determine the number of code iterations on the steady state T/H solution Int-iter is the number of iterations during the initialization. Experience has shown that 30 iterations is sufficient. This value can be dependent on the controller setup The time steps assumed for the controllers during the initialization is 0.1 seconds so that the equivalent of 3 0 seconds pass - this is enough time to force the controllers to steady state so long as the time constants for lead/lags are less than 3 0 seconds Reference 1, Appendix D

2239 CTL ILEVEL Partition RE 15 instrument level readings for controls Fraction 2240 CTLSGILEVEL Output SG RE 4, 3 SG level readings. This output array is the CENTS calculated WA Fraction

and NR SG level indications The first index is the SG, and the second index is the reference leg as defined in the partition SG-REFLEGS This parameter is based on CENTS calculation of actual SG downcomer level and the fluid conditions with respect to the calibration conditions for the level indication system. These parameters are used in the controller system as input for controller actuation for such systems as RPS, AFW, FWCS, etc Reference 1, Sections 6 7 4 and 7 3 1

2241 CTL_PRZRILEVEL Output PZR RCS RE Pressurizer level reading This output is the CENTS calculated Fraction pressurizer level indication. This parameter is based on CENTS calculation of actual pressurizer level and the fluid conditions with respect to the calibration conditions for the level indication system. This parameter is used in the controller system as input for controller actuation for such systems as RPS, CVCS, Pressurizer heaters, etc. Reference 1, Section 6 2.2.

2243 CTL CONTROLLER Partition I RE 3000 Control module variables Partition 2244 ELLAST Output Control Model RE 1000 Saved 'last values" of control elements These "last values" are Undefined

Design needed as input by that particular element type in the next time step calculation See Reference 2. 2245 GROUT 1/O Control Model RE 1000 Control group output signals. This array of values represents the Undefined

Design final output from each controller at every time step. For any controller for which the malfunction MAL_CTL0 = T, the GROUT calculation is bypassed, and the User may input GROUT directly. See Reference 2

2246 MALCTL Input Control LO 1000 Control group malfunction cues See Reference 2 Malfunc Normal

2247 CTL_DELAYS Partition RE 50 Partition for control system delays. Note. Some delay variables Partition appear elsewhere: CTL_CORETURB_TRIPDELAY, CTL_SISDELAY, CTL_FWSTURB_TRIP_DELAY,

2248 _______________________ DELAYS _____tio ____CTL AFWS DELAY, SCRAM DELAY !Partitio 2248 OILCORETRIP DELAYS Partition ___RE 30 Partition for Scram channel delays Partition 2249 CTLCORE HIPOWER FRAC TRIPDL lnput Control I _ Delay RE I____High power fraction scram delay Seconds



Index Long Variable Name - Input/ System Sstem System Variable's, Type Dimen- Definition Units No.....=. ' Output .. _Alt. 1 Alt 2 Function slons ____

2250 CTLCOREHIPOWERSURTRIPDL Input Control Delay RE High power SUR scram delay Seconds

2251 CTLCORELOWPRZRPRESTRIPDL Input Control Delay RE Low pressurizer pressure scram delay Seconds

2252 CTLCOREHIPRZRPRESTRIPDL Input Control Delay RE High pressurizer pressure scram delay Seconds

2253 CTLCOREHIPRZRLEVELTRIPDL Input Control Delay RE I High pressurizer level scram delays Seconds

2254 CTLCOREOVERTEMPMRGN_TRIPDL Input Control I Delay RE Over-temperature thermal margin scram delay Seconds

2255 CTLCOREOVERPOWERMRGNTRIPDL Input Control Delay RE Over-power thermal margin scram delay Seconds

2256 CTLCORERCSFLOWFRACTRIPDL Input Control Delay RE Low loop flow scram delay Seconds

2257 CTLCORE_SIASTRIPDL Input Control Delay RE Scram due to SIAS delay Seconds

2258 CTLCORELOWSGPRESTRIPDL Input Control 1 Delay RE Low SG pressure scram delay Seconds

2259 CTLCORELOWSGLEVELTRIPDL Input Control Delay RE Low SG level scram delay Seconds

2260 CTLCOREHISGLEVELTRIPDL Input Control Delay - RE High SG level scram delay Seconds

2261 CTL.STEAMFEED MISMATCHTRIPDL Input Control Delay RE Steam-feed flow mismatch scram delay Seconds

2262 CTLCOREHICONTPRESTRIPDL Input Control Delay RE High containment pressure scram delay Seconds

2263 CTLCOREUSERDEFINEDTRIPDL Input Control Delay RE 10 Space for other scram delays Seconds

2264 CTLMISCTRIPDELAYS Partition RE 20 Partition for miscellaneous control system delays Partition

2265 CTL TURB TRIP DELAY Input Control Delay RE Turbine trip signal delay I I Seconds

2266 CTL MSIS TRIP DELAY- Input Control Delay RE Main steamline Isolation signal delay Seconds

2267 CTLFWSTRIPDELAY Input Control Delay RE Main feedwater trip signal delay Seconds

2268 CTLRPCSTRIPDELAY Input Control Delay RE I Reactor Power Cutback signal delay Seconds

2269 CTLTURBSETBACK TRIPDELAY Input, Control Delay RE _ Turbine Setback signal delay Seconds

2270 CTL TURB RUNBACKDELAY Input Control Delay RE _ Turbine Runback delay Seconds

2271 CTL MISC DELAYS Input Control Delay RE 10 Space for other control system delays Seconds

2272 USER-COMMON Segment RE 1024 User global common variables Segment

2273 SCRAM.DELAY Input CORE RCS RE Total scram delay time after trip. This USER input is intended to be Seconds the delay time from the onset of a reactor trip signal until the scram breakers open. It may be different for each scenario, depending upon which trip function actuates. For safety analysis, it is usually set to the Tech Spec. max. time. Normally, it does not include the UV trip coil delay. This is usually Included In the scram reactivity vs. time table, which starts after SCRAMDELAY has elapsed. Note that some plant controller decks have lags established for the pressure, temperature, and level sensors. For these plants, it Is important for the USER to know how these lags figure into the overall calculation of the scram delay time so that the lags are not

"double counted" when entering a value for SCRAM-DELAY.

2274 MSLHNO.MOISTURECARRY Input MSL SG RE 1 => No moisture carryover. This Input variable = 1 forces CENTS Dimensionless to allow only steam to exit the SG outlet nozzle, regardless of the two-phase level in the SG. This allows compliance with regulatory guidelines for conservative estimations of SG blowdown during an MSLB event.



Index Long Variable Name !p System System System Variable's IYl! Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

2275 SGTINITOPTION Input SG RE 0 => Adjust area. 1 => Find SG press. During initialization of Dimensionless CENTS with a basedeck and set of initial conditions, two options are available for setting the SG steam dome pressure. If the USER knows exactly the desired pressure for the given scenario, then SGT_INITOPTION = 0 is chosen In this case, the code will adjust the tube heat transfer area to allow the proper RCS to SG heat balance necessary to attain the desired pressure Normally, the variable is set to 1, which allows CENTS to calculate the SG pressure which provides the best steady state heat balance for the given initial conditions. The SG tube heat transfer areas, in this case, remain at their base deck value

2276 INTERPOLATIONERROROPTION Input RE If 1 => Error stop after each interpolation out-of-table-range error, in Dimensionless order to avoid the danger of extrapolation If 0, => Extrapolation will proceed with no message

2277 SGSDEBUGSGSINI Input SG RE 1 => Debug print on in subroutine SGSINI. 0 => No debug print Dimensionless

2278 SGS DEBUG SGHEAT Input SG RE I => Debug print on in subroutine SGHEAT. 0 => No debug print Dimensionless

2279 CTLCOREPOWERA Output CORE RE Core power. This CENTS calculated output (in Mwt) is the Megawatts essentially equivalent to CTL_COREPOWER (in BTU/sec) or CTLCOREPOWERFRACTION (in fraction of POW USERPOWZ, which is design 100% power)

2280 SGSAREADOWNCOMER Input SG RE 4 Area of downcomer for bubble rise calculation This calculated Ft2

input is normally chosen to be an average area, or total volume/total height

2281 SGS ALPHA DOWNCOMER Output SG RE 4 Steam generator downcomer steam volume fractions Dimensionless

2282 SGSVEL31_MULT Input SG RE 4 Downcomer multiplier on Wilson velocity. Normally set to 1.0 Dimensionless except for special testing or tuning to known plant conditions or other codes

2283 SGS STEAM VEL31 Output SG RE 4 Steam velocity downcomer to steam dome Ft/sec

2284 RCS BALANCE Partition RCS RE 54 RCS mass and energy balance Partition

2285 RCS NODAL EXT FLOWS Output RCS RE 50 Sum of the external flows to each node. Reference 1, Section 7 6 3 Lbm/sec

2286 RCSNETEXTFLOW Output RCS RE Sum of all external RCS flows - includes PRZR. This output Lbm/sec parameter is the SUM(RCSNODALEXTFLOW(I)). Reference 1, Section 7 6 3

2287 RCS NET HEAT RATE Output RCS RE Sum of all heat flows to RCS Reference 1, Section 7 6 3 Btu/sec

2288 RCS_TOTALMASS Output RCS RE Sum of all RCS nodal fluid masses - inc PRZR. Reference 1, Lbm Section 7 6 3

2289 RCSTOTALENERGY Output RCS RE Sum of all RCS node total energy in the fluid system Reference 1, Btu I Section 7.6 3

2290 IODINE TOTALS PARTITION Partition RE 10 Variables to check iodine release model Partition

2291 RCS TOTAL IODINE Output RCS RE Total iodine in RCS nodes Curies

2292 SGS TOTAL IODINE Output RCS RE Total iodine in stm Generators & header Curies

2293 RCS IOD REL TOT Output RCS RE I Total of core release & external flows Cunes

2294 RCS IOD REL RATE Output RCS RE I__ Net rate of core release and ext flows Microcurie/sec

G3-177WCAP- 15996-NP, Revision 0

Table G.A: Dictionary Listing "Index Long Varable Name, , . 7input/ System System System Variable's,: Tp DImen- Definition,. . Unlts', ,

N , -... ,, Pi' •. Output - Alt1 Alt2. Function,:- slons : i.i.: -° - '

2295 CTLSUMMARY.DATA Partition RE 150 Case summary data Partition

2296 CTL MAXPOWERFRAC Output CORE RCS RE Maximum power fraction during run. Reference 1, Section 7.6.3. Fraction

2297 CTL_MAXPOWER TIME Output CORE RCS RE Time of maximum power during run. Reference 1, Section 7.6.3. Seconds

2298 CT _MAX HEATFLUX FRAC Output CORE RCS RE Maximum heat flux during run. Reference 1, Section 7.6.3. Fraction

2299 CTLMAXHEATFLUXTIME Output CORE RCS RE Time of maximum heat flux during run. Reference 1, Section 7.6.3. Seconds

2300 CTLMAXPRZR_PRESS Output PZR RCS RE Maximum Pressurizer Pressure during run. Reference 1, Section Psla

7.63.

2301 CTL_MAXPRZRPRESS_TIME Output PZR RCS RE Time of maximum Pressurizer Pressure during run. Reference 1, Seconds Section 7.6.3.

2302 CTLMINPRZRPRESS Output PZR RCS RE Minimum Pressurizer Pressure during run. Reference 1, Section Psia

- _1 -7.6.3.r

2303 CTLMINPRZRPRESS_TIME Output PZR RCS RE Time of minimum Pressunzer Pressure during run. Reference 1, Seconds

I ' Section 7.6.3. , ... .

2304 CTLMAX RCS PRESS Output RCS RE Maximum RCS Pressure during run. Reference 1, Section 7.6.3. Psia

2305 CTLMAXRCS_PRESS_TIME Output RCS RE Time of maximum RCS Press during run. Reference 1, Section Seconds

7.6.3.

2306 CTLMIN RCSPRESS Output RCS RE Minimum RCS Pressure during run. Reference 1, Section 7.6.3. Psla

2307 CTLMINRCSPRESSTIME Output RCS RE Time of Minimum RCS Press during run. Reference 1, Section Seconds 17.6.3.

2308 CTLMAXSG_PRESS Output SG RE 4 Maximum SG Pressure during run. Reference 1, Section 7.6.3. Psla

2309 CTLMAXSGPRESSTIME Output SG, RE 4 Time of maximum SG Press during run. Reference 1, Section Seconds

7.63.,

2310 CTL_MIN_SG_PRESS Output SG RE 4 Minimum SG Pressure during run. Reference 1, Section 7.6 3. Psia

2311 CTLMIN_SG_PRESSTIME Output SG RE 4 Time of minimum SG Press during run. Reference 1, Section 7.6.3. Seconds

2312 CTLINTEGPFLOWNONMOM Output RCS RE 50 Integrated flow though all leak paths. Reference 1, Section 7.6.3.- Ibm

2313 CTLINTEGSGSVALVES Output SG RE 50 Integrated flow though secondary paths. Reference 1, Section Lbm

- - __ 7.6.3. -

2314 CTLINTEGMSLBINFLOW Output MSL RE 8 Integrated flow MSLB Inside containment. Reference 1, Section Lbm

_. . .. __ 7.63.

2315 CTLJINTEG-MSLB-OUT.FLOW Output MSL RE Integrated flow MSLB outside containment Reference 1, Section Ibm

I . .. 7.6.3.

2316 CTLINITIAL COREFLOW Output CORE RCS RE Initial core flow. Reference 1, Section 7.6.3. Lbm/sec

2317 CTLCORE FLOWFRAC Output CORE RCS RE Normalized core flow - frac of initial. Reference 1, Section 7.6 3.- Fraction

2318 CTLHEATFLUXFRAC Output CORE RCS RE Core average heat flux fraction. Reference 1, Section 7.6.3. - Fraction

2319 CTL.CETOPMINDNBR Output RCS Core RE CETOP Minimum DNBR for the entire case run. Reference 1, Fraction

- I Section 7.6 3 and Appendix F.

2320 CTL CETOPMINDNBR_'IME Output RCS Core RE Time of CETOP Minimum DNBR. Reference 1, Section 7.6.3 and Seconds -- - - __ Appendix F.

2321 CETOPLINK . Partition RE 50 Partition to store CETOP link data. Referencel , Appendix F. Partition

2322 CETOP.OUT Partition RE 19 ICETOP standard output. Reference 1 , Appendix F. Partition

2323 CETOPOUTCASE Output RCS Core RE CETOP out: Case number. Reference 1 , Appendix F. Fraction

2324 jCETOPrOUT ODBL Output RCS Core RE CETOP out: Heat flux. Reference 1 , Appendix F. MegBtu/hr-f r. 1,7o

WCAP-15996-NP, Revision 0 U-I I0


Index Lonfi Variable Name Input System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

2325 CETOPOUTPOLR Output RCS Core RE CETOP out Power operating limit Reference 1 , Appendix F. Fraction 2326 CETOPOUT TIN Output RCS Core RE CETOP out: Inlet temperature Reference 1 , Appendix F. Degree F 2327 CETOPOUTPIN Output RCS Core RE CETOP out: Pressure Reference 1 , Appendix F. Psia 2328 CETOP OUT GAVG Output RCS Core RE CETOP out Core average mass velocity. Referencel , Appendix F 10e6 lb/hr-ft2 2329 CETOPOUT ASI Output RCS Core RE CETOP out, Axial shape index. Reference1, Appendix F Ratio 2330 CETOPOUTNRAD Output RCS Core RE CETOP out: Peripheral Axial shape index Referencel , Appendix Fraction

I_ F 2331 CETOP_OUTP1MAX Output RCS Core RE CETOP out: Max radial avg peaking factor Referencel , Appendix Fraction

F. 2332 CETOPOUT DNB-N Output RCS Core RE CETOP out: Min DNBR at final iteration. Referencel , Appendix F. Fraction 2333 CETOPOUT X-N Output RCS Core RE CETOP out, Quality at final iteration Referencel , Appendix F. Fraction 2334 CETOPOUT DNB-1 Output RCS Core RE CETOP out. Min DNBR at first iteration Referencel , Appendix F. Fraction 2335 CETOP OUT X-1 Output RCS Core RE CETOP out. Quality at first iteration Referencel , Appendix F. Fraction 2336 CETOPOUT QUIX Output RCS Core RE CETOP out' QUIX file case number. Referencel, Appendix F. Fraction 2337 CETOPOUTITER Output RCS Core RE CETOP out' Number of iterations. Referencel , Appendix F. Fraction 2338 CETOPOUTlEND Output RCS Core RE CETOP out: Iter code. 1 => DNBR converged. Referencel, Fraction

Appendix F. 2339 CETOPOUTATR Output RCS Core RE CETOP out. Average enthalpy transport coefficient Referencel, Composite

Appendix F. Units 2340 CETOPOUTHCH Output RCS Core RE CETOP out' Min DNBR hot channel number. Referencel, Pointer

Appendix F 2341 CETOPOUT MNOD Output RCS Core RE CETOP out: Min DNBR node location Referencel , Appendix F Pointer 2342 CETOP IN Partition RE 7 CETOP Inputs from CENTS Referencel , Appendix F Partition 2343 CETOP_IN_TIME Output RCS Core RE CETOP in: CENTS simulation time CETOPINJTIME is equal to Seconds

the CENTS variable TIME, and replaces CETOP vector #93. Referencel , Appendix F

2344 CETOPINFLOWFRAC Output RCS Core RE CETOP in: Normalized core flow. CETOPINFLOWFRAC is Fraction equal to the CENTS variable CTLCOREFLOWFRAC, which is defined as the ratio of the current core inlet mass flow to the initial core inlet mass flow. The CETOP mass flow specified by CETOP

I__II vector #1 is multiplied by this factor. Referencel , Appendix F. 2345 CETOPININLETTEMP Output RCS Core RE CETOP in' Core inlet temperature. CETOPjN_INLET_TEMP is Degree F

equal to the CENTS variable CHTTEMPCOOL(1) This value replaces CETOP vector #3 Referencel , Appendix F

2346 CETOPINCORE_PRESSURE Output RCS Core RE CETOP in' Core pressure CETOP IN COREPRESSURE is Psia equal to the CENTS variable PRESS(NODECORE). This value replaces CETOP input vector #4. Referencel , Appendix F.

2347 CETOP_IN_HEATFLUXFRAC Output RCS Core RE CETOP in: Heat flux fraction. CETOPIN_HEAT_FLUX_FRAC is Fraction equal to the CENTS variable CTLHEAT_FLUXFRAC, defined as the ratio of the current core average heat flux to the heat flux at full power The CETOP heat flux specified in CETOP vectors 2 and 102 are multiplied by this factor Referencel , Appendix F.



Index Long Variable Name.,, -.Input System System System Variable's T DImen- Definition Un- tlt,.s No.-- Output Alt. 1- Alt. 2 Function slons - "

2348 CETOP_IN_FR_USER_MULT Input RCS Core RE CETOP In: User input Fr multiplier. CETOPJNN_FRUSERMULT Fraction is a user specified multiplier on the CETOP Fr given by CETOP input vector # 58. The base radial peak used by CETOP Is specified in the CETOP input file by the variable A(58). When the CETOP link Is active, this peak Is adjusted by two multiplicative factors. The first factor is CETOPIN_FR_USER_.MULT. The user sets this multiplier (possibly with the RAMP command) to account for radial effects such as the increase In Fr due to a dropped CEA. This variable should normally be set to 1.0. The second factor is CETOP_IN_FRTEMPMULT. Referencel , Appendix F.

2349 CETOPJN.FR.TEMP..MULT Output RCS Core RE CETOP In: FR temperature multiplier. Fraction CETOP_IN_FRTEMPMULT is one of two multipliers on the CETOP Fr given by CETOP input vector #58. This factor accounts for the increase in core peaking due to changes In core inlet temperature. The variable CETOPINFR TEMPMULT is calculated by CENTS based on current path temperatures by the formula

CETOPINFRTEMPMULT = 1.0 + CETOPFRDERIV ICETOPFRDELTEMPI

The other multiplier Is CETOP_IN_FR_USER_MULT: Referencel, _ _ _ _ _ _Appendix F.

2350 CETOPLINKCONTROL Partition RCS Core RE 7 CETOP link variables and options. Referencel , Appendix F. Partition

2351 CETOPPRESSOPT Input RCS Core LO CETOP link: Constant pressure option. CETOPPRESS_OPT Is a True False flag to use constant pressure in the DNBR calculation. The default is False, so that CETOP is passed the current value of core pressure. When CETOPPRESS_OPT is set to true, the data base variable CETOP_IN_CORE_PRESSURE must be set by the user. Referencel , Appendix F.

2352 CETOPFR-DERIV Input RCS Core RE CETOP link: User input derivative of Fr with respect to temperature. 1/Del-DegF See CETOPINFRTEMPMULT. The variable CETOPFRDERIV Is specified by the user. A typical value Is 0.005 /degF. To disable the Fr temperature correction, set CETOP_IN_FR_DERIV to 0 0 so that CETOPINFRTEMP._MULT will always be 1.0. Referencel, Appendix F.

2353 CETOPLFRPATH1 Input RCS Core IN CETOP link: Path number for CETOPYFR-TEMP1. Referencel, Pointer -_-_ _Appendix F.

2354 CETOPFRPATH2 Input RCS Core IN CETOP link: Path number for CETOP_FR_TEMP12. Reference1, Pointer Appendix F..



Index Long Variable Name Input System System System Variable's Type Dimen- Definition Units No.___ Output Alt. 1 Alt. 2 Function slons

2355 CETOP-FRJTEMP1 I/O RCS Core RE CETOP link. Templ for DT calculation. Degree F

If CETOP_FR_PATHt1 > 0. Temperature in that path, set be CENTS If CETOPFRPATH1 < 0 Constant temperature, assigned by user.

This enables the user to calculate the temperature correction based on the difference of a path temperature and a reference value.

See CETOPFRDEL_TEMP and CETOPINFRTEMPMULT. Referencel , Appendix F.

2356 CETOPFR_TEMP2 I/O RCS Core RE CETOP link. Temp2 for DT calculation. Degree F If CETOPjRPATH2 > 0. Temperature in that path, set be CENTS

If CETOP FRPATH2 <0. Constant temperature, assigned by user. This enables the user to calculate the temperature correction based on the difference of a path temperature and a reference value.

See CETOPFRDELTEMP and CETOPIN_FR_TEMPMULT. Referencel , Appendix F

2357 CETOPFR_DELTEMP Output RCS Core RE CETOP link: Temp Duff for Fr correction. The variable Degree F CETOPFRDEL.TEMP used in the Fr temperature correction is an inlet temperature difference which is calculated as the difference of CETOPFRTEMP1 and CETOP_FRTEMP2. The two temperatures are set by CENTS to the temperature of any CENTS paths based on the value of the pointers CETOPFR_PATH1 and CETOPFR.PATH2. If the value of one or both of the pointers is 0, the corresponding temperature is not updated by CENTS and must be set by the user. This enables the user to calculate the temperature correction based on the difference of a path temperature and a reference value. Referencel , Appendix F

2358 VATTENFALL-MISCELLANEOUS Partition RE 200 Partition for Vattenfall use Partition

2359 INITDEBUGOUTPUT Input RE 1 => Debug print on in the INITIALization routine. 0 => No debug Dimensionless print

2367 CDCONT COMMON Partition RE 50 Container array for Cooldown Controllers Partition

2368 DBG SGTR PARTITION Output RCS RE 36 SGTR Debug Variables Partition

2369 DBG SGTR FLOW1 Output RCS RE 4 Debug Variable SGTR Flow side 1 Lbm/sec

2370 DBGSGTR FLOW2 Output RCS RE 4 Debug Variable SGTR Flow side 2 Lbm/sec

2371 DBG SGTR FLOW SLOT Output RCS RE 4 Debug Variable SGTR Slot flow Lbm/sec

2372 DBG SGTR PRESS PRIl Output RCS RE 4 Debug Variable SGTR Primary pressure side 1 Psia

2373 DBG SGTR PRESS PRI2 Output RCS RE 4 Debug Variable SGTR Primary pressure side 2 Psia

2374 DBG SGTR PRESS SG Output RCS RE 4 Debug Vanable SGTR Secondary pressure Psia

2375 IDBG SGTR PRESS ITER Output RCS RE 4 Debug Variable SGTR Slot pressure Psia

2376 DBG SGTR SVOL TUBE1 Output RCS RE 4 Debug Variable SGTR Tube 1 specific volume ftA3/Ibm

2377 DBG SGTR SVOL TUBE2 Output RCS RE 4 Debug Variable SGTR Tube 2 specific volume ft^3/Abm

2378 FWS COMMON Segment FW RE 20000 Feedwater System model segment Segment

2379 FWS FDPATH Partition FW RE 1600 FWS model flow path partition Partition



Index Long Variable Name , Input/ Sstem System System Variable's Type Dlmen- Definition . Units

No.. - Output Alt. 1 AIL-2 Function sions

2380 FWS_DPEL Input FW Plant Design RE 50 FWS model flow path elevation gain, external path. Referencel, Feet Section 5.5, 6.7 and 7.3.4.

2381 FWS._CV Input FW Plant Design RE 50 FWS model flow path flow coefficient Referencel , Section 5.5, 6.7 Composite

I I and 7.3 4. 1 Units

2382 FWS_RESL Input/init FW Plant Design RE 50 FWS model flow path flow resistance. Referencel , Section 5 5, 6.7 Composite and 7.3 4. Units

2383 FWSRHOFD Output FW T/H State RE 50 FWS model flow path density. Referencel , Section 5.5, 6.7 and Lbm/FtA3 7.34. _

2384 FWSPEXT Output FW T/H State RE 50 FWS model flow path external pressure. Referencel , Section 5.5, PsIa I_ I_ I_16.7 and 7.3.4.

2385 FWSWMAS Output FW T/H State RE 50 FWS model flow path mass flow rate. Referencel , Section 5.5, 6.7 Lbm/sec , I I and 7.3.4. __-_ __-

2386 FWS_W0 Output FW T/H State RE FWS model flow path volumetric flow. Referencel , Section 5.5, 6.7 Gal/min and 7.3 4.

2387 FWSW Output FW T/H State RE 50 FWS model flow path volumetric flow. Referencel , Section 5.5, 6.7 Gal/min III_ and 7.3 4.

2388 FWSHPATH Output -W T/H State RE 50 FWS model flow path flow enthalpy. Referencel Section 5.5, 6.7, BtuA/bm _ I _ and 7.3.4. - ,

2389 FWSOCURR Output FW RE 50 FWS model flow path heat transfer. Referencel , Section 5.5, 6.7 Btulsec and 7.3 4. .

2390 FWSRESV Output FW RE 50 FWS model flow path valve flow resistance. Referencel , Section Composite - 5.5, 6.7 and 7.3 4. Units

2391 FWSRES Output FW RE 50 FWS model flow path total resistance. Referencel , Section 5.5, Composite

1 6.7 and 7.3 4. Units

2392 FWS_HEXT Output MW T/H State RE 50 FWS model flow path ext node enthalpy. Referencel , Section 5.5, BtuA/bm 6.7 and 7.3 4.

2393 FWSRHOEXT Output FW T/H State RE 50 FWS model flow path ext node density. Referencel , Section 5.5, Lbm/FtA3 .. 6.7 and 7.3 4.

2394 FWSRP Output FW RE 50 FWS model flow path pump resistance. Referencel , Section 5.5, Composite

-_6.7 and 7.3 4. Units

2395 FWSPS Output FW RE 50 FWS model flow path pump head. Referencel , Section 5.5, 6.7 PsId

and 7.3 4.

2396 FWS_SUMP Output -'W RE 50 -NS model flow path pressure error. Reference1 , Section 5 5, 6.7 Psid and 7.3 4. - . .

2397 FWS_GPMCOR Output FW RE 50 FWS model flow path density correction. Referencel , Section 5.5, Composite 6.7 and 7.3.4. Units

2398 FWS_NDIN Input MW Model IN 50 FWS model flow path Input node ID.- Referencel , Section 5.5,6.7 Pointer

- - _ _ __ Design and 7.3.4.._-_-

2399 FWSNDOUT - Input FW Model IN 50 FWS model flow path output node ID. Referencel , Section 5 5, 6.7 Pointer

R...... Design and 7.3 4. _ _ _ _ _

2400 FWS_NDEXT Input FW Model IN 50 FWS model flow path external node ID. Referencel , Section 5.5, Pointer

I _Design 1 6 7 and 7.3.4. _



Index Lonq Variable Name Input/ System System System Variable's Type Dimen- Definition Units No. Output Alt. 1 Alt. 2 Function slons

2401 FWSNCPUMP Input FW Model IN 50 FWS model flow path pump ID Referencel, Section 5.5, 6.7 and Pointer Design 7 3 4

2402 FWSICPUMP Output FW IN 50 FWS model flow path pump status. Referencel , Section 5 5, 6.7 Flag I and 7.3 4

2403 FWSICK Input FW Model IN 50 FWS model flow path check valve flag. Referencel , Section 5 5, Pointer Design 6.7 and 7 3 4

2404 FWS_IMF Output FW IN 50 FWS model flow path calculation flag. Referencel , Section 5 5, 6 7 Pointer and 7.3.4.

2405 FWS._POSISO I/O FW RE 50 FWS model path isolation valve position. Referencel , Section 5 5, Fraction 6 7 and 7.3 4.

2406 FWSCVAFLO Output / FW RE 50 FWS model path check valve flow area. Reference 1 , Section 5.5, Fraction lnit 6 7 and 7 3.4.

2407 FWSCVRESMN Input/Init FW RE 50 FWS model path check valve flow resistance. Referencel , Section Composite 5 5, 6 7 and 7 3 4 Units

2408 FWSCVDPMIN Input/init FW RE 50 FWS model path check valve minimum DP. Referencel , Section Psid 5 5, 6 7 and 7 3.4.

2409 FWSNFLO Input FW Model IN FWS model network number of paths. Reference1 , Section 5 5, Counts Design 6 7 and 7 3 4

2410 FWS_KEY Output FW IN FWS model any fw pumps on flag. Referencel , Section 5.5, 6.7 Flag and 7.3.4.

2411 FWS_FDNODE Partition FW RE 400 FWS model node partition Partition 2412 FWSPEXTN Input FW T/H State RE 20 FWS model external node pressure. Referencel , Section 5.5, 6.7 Psia

I_ and 7 3 4 2413 FWSHEXTN Input FW TiH State RE 20 FWS model external node enthalpy Referencel , Section 5 5, 6.7 Btu/lbm

I land 7 3.4. 2414 FWS_P0 Output FW T/H State RE FWS model node pressure. Referencel , Section 5.5, 6.7 and Psia

1734 2415 FWS_P Output / FW T/H State RE 30 FWS model node pressure Referencel , Section 5.5, 6.7 and Psia

Init 734 2416 FWSHNODE Output / FW T/H State RE 30 FWS model node enthalpy Referencel , Section 5 5, 6 7 and Btu/lbm

Init 734 2417 FWSRHONOD Output FW T/H State RE 30 FWS model node density. Referencel , Section 5 5, 6.7 and 7 3.4. Lbm/FtA3 2418 FWSWEXTF I/O FW T/H State RE 30 FWS model node ext flow. Positive out of node. Typically used to Lbm/sec

represent leakage flow out of system. Reference1, Section 5.5, 6.7 and 7 3 4

2419 FWSHEXTF I/O FW T/H State RE 30 FWS model node external flow enthalpy = node enthalpy for Btu/lbm leakage flow leaving a node.. Referencel , Section 5.5, 6.7 and 7.3.4.

2420 FWS_AEXTF Input FW T/H State RE 30 FWS model node extemal flow leakage area used to calculate the Ft2

leakage flow rate given node pressure and leakage flow path external node pressure below.. Referencel , Section 5.5, 6.7 and

1___ 1734 1

WCAP-I5996-NP, Revision 0 G-183


Index Lona Variable Name - -, - Input I System System System Varlable'st, Type Dimen- Definition " .. Units

No. - Output Alt.,1- Alt. 2. Function slons ,

2421 FWS_PEXTF 1/0 FW T/H State RE 30 FWS model node external leakage flow back pressure used to Psia

calculate leakage flow.. Referencel , Section 5.5, 6.7 and 7.3.4.

2422 FWSWSUM Output FW RE 30 FWS model node flow error. Referencel , Section 5.5, 6.7 and Lbm/sec

1 7.34.

2423 FWSIMN Output FW IN 30 FWS model node network masking flag. Referencel, Section 5.5, Pointer 6.7 and 7.3 4.

2424 FWS._NNOD Input FW Model IN FWS model network number of nodes. Referencel, Section 5.5, Counts

Design 6.7 and 7.3.4. 1

2425 FWSNEXTN Input , FW Model IN FWS model network number of extnodes. Referencel , Section Counts

.I Design 5.5, 6.7 and 7.3 4.

2426 FWSNPSGMFW Input FW SG Model IN 4 FWS model SG main fw path ID. Reference1 , Section 5.5, 6.7 and Pointer

Design 7.3.4.

2427 FWSNPSGECO Input FW SG Model IN 4 FWS model SG economizer fw path ID. Referencel , Section 5.5, Pointer.

Design 6.7 and 7.3.4.

2428 FWSNPSGAFW Input FW SG AFW Model , IN 4 FWS model SG emergency/aux fw path ID. Referencel , Section Pointer

-_ _ Design 5.5, 6.7 and 7.3.4.

2429 FWS,_NPFWLB Input FW Model IN 4 FWS model MFWLB path ID. Referencel , Section 5 5, 6.7 and Pointer

-Design 7.34. 1 "

2430 FWS, AFWLB Output FW RE 4 FWS model MFWLB flow area (local) F•t2

2432 FWSNSG Output FW IN FWS model number of SG (local) Pointer

2433 FWS_FDVALV Partition FW __ RE 1000 FWS model valve partition Partition

2434 FWS STROKE I/O FW RE 30 FWS model valve demand (per cent) Percent

2435 FWSPOSIT Output FW RE 30 FWS model valve position. Referencel , Section 5 5, 6.7 and 7.3.4. Percent

2436 FWSVCW Output FW RE 30 FWS model valve flow coefficient. Referencel , Section 5.5, 6.7 Composite

and 7.3.4. Units

2437 FWS_TOPN Input FW Component RE 30 FWS model valve stroke open time. Referencel , Section 5.5, 6.7 Seconds

_Design and 7.3.4.

2438 FWSTCLOS Input FW Component RE 30 FWS model valve stroke close time. Referencel , Section 5.5, 6.7 Seconds

Design _ and 7.3.4.

2439 FWSTLAG Input FW - Component RE 30 FWS model valve actuator lag. Referencel , Section 5.5, 6.7 and Seconds Design 7.34.

2440 FWS CVP Input FW Component RE 200 FWS model valve CV vs Position. Referencel , Section 5 5, 6.7 Composite

-_Design and 7.3.4. Units

2441 FWSSTP Input FW Component RE 200 FWS model valve position vs CV. Referencel , Section 5.5, 6.7 Fraction

CD si n and 7.3.4.

2442 FWSNPATH Input FW Model IN 30 FWS model valve path location ID. Referencel , Section 5.5, 6.7 Pointer

Design and 7.3.4.

2443 FWSNTABLE Input, FW Model.- IN 30 FWS model valve CV table ID. Referencel , Section 5.5, 6.7 and Pointer

S .... . .... Design 7.3.4.

2444 FWSNPTV Input FW IN 10 FWS model valve CV table no of pts. Referencel , Section 5.5, 6.7 Counts

and 7.3.4.

2445 FWSINDEXF Output FW IN 30 FWS model valve CV table Index. Referencel , Section 5.5, 6.7 Pointer

and 7.3.4.

U_- 1154.WCAP-15996-NP, Revision 0


Index Long Variable Name Input System System System Variable's Type Dimen- Definition Units No_. Output Alt. 1 Ait. 2 Function slons 2446 FWSNVMFV Input FW Model IN 4 FWS model Main Feed Valve ID Referencel , Section 5 5, 6 7 and Pointer

Design 7.3.4. 2447 FWSNVBFV Input FW Model IN 4 FWS model Bypass Feed Valve ID Reference1 , Section 5.5, 6 7 Pointer

Design and 7 3 4 2448 FWSNVAL Input FW Model IN FWS model number of valves. Referencel , Section 5.5, 6.7 and Counts

Design 73 4 2449 FWSNHDV Input FW Model IN FWS model number of Heater Drain valves. Referencel , Section Counts

Design 5 5, 6 7 and 7 3 4 2450 FWSNVHDV Input FW Model IN 3 FWS model heater drain valve ID Referencel , Section 5 5, 6 7 Pointer

Design and 7 3 4 2451 FWSNAFWVT Input FW AFW Model IN FWS model total number of AFW valves Referencel , Section 5 5, Counts

Design 6 7 and 7 3 4 2452 FWSNVAFW1 Input FW AFW Model IN FWS model AFW valve 1 ID. Referencel , Section 5.5, 6.7 and Pointer

I Design 7 3 4. 2453 FWSNTABFV Input FW Model IN FWS model number of fw valve tables Referencel, Section 5 5, Counts

Design 6 7 and 7 3 4 2454 FWS FDPUMP Partition FW RE 1200 FWS model pump partition Partition 2455 FWSSPDMD I/O FW RE 20 FWS model pump speed demand. Referencel , Section 5.5, 6.7 Fraction

and 734 2456 FWS SPEED Output FW RE 20 FWS model pump speed Referencel , Section 5 5, 6 7 and 7 3 4 Fraction 2457 FWSTAUON Input FW Component RE 20 FWS model pump speed lag (increasing). Reference1, Section Seconds

Design 55,6 7and734 2458 FWSTAUOFF Input FW Component RE 20 FWS model pump speed lag (decreasing). Referencel , Section Seconds

Design 5 5, 6 7 and 7.3 4 2459 FWSHT Input FW Component RE 200 FWS model pump head vs flow tables Reference 1 , Section 5 5, Feet

Design 6 7 and 7 3 4 2460 FWSWT Input FW Component RE 200 FWS model pump flow vs head tables. Referencel , Section 5.5, Gal/mmn

Design 6 7 and 7.3 4. 2461 FWSBTABLE Input/mit FW Component RE 200 FWS model pump BTABLE vs flow Referencel , Section 5 5, 6 7 Composite

I Design and 7 3 4 Units 2462 FWSATABLE Inputhmit FW Component RE 200 FWS model pump ATABLE vs flow Referencel , Section 5 5, 6.7 Composite

Design and 7 3 4 Units 2463 FWSNPMPTH Input FW Model IN 20 FWS model pump path ID. Referencel , Section 5.5, 6.7 and 7 3 4 Pointer

Design 2464 FWSNTABP Input FW IN 20 FWS model pump perf table ID. Referencel , Section 5.5, 6 7 and Pointer

734 2465 FWSNPTP Input FW IN 10 FWS model pump table no of pts. Referencel , Section 5.5, 6 7 Counts

and 7.3 4. 2466 FWSNPMPMFW Input FW Model IN 4 FWS model pump MFP ID. Referencel , Section 5 5, 6 7 and 7.3 4. Pointer

Design 2467 FWSNPMPEFW Input FW Model IN 4 FWS model pump AFW/EFW pump ID. Referencel , Section 5 5, Pointer

Design 6 7 and 7 3 4.



Index Long Variable Name , Input I System System System Variable's Type Dimen- Definition • , - , - Units

No.. , -- Output Alt. 1 AlL 2 Function , slons, - , - .....

2468 FWSNPTHMFP Inputinit FW Model IN 4 FWS model pump MFP path ID. Referencel Section 5.5, 6.7 and Pointer

Design 7.3.4.

2469 FWS.NPUM Input FW Model IN FWS model number of pumps. Referencel , Section 5.5, 6.7 and Counts I . Design 7.3.4.

2470 FWS.NTABFP Input FW Model IN FWS model number of fw pump tables. Referencel , Section 5.5, Counts

- - Design 16.7 and 7.3 4.

2471 FWS_NMFWP Input FW Model IN FWS model number of mfw pumps. Referencel , Section 5.5, 6.7 Counts

Design and 7.3.4.

2472 FWSNEFWP Input FW Model IN FWS model number of efw pumps. Reference1 , Section 5.5, 6.7 Counts Design and 7.3.4.

2473 FWSFDHEAT Partition FW RE 500 FWS model fw heater partition - Partition

2474 FWSTPWR Output -FW "_ RE FWS model turbine power. Referencel , Section 5.5, 6.7 and 7.3.4. Fraction

2475 FWS_TQLAG Input FW Component RE 9 FWS model fw heater heat xfer tau. Referencel , Section 5.5, 6.7 Seconds

Design and 7.3.4.

2476 FWSHTRHOV Input FW Component RE 9 FWS model fw heater thermal mass. Referencel , Section 5.5, 6.7 Lbm

Design and 7.3 4.

2477 FWSPWRTBL Input FW Component RE 90 FWS model fw heater turb pwr vs 0. Referencel , Section 5.5, 6.7 Percent

Design -' and 7.3.4. _

2478 FWSQPTBL Input FW Component RE 90 FWS model fw heater 0 vs turb pwr. Referencel , Section 5.5, 6.7 Btu/sec

_ _ _Design - and 7.3.4. _

2479 FWS._HTRHMX Input FW Component RE 90 FWS model fw heater max enthalpy. Referencel , Section 5.5, 6.7 Btu/ibm

Design -and 7.3.4.....

2480 FWSTPOWR Input FW Plant Design RE 10 FWS model fw Htr Dm turb pwr table. Referencel , Section 5.5, 6.7 Percent and 7.3.4.

2481 FWS-TWHDP Input FW Plant Design RE 10 FWS model fw Htr Dm flow vs turb pwr. Referencel , Section 5.5, Lbm/sec - -6.7 and 7.3 4.

2482 -FWSTENHDP Input FW Plant Design RE 10 FWS model fw Htr Dm enth vs turb pwr. Referencel , Section 5.5, BtuAbmn 6.7 and 7.3 4.

2483 FWS..MAXTAU Input FW Component RE 9 FWS model fw heater max tau. Reference1 , Section 5.5, 6.7 and Seconds

Design 7.34.

2484 FWSjFDPOS0 Output FW IN 9 FWS model fw heater table index. Referencel , Section 5.5, 6.7 Pointer

and 7.3 4.

2485 FWSHFWBIAS Input FW RE FWS model fw enth bias to tune fw enth. Reference1 , Section 5.5, Btu/ibrn 6.7 and 7.3.4.

2486 FWSNPHEAT Input FW Model IN 9 FWS model fw heater path location ID. Referencel , Section 5.5. Pointer

Design - 6.7 and 7.3 4. - .

2487 FWSNHTBL Input FW Model IN 9 FWS model fw heater table no of pts. Reference1 , Section 5.5, 6.7 Counts

- _ - -Design - - and 7.3 4.

2488 FWSNHT Input FW - Model IN FWS model number of fw heaters. Referencel , Section 5.5, 6.7 Counts

Design and 7.3 4. - -_--___

2489 FWSNHDPTBL Input FW Model IN FWS model fw htr dm table no of pts. Referencel , Section 5.5, 6.7 Counts

2489-Design and 7.3.4.

2490 nFWSnFDMODL Partition FW - RE 288 FWS model fw model misc controls Partition

WCAP-15996-NP, Revision 0 U-Loo

Table G.1: Dictionary Listing Index Long Variable Name Inpout System System System Variable's Type Dlmen- Definition Units

N.Output Alt. 1 Alt. 2 Function slons 2491 FWSNRCIRC Input FW Model IN FWS model no of recirc flow cntds. Referencel , Section 5 5, 6.7 Counts

Design and 7 3 4 2492 FWSFWRCPB Input FW Controller RE 20 FWS model pump recirc control PB. Referencel , Section 5.5, 6 7 Percent Setpoint and 7.3 4 2493 FWSFWRCRE Input FW Controller RE 20 FWS model pump recirc control reset Referencel , Section 5.5, Seconds Setpoint 6.7 and 7 3 4 2494 FWSFWRCSP Input FW Controller RE 20 FWS model pump recirc control setpt Reference1 , Section 5 5, Gal/mm Setpoint 6 7 and 7.3 4. 2495 FWS_FWRCIR Input FW Controller RE 20 FWS model pump recirc cntrl instr range Referencel , Section 5.5, Gallons Setpoint 6 7 and 7 3 4. 2496 FWSFWRCOUT Output FW Controller RE 20 FWS model pump recirc control output Referencel, Section 55, Fraction State 6 7 and 7 3 4. 2497 FWS_FWRCINT Output FW Controller RE 20 FWS model pump recirc control integral Reference I, Section 5.5, Fraction State 6.7 and 7.3.4. 2498 FWSNPTHRC Input FW Model IN 20 FWS model pump recmrc cntrl path ID. Referencel , Section 5.5, 6.7 Pointer Design and 7 3 4 2499 FWSNVALRC Input FW Model IN 20 FWS model pump recirc cntd valve ID. Reference1 , Section 5.5, Pointer

__Desian 6 7 and 7.3 4. 2500 FWSNPMPRC Input FW Model IN 20 FWS model pump recirc cntrl pump ID. Referencel, Section 5 5, Pointer Design 6 7 and 7 3.4. 2501 FWS_IAUTORC Input/Init FW Flag IN 20 FWS model pump recirc cntd auto flag Referencel, Section 5 5, Pointer

.6 7 and 73 4 2505 FWSDCLMASS Output FW T/H State RE 4 FWS model downcomer line mass. Referencel , Section 5.5, 6.7 Lbm and 7.3 4

2506 FWSECLMASS Output FW T/H State RE 4 FWS model economizer line mass. Reference1 , Section 5 5, 6 7 Lbm and 7.3.4.

2507 AFWSFLOW I/O FW AFW T/H State RE 4 Auxiliary feedwater flow rate. Reference1 , Section 5 5, 6 7 and Lbm/sec 734 "2508 FWS_LINEMASSES Output FW T/H State RE 4, 2 FWS steady state feed line mass. Referencel , Section 5.5, 6 7 Lbm and 7 3 4. 2509 FWSFDSYST Partition MN RE 10000 FWS model fw system eqn partition Referencel , Section 5.5, 6.7 Partition and 7 3 4

2510 NONCONDCOMMON Segment RE 9000 Species and noncondensibles transport Segment 2511 RCSSPECIESCONSTANTS Partition RE 61 Species Constants Partition Partition 2512 NUMSOLUTES Input RCS IN Number of dissolved solute species exclusive of non- Counts

condensibles(NC), where Solutes (SO)+NC <= 20. This parameter sets the expected count for other partition variables. Reference

_ _ SOLUTS1, Sections 4 15, 5 8 1 1 2513 HALF_LIFE_SOLUTES Input RCS RE 20 Radioactive decay half lives of dissolved species For stables Seconds solutes, the value for this variable is set to 0 0 sec Nitrogen-16 carries a short half life which should be set for proper tracking of N

7 1 _ 1_ 16. Reference 1, Sections 4 15, 5 8



Index Long Variable Name . Input System System System Varlable's•, Type Dlmen- Definition', Units' No. - Output _ Alt. I Alt. 2 Function slons - • '• ° '

2514 CONCRATIOSTMLIQ Input RCS RE 20 Measure of each solute's relative solubilities in liquid & steam. Fraction Concentration ratio stm,liq = Cstmmaxt(Cstmmax+Cliqmax) [0 0,1.01 Reference 1, Sections 4.15, 5 8.

2515 CONCMAX Input RCS RE 20 Maximum concentration of each species in solution Composite I_ I I _I (LBM/LBPPM,...) Reference 1, Sections 4.15, 5.8. Units

2516 IDTYPESPECIES Partition IN 20 Identifying pointers for the species. Partition

2517 IDTYPESOLUTE Partition IN 15 Identifying pointers for the solutes. Reference 1, Sections 4.15, Pointer 7.2.7.

2518 IDTYPEBORON Input RCS IN Identifying pointer for boron. Reference 1, Sections 4.15, 7.2.7. Pointer

2519 IDTYPEN16 Input RCS IN - Identifying pointer for N-16. Reference 1, Sections 4.15 7.2.7. Pointer

2520 IDTYPEIODINE Input RCS IN Identifying pointer for iodine. Reference 1, Sections 4.15, 7.2.7. Pointer

2521 IDTYPEXENON Input RCS IN Identifying pointer for xenon. Reference 1, Sections 4.15, 7.2.7. Pointer

2522 ID_TYPEPART Input RCS IN Identifying pointer for particulates. Reference 1, Sections 4.15, Pointer 7.2.7.

2523 IDTYPENONC Partition IN 5 Identifying pointers for the nonconds. Reference 1, Sections 4.15, Pointer 7.2.7.

2524 IDTYPEHYD Input RCS IN Identifying pointer for hydrogen. Reference 1, Sections 4.12, 7.2.7. Pointer

2525 IDTYPE-NIT Input RCS IN Identifying pointer for nitrogen. Reference 1, Sections 4.12, 7.2.7. Pointer

2526 IDTYPEAIR Input RCS IN Identifying pointer for air. Reference 1, Sections 4.12. 7.2.7. Pointer 2527 RCSNONCOND-CONSTANTS Partition RE 65 Noncondensibles constants Partition Partition

2528 NUMNONC Input RCS IN No. of non-condensible species, NC <= 5 Reference 1, Sections Counts 4.12, 7.2.7.

2529 NONC_K_DISSOLVE Input RCS RE 5 NC gas dissolution coefficient, for each species, Ilbsec-ft2-delconc. Composite If the concentration of the NC within the liquid In the node is less Units than saturated , then separated gas may dissolve. The rate of dissolution Is directly proportional the dissolution coefficient, stm-liq surface area, concentration of dissolved no and the specific volumes of the stm & lig. Reference 1, Sections 4.12, 4.15.

2530 NONC_MW Input RCS RE 5 Molecular weights of non-condensible. Reference 1, Section 4.12. Composite I I_ I Units

2531 COREN16_MULT Input RCS Core RE Production constant for N-16. The generation rate of N-16 = gC / POWUSER_QC (fission power fraction) * COREN16 MULT. power-fraction Reference 1, Sections 4.15, 5.8, 7.2.7.

2532 CONDLNONCFRAC Input RCS RE 2 Condensation efficiency In the presence of non-condensible gases. Fraction - When the node's gas fraction QUALNONCSEP_TOT Is at

COND_NONCFRAC(1) or below, condensation of steam can occur at full efficiency. When the node's gas fraction Is at

S - .... COND-NONCFRAC(2) or above, the condensation efficiency Is zero, and no steam condensation can occur. Between these points, the condensation efficiency is Interpolated. Reference 1, Section 4.12. _

2533 CONDNONODEGMULT Input RCS RE 50 Condensation degradation with non-condensibles. Reference 1, Dimensionless Section 4.12. 1



Index Long Variable Name Input/ System System System Variable's Type Dimeno Definition Units No. Output Alt. I Alt. 2 Function sions 2534 RCSPRZRSPRGASENTR Input RCS RE Constant for gas entrainment in pzr spray. The rate of entrainment Dimensionless

= rcs-przrspr.gasentr* pjlow.spray gas quality in the pzr stm space Reference 1, Section 4.12

2535 RCSSPECIESNODES Partition RE 2300 Node species state Partition 2536 MASSNONCDIS Output RCS RE 50, 5 Nodal mass of each dissolved non-condensibles Reference 1, Lbm

Section 4.12, 4.15, 7.2.7. 2537 MASSNONCDISTOT Output RCS RE 50 Nodal mass of Total dissolved non-condensibles. Reference 1, Lbm

Section 4 12, 4.15, 7.2.7. "2538 RCSCONCSOLUTE Output RCS RE 50, 20 Node concentrations of all dissolved solute species. Composite

Rcs.conc-solute(I) = solute (k) mass / mass tot(I) Reference 1, Units Section 4.15, 7.2.7.

2539 RCSCUMSOLU Output RCS RE 50, 20 Node solute accumulation rate: production+net flow+dissolution Composite rate Reference 1, Section 4.12, 4 15. Units

2540 RCS-NONCOND NODES Partition RE 1450 Node noncondensables state Partition 2541 MASSNONCSEP Output RCS RE 50, 5 Mass of each non-condensible in the steam/gas space of each Lbm

node Reference 1, Section 4.12, 7.2.7. 2542 MASSNONCSEP_TOT Output RCS RE 50 Total mass of all non-condensibles in the steam/gas space of each Lbm

node Reference 1, Section 4.12, 7 2.7 2543 QUALNONCSEP Output RCS RE 50, 5 Quality of each non-condensible in the nodal steam/gas space. Fraction

Xg(l,k) = mass-nonc-sep(l,k)/(mass-stm(l)+ mass-nonc-sep-tot(I)). Reference 1, Section 4.12

2544 QUALNONCSEPTOT Output RCS RE 50 Quality of all non-condensibles in nodal steam/gas space, or the Fraction I_ sum of all the qual-non-sep(l,k). Reference 1, Section 4.12.

2545 RCSCUMNONC Output RCS RE 50, 5 Per node, each non-condensible accumulation rate: net flow in + Lbm/sec separation of dissolved gas from the liquid to the steam space I Reference 1, Section 4.12, 4 15

2546 CONDNONC Output RCS RE 50 Node rates of non-condensible dissolution Reference 1, Section Lbrn/sec 4 12, 4,15

2547 PPRESNONC Output RCS RE 50, 5 Partial pressures of each non-condensible in each node. Psia Calculated using the ideal gas law: Ppres-nonc(k) = R*Mass-nonc-sep(k)/nonc.mw(k)

*(Temp-nonc+459.7)/Pvolnonc_tot. Reference 1, Section 4 12

2548 PPRESNONCTOT Output RCS RE 50 Sum of partial pressures of all the non-condensibles in the steam Psia space of each node (I.e. the sum of ppres.nonc). This variable is limited to a 10 psVsec rate of increase for numerical stability. Reference 1, Section 4.12

2549 PPRES STM Output RCS RE 50 Node steam partial pressures Reference 1, Section 4 12 Psia 2550 PVOLNONCTOT Output RCS RE 50 Total volume of separated non-condensible gas This equates to Ft3

the steam/nc or "free" space in each node. Reference 1, Section I_ I_ I_ 1_ _412. 1 1



Index Long Variable Name Input System System System Variable's Tvyp Dimen. Definition, Un,- - , NO.No:; ,', ;•' Output ,Alt 1 Alt. 2 Function slons

2551 TEMP_NONC Output PCS RE 50 Temperature of non-condensible In each node. If no steam space Is Degree F present in a given node, then the liquid temperature is used. It Is assumed that the temperature of the non-condensibles is the same

as the steam temperature. Reference 1, Section 4.12.

2552 PRESSSTM LAST Output RCS RE 50 Last Nodal Pressure -does not include gas Psia

2553 PTEMPSTM_SAT Output RCS RE 50 Steam saturation temperature at its partial pressure. Related Degree F variables are TEMPSTM & TEMP_SAT. Reference 1, Section 4.12.

2554 RCS SPECIES PATHS Partition RE 3000 Path species state Partition

2555 P_CONC_SOLU Output RCS RE 150, 20 Path concentrations of each dissolved species, inclusive of Intemal, Composite

I I I external, leak, etc. paths. Reference 1, Section 4.15, 5.8, 7.2.7. Units

2556 RCS NONCONDPATHS Partition RE 1080 Path noncondensables state Partition 2557 P FLOWNONC Partition RE 150 Path flows of all separated non-condensibles. Lbm/sec

2558 PFLOW_NONCMOM Output RCS RE 100 Mom path flows of all separated non-condensibles. Reference 1, Lbm/sec _ Section 4.12,7.2.7.

2559 P_FLOW_NONC_NONM Output RCS RE 50 Non-mom path flows of all separated non-condensibles. Reference Lbmfsec

1 1, Section 4.12, 7.2.7.

2560 P_FRAC_NONC Output RCS RE 150, 5 Path concentrations of each of the separated non-condensibles in Fraction j :each flow path (momentum and nonmomentum). Reference 1,

_ ___ Section 4.12, 7.2.7.

2561 P_FRAC_NONC_TOT Output RCS RE 150 Path concentrations of the sum of separated non-condensibles in Fraction each flow path (momentum and nonmomentum). It Is the sum of

____ p_jrac nonc for each path. Reference 1, Section 4.12.

2562 MASS_NONC_SEP_RCS Output RCS RE Total mass of all non-condensibles in the steam/gas space of the Lbm RCS. This equals the sum of mass._nonc_.sep.tot(l). Reference 1, Section 4.12, 7.2.7.

2563 FLOWDPMAXERR Output RCS RE Max error of predicted pressure relative to calculated pressure Psid

2564 FLOWDPNODEMAXERR Output RCS IN Node at which maximum error FLOWDPMAX occurred. Point6r

2565 FLOWDPPRINT NODE Input RCS IN Print DP data for this node number (for debug) Pointer

2566 MASSNONC_RCS Output RCS RE RCS non-condensible total mass (separated & dissolved), sum of all L:bm species and all nodes. Reference 1, Section 4.12,4.15.

2567 RCSPRZROEFF Input PZR RCS RE Pressurizer condensation efficiency when non-condensibles are Fraction present. Reference 1, Section 4.12.

2568 RCSPRZR 0 COND Output PZR RCS RE Pressurizer condensation heat transfer. Reference 1, Section 4.12. Btu/sec

2569 MASSNONC_DISRCS Output RCS RE Total mass of dissolved non-condensibles In all RCS nodes Lbm combined. Reference 1, Section 4.12,4.15,7.2.7.

2571 CORERELESOLU Output RCS RE 20 Solute release rate in core (fuel failure). Reference 1, Section 4.12, Composite - - _. 4.15, 5.8. Units

2572 RCS-NONCOND-INTERF Partition RE 38 Noncondensible interfaces partition Partition

2573 P_FLOW_AUXSP._NONC Output RCS RE 5- Auxiliary spray non-condensibles flow, for each species. This Lbm/sec should equal the concentration of non-condensibles in the charging lines "the aux. spray flow rate in Ibm/sec. Reference 1, Section 4.12. 1

G- 190WCAP- 15996-NP, Revision 0


Index Long Variable Name Input / System System System Variable's Type Dlmen- Definition Units No. ... _Output Alt. 1 Alt. 2 Function slons

2574 SIS_RCS_NONC Input RE 6, 5 Noncondensables inflow via SI lines. Reference 1, Section 4 12, Lbm/sec Partition 7 2 7.

2575 SISIRCSNONC Input RCS RE 5 Each non-condensibles inflow via SI line, CL 1. Reference 1, Lbm/sec

I I _ I Section 4 12, 7 2 7. 2576 SIS2_RCS_NONC Input RCS RE 5 Each non-condensibles inflow via SI line, CL 2. Reference 1, Lbm/sec

Section 4.12, 7 2 7. 2577 SIS3_RCS_NONC Input RCS RE 5 Each non-condensibles inflow via SI line, CL 3. Reference 1, Lbm/sec

Section 4 12, 7 2 7 2578 SlS4_RCS_NONC Input RCS RE 5 Each non-condensibles inflow via SI line, CL 4. Reference 1, Lbm/sec

Section 4.12, 7.2.7.

2579 SIS5_RCSNONC Input RCS RE 5 Each non-condensibles inflow via SI line, HL 1 Reference 1, Lbm/sec Section 4.12, 7 2.7

2580 SIS6_RCSNONC Input RCS RE 5 Each non-condensibles inflow via SI line, HL 2. Reference 1, Lbm/sec Section 4 12, 7 2 7

2581 GSVESNONC Input RCS RE Non-condensibles inflow to vessel via Gas System. Reference 1, Lbm/sec

I _ Section 4.12, 7.2.7.

2582 GSPRZRNONC Input RCS RE Non-condensibles inflow to pressurizer via Gas System. Reference Lbm/sec

1 1, Section 4 12, 7 2 7

2583 GSSPECIES Input RCS IN Species of Gas System gas (from IDTYPESPECIES) that is Pointer entering the RCS via any of the inputs SISn_RCS_NONC, GSVESNONC or GSPRZRNONC. Reference 1, Section 4 12, 727


Table G.2: Variables Dictionary in Tree Structure

index Vari able Name! No. Short Long

1 CHR CHMRCO!0ON 2 PLABEL PLANTDATALABEL 3 PFILE - PLANTrDATA.FILENAME 4 PTITLE PLANTDATA.TITLE 5 PTIME PLANTDATA.TIME 6 PDATE PLANTDATADATE 7 SLABEL SNAPSHOTLABEL 8 . . SFILE SNAPSHOTFILE.NAME 9 . STITLE SNAPSHOT-TITLE

10 . STIME SNAPSHOT-TIME 11 . SDATE SNAPSHOT-DATE

12 . CTLT CTLTITLE

13 PLT PLTDATA 14 PLTO1 UNUSED-VAR-PLT01 15 . DUMMY] CORERADOUTDUMMY 16 . TNMAXL CHT_NUM-LINPROP 17 . TNPROP CHTTIME.STPNUM 18 DRCS PLT-RCS 19 DRDESN PLT-RCS_.DESIGN 20 . NUMSG NUMSG

21 . . DRTYPE PLTRCSTYPE

22 DNPROP NUMPROPHEATERS 23 DNBACK NUMBACKHEATERS 24 . . DNCHGS NUM CHGSPUMPS

25 . . DNSPRA RCS_NUM_MSPRAYVLVS 26 . . DNPORV RCS_NUMPORVS

27 . . DNPRSV RCS_NUM_SAFETYVLVS 28 . . DMODIN MODINIT 29 . . DMDINV MOD0INITV

30 DNODE PLTRCSNODE 31 . NODENO PLT-1RCS-NODALIZATION 32 . . .. NODETO RCS_NODETOTALS

33 ....... .. NUMNOD NUMNODES 34 ....... .. NNODSE NUM_.NODESSEC 35 ....... .. NNODSG NUMSGNODES 36 ....... .. NNODHL NUXHLNODES 37 ....... .. NNODSL NUMSLNODES 38 ....... .. NNODCL NUMCL.NODES 39 . . . . NODENU RCSNODENUMBERS

40 ....... .. NODEHL RCS.NODEHL 41 .... ...... NHLI NODEHLl 42 ......... .. NHL2 NODEHL2 43 ......... .. NHL3 NODE_.L3 44 ......... .. NHL4 NODEHL4 45 ....... .. NODESG NODESG 46 ......... .. NSG1H NODESGIH 47 .......... .NSGIC NODE._SGIC 48 ......... .. NSG2H NODESG2H 49 ......... .. NSG2C NODE_SG2C 50 ......... .. NSG3H NODESG3H 51 ....... .. NSG3C NODESG3C 52 ........ .. NSG4H NODESG4H 53 ......... .. NSG4C NODESG4C 54 ....... .. NODECL NODE.CL ' 55 ......... .. NCL1 NODECL1 56 ......... .. NCL2 NODECL2 57 ......... .. NCL3 NODECL3 58 ......... .. NCL4 NODECL4 59 ........ NODESL RCSNODESL 60 .... ...... NSGIP NODESGIP 61 ......... .. NSG2P NODE_SG2P 62 ......... .. NSG3P NODESG3P 63 ......... .. NSG4P NODESG4P 64 ....... .. NODEOT RCS-NODEOTHERS 65 ......... .. NCORE NODECORE 66 ......... .. NPRZR NODEPRZR 67 ......... .. NUHEAD NODEUHEAD 68 ........... NANNUL NODE-ANNUL 69 ......... .. NCEASH NODE-CEASH 70 . . . NODGEO RCSNODEGEOMETRY

71 . . . . NODEA NODE-AREA 72 . . . . NZTOT NODEHEIGHT

73 . . . . NELBOT NBOT

DimenT sions Definition

CH 336 Character variables for snapshot ID CH Plant data title character variables CHM Plant data file description CH Plant data file title CH Plant data file time stamp CH Plant data file date stamp CH Snapshot file character variables CH Snapshot file description CH Snapshot file title CH Snapshot file time stamp CH Snapshot file date stamp CH 1000 Titles of controllers RE 25000 Restore-only plant data RE 15 Unused Partition RE 3 Unused Variable IN Unused Variable IN Unused Variable RE 2350 Restore-only RCS plant data IN 10 RCS design features IN Number of steam generators IN Unused Variable IN Number of proportional heaters IN Number of backup heaters IN -Number of charging pumps IN Number of przr main spray valves IN Number of przr PORVs IN -Number of przr safety valves LO Plant data initialization cue LO Plant data initialization cue - data

RE 900 Restore-only RCS plant node data IN 50 RCS nodalization data IN 6 RCS total number of nodes per group IN Total number of nodes (50 max) IN Number of sectionalized nodes (1 max) IN Number of SG nodes (2 per SO, 16 max) IN RCS number of hot leg nodes IN RCS number of suction leg nodes IN RCS number of cold leg nodes IN 30 -RCS node numbers IN 4 RCS hot leg nodes IN Hot leg 1 node number IN Hot leg 2 node number IN Hot leg 3 node number IN Hot leg 4 node number IN 16' Array of SG node numbers IN SG tube hot side node number~loop 1 IN SG tube cold side node number, loop 1 IN SG tube hot side node number, loop 2 IN SO tube cold side node number, loop 2 IN SG tube hot side node number,loop 3

-IN -SG tube cold side node number, loop 3 IN SO tube hot side node number, loop 4 IN SG tube cold side node number, loop 4 IN 4 Array of cold leg node numbers IN - Cold leg node number, loop 1 IN Cold leg node number, loop 2 IN Cold leg node number, loop 3 IN Cold leg node number, loop 4 IN 4 RCS suction leg node numbers IN SO outl plen. and suct. leg node loop IN SG outl plen. and suct. leg node loop IN SG outl plen. and suct. leg node loop IN - SG outl plen. and suct. leg node loop IN 10 RCS remaining nodes IN Core node number IN -- Pressurizer node number IN Upper head node number IN Annulus node number

IN CEA shroud node number RE 250 RCS node geometry variables RE 50 Node cross sectional area RE 50 Node height RE 50 Node bottom elevation

units

Segment Partition Character Character Character Character Partition Character Character Character Character Character Segment Dimensionless Dimensionless Dimensionless

,Dimensionless Partition Partition Counts Dimensionless Counts Counts Counts Counts Counts Counts True False True False Partition Partition Partition Counts Counts Counts Counts Counts Counts Partition Partition Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Partition

1 Pointer 2 Pointer 3 Pointer 4 Pointer

Partition "Pointer

,Pointer Pointer

'Pointer Pointer

,Partition Ft^2 Feet Feet



Index No.

74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99

100 101 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 . 126 127 128 129 130 131 132 133 134 135 136 . 137 . 138 139 140 141 142 143 144 145 146 147 -

DimenTM sions

Variable Name: Short Long

. NGEOM N_GEOM . NOSECT NSECTIONS

NODETH RCS.NODETHVARS . NXLIQ N_HEAT_XFERLIQ

* - . NXSTM N_HEAT.XFERSTM . . . NXCON NHEAT_XFER_CONT - - - NXBOT N__JEATXFERBOT

NWLMXC N_HEATCAP NXBOIL NXFER_BOIL NXINJ N_XFER_INJ NXSPOF XFERSURFPOFF NXSPON XFERSURFPON NAMULT AREA_INJ_MULT

NSECT RCSNODESECTIONALIZED NUMSEG RCSPRZR_NSECT APZR RCSPRZRASECT HPZR RCSPRZR_HSECT NIJMANN RCSANNULNSECT AANN RCS_ANNULASECT

* . ZANN RCS4ANNUL_HSECT . - ASECVA N_AREASECT * . ZSECVA NHEIGHTSECT DPATH PLTRCS_PATH . PATHNO RCSPATHSNODALIZATION . . PATHTO RCSPATHSTOTALS

PNMOM NUMPATHSJ.MOM . . PNEXT NUMPATHS_EXT

PNLEAK NUM_PATHS_LEAK PNINT NUM_PATHS_INT PNPATH NUM_PATHS PNSB NUM_SMLBRK PNHL NUM_PATHS_HL PNCL NUM_PATHSCL PNNONM NUMPATHSNONM PNCHGS RCS_NUMINCHGS PNLET RCS_NUMOUT_LDNS PNDRN RCSNUMOUT_RCWDRAINS

* . PNSDC RCSNUMOUTSDC . . PNSIS RCSNUMINSIS . . PNRCP RCSNUIOAXRCP . - PNCHGM RCSNUMMAXMCHGSIN

* . PNLETM RCS_NUMMAXLDNSOUT PNDRNM RCS_NUMMAXDRAINSOUT PNSDCM RCS_NUMMAXSDCOUT PNSISM RCSNUMM.A_SISIN PNMOMM RCS_NUMMAX_MOM

PATHNU RCSPATHSJNUMBERS - PSURGE PATHSURGE

. PANCOR PATHANNULCORE

. PCORUH PATHCORE_UHEAD

. PSPRAY PATHSPRAY . . PLBLOC PATHLB-LOCA

PPUMP PATHPUMP PATHHL PATHHL PATHCL PATH_CL PATHSG PATHSG PUCEA PATHJUCEA

PATHG RCSPATHS_GEOMETRY PINLET P_NODE_INLET . PIMOM RCS_P_NODEINLETMOM

. . PINMOM RCS_P_NODE INLETNONM . . * PIEXT RCS_PATHEXTPNODEIN

PIRCP RCSRCPLEAXPNODEIN PICHGS RCSCHGSPNODEIN PILET RCSLDNS-PNODEIN PIDRN RCSRCWNPNODEIN PISDC RCS_SDC_PNODEIN

. PISIS RCSSISPNODEIN

- PIGAS RCS_GASPNODEIN . PILEAK RCSPATHLEAKPNODEIN

PISGTR RCSSGTRPNODEIN - - . PISB RCSSBLOCAPNODEIN

. . . PIRODE RCSRODEJ_PNODEIN

. . PIORIN RCSORING_PNODEIN

IN IN RE RE RE RE RE RE RE RE RE RE RE RE IN RE RE IN RE RE RE RE RE

IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN RE IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN

50 50 500 50 50 50 50 50 50 50 50 50 50 100

3 3

3 3 1,22 1,22 1400 60 25

35

4 8 8 4

1300 150 100 50 25 4 4 4 1 2 8 2 17 8 4

Definition

Node geometry indicator Sections in node (node I max 22, rest 1) RCS node thermo-hydraulic constants Node wall-to-liq overall heat tr coeffs Node wall-to-stm overall heat tr coeffs Node wall-to-cont overall heat tr coeffs Node bottom wall-to-fluid ht coef Node wall heat capacity Node boiling condensation coef Node liquid injection condensation mult Node surface condensation coef(pump off) Node surface condensation coef(pump on) Interfacial condensation area mult RCS sectionalized nodes variables Number of area sections in przr Przr cross-sectional areas Przr section heights Number of sections in annulus low plen Annulus cross-sectional areas Annulus section heights Cross sect area of section(node,section) Height of section (node.section) Restore-only flow path RCS plant data RCS paths nodalization variables RCS total paths Number of momentum paths Number of external flow paths (25 max) Number of leak flow paths (17 max) Number of internal flow paths (8 max) Total number of flow paths Number of SB leak flow paths (4 max) Number of hot leg flow paths (4 max) Number of cold leg flow paths (8 max) RCS number of non-momentum paths Number of RCS-CHGS connections Number of RCS-letdown connections Number of RCS-RCW drain connections Number of RCS-SDC connections (I max) Number of RCS-SIS connections Maximum number of RCP paths Max. number of CHGS conn to RCS Max. numb. of ldns connect to RCS Max. numb. of drains to RCW from RCS Max. numb. of SDC connect to RCS (out) Max. numb. of SIS connect to RCS (in) Maximum number of momentum paths RCS path numbers Surge line path number Annulus-to-inner vessel path number Upper head-to-inner vessel path number Pressurizer spray path number Large break LOCA path number (mal 038) RCP paths array (lla, llb, 12a, 12b) Inner vessel-to-hot leg path array Array of cold leg path nos.: lla,b.12a,b Top of SG tube bundle path number CEA to upper head path number RCS paths geometry variables Path inlet node number (all paths) Path inlet number (momentum) Path inlet number (non momentum) External paths inlet node RCP leak inlet node Charging inlet node RCS- letdown inlet node RCS RCW drains inlet node RCS shutdown cooling inlet node RCS safety injection inlet node RCS gas injection inlet node Leak paths inlet node RCS SG tube rupture inlet node RCS small break LOCA inlet node RCS rod ejection small break inlet node RCS o-ring seal inlet node

WCAP-15996-NP, Revision 0

Units

Pointer Counts Partition Btu/sec-degF Btu/sec-degF Btu/sec-degF Btu/secft^2degF Btu/degF Btu/sec-degF Dimensionless Btu/secft^2degF Btu/secft-2degF Dimensionless Partition Counts Ft^2 Feet Counts Ft^2 Feet Ft 2 Feet Partition Partition Partition Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Counts Partition Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Partition Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer

G- 193

I, 11


Index V a r i a b l e N aim e: No. Short L MM

148 ........ PILB RCS_LBLOCAPNODEIN IN 149 ....... PINT RCSPATHINTPNODEIN IN 150 ... ....... .. PISPRA RCS_SPRAYPNODEIN IN 151 ... ....... .. PIBLED RCS_ESPRAYBLEEDPNODEIN IN 152 ... ....... .. PIPZRR RCS_PRZRRELIEFPNODEIN IN 153 ... ....... .. PIUHR RCSOUHEADRELIEF-PNODEIN IN 154 . ... PEXIT PNODEEXIT IN 155 . ... PEINIT P_ELEV_INLET RE 156 ....... .. PEMOM RCS_P_ELEVINLETYOM RE 157 ....... .. PENONM RCS_P_ELEVINLETNONM RE 15B ......... .. PEEXT -RCSPATHEXT.PELEVIN RE 159 ... ....... .. PERCP RCS_RCPLEAKPELEVIN RE 160 ... ....... .. PECHGS RCSCHGSPELEVIN RE 161 ... ....... .. PELET RCS_LDNS_PELEVIN RE 162 ... ....... .. PEDRN RCS_RCWPELEVIN RE 163 ... ....... .. PESDC RCSSDCPELEVIN RE 164 ... ....... .. PESIS ,RCS_SIS-PELEVIN RE 165 ... ....... .. PEGAS RCSGASPELEVIN RE 166 ......... .. PELEAK RCS_PATHLEAKPELEVIN RE 167 ... ....... .. PESGTR RCSSGTRPELEVIN RE 168 ... ....... .. PESB RCS_SBLOCAPELEVIN RE 169 ... ....... .. PERODE RCSRODEJPELEVIN RE 170 ... ....... .. PEORIN RCS_ORINGPELEVIN RE 171 ........... PELB RCSLBLOCAPELEVIN RE 172 ......... .. PEINT RCS_PATHINT_PELEVIN RE 173 ... ....... .. PESPRA RCSSPRAYPELEVIN RE 174 ... ....... .. PEBLED RCSSPRAYBLEEDPELEVIN RE 175 ... ....... .. PEPZRR RCSPRZR.RELIEFPELEVIN RE 176 ... ....... .. PEUHR RCS_UHEADnRELIEF._PELEVIN RE 177 . . .. PEEXIT PELEVEXIT RE 178 . . . . PGEOM PGEOM IN

179 . . . . PRADII PRADIUS RE 180 . . . . PTLOA PATHSTLOA RE 181 . . . . PKXPOS PATH_KLOSS_POS RE

182 . . . . PKXNEG PATH_KLOSSNEG RE 183 . . . . PAREA PAREA RE 184 . . . . PLDIAM PATH_.LENDIAM RE 185 . . . . PDIA PDIAMfHYD RE 186 DINVES PLT_RCS_VES RE 187 DUPMIN PRES_ATWSMIN RE 188 DUAMIN PAREA_ATWS_MIN RE 189 DUPMAX PRESEATWS_MAX RE 190 DUAMAX P.AREA_ATWSJAX RE 191 DUAROD PAREA_RODEJ RE 192 ZOUTUP NTOP_UPLEN RE 193 ZINUP N_BDTJUPLEN RE 194 XPOSUP KLOSSUPLEDPOS RE

195 XNEGUP KLOSSUPLEN_NEG RE 196 CORBOT COREBOT RE 197 CORTOP CORETOP RE

198 FLA AREA-CORE RE 199 DIHACE HA_CEASCORE RE 200 PUPCEA PATH_CEALOW IN 201 PCEAUH PATHSCEAUP IN

202 DINCEA NUMNCEAS IN 203 DIHCEA CEASDIST RE 204 DIEXBO EXCOREBOT RE 205 DIEXTO EXCORETOP RE 206 DIEXMP MAP_EXCORE IN

207 DIFBY RTRV_BYPASS RE 208 DIFTLT RCSKWEIGHTJHTILT RE 209 DIHAUI HAUHEADfCORE RE 210 DPRZR PLTRCS0PRZR RE 211 DHNUM NUM__EATERS IN 212 DHBURN BURNOUTJIEATER RE 213 DWABLD AREA_BLEED._MIN RE

214 DHHCAP HCAP_HEATER RE 215 DHHA XFER.HEATER RE

216 DHOHMS RESIHEATER RE 217 DHLTOP TOP_HEATERS RE

218 DHVMAX VOLTJHEATER.MAX RE 219 DPLRTD LEVLPRZRRTD RE 220 DPLRBO LEVLREFBOT RE

221 DPLRTO LEVL_REFTOP RE

Dimensions Definition

8

2

100 150 100 50 25 4 4 4 1 2 8 2 17 8 4

8

2

100 100 100 100 100 100 100 100 100 60

10

4,4

40

6

6 6 6

Units

-RCS large break LOCA inlet node Pointer RCS internal paths inlet node Pointer RCS przr spray inlet node Pointer RCS przr spray bleed inlet node Pointer Przr relief valves inlet node Pointer

-* Upper head relief valves inlet node Pointer Path exit node number (momentum paths) Pointer Path inlet elevation (at circle center) Feet Inlet elevation (mom. paths) Feet Path inlet elevation (non momentum) Feet External paths inlet elevation Feet RCP leak inlet elevation Feet Charging inlet elevation Feet RCS- letdown inlet elevation Feet RCS RCW drains inlet elevation Feet RCS shutdown cooling inlet elevation Feet RCS safety injection inlet elevation Feet RCS gas injection inlet elevation Feet Leak paths inlet elevation Feet RCS SG tube rupture inlet elevation Feet RCS small break LOCA inlet elevation Feet RCS rod ejection small break inlet eleva Feet RCS o-ring seal inlet elevation Feet RCS large break LOCA inlet elevation Feet RCS internal paths inlet elevation Feet RCS przr spray inlet elevation Feet RCS przr spray bleed inlet elevation Feet Przr relief valves inlet elevation Feet Upper head relief valves inlet elevation Feet Path exit elevation (at circle center) Feet Path end geom(0-3=ptcircu semi,l semi) Pointer Path radii at end(not related to parea) Feet Combined inertia length/area CdMom/dt) Composite Units Geometric forward k-factor Dimensionless Geometric reverse flow k-factor Dimensionless Path flow area Ft^2 Path length-to-diameter ratio Dimensionless Path hydraulic diameter Feet Restore-only inner vessel RCS plant data: Partition Atws min head seal leakage pressure Psia Atws min head seal leak area ýFt^2 Atws pressure for max head seal leak Psia Atws area at max head seal leak -Ft^2 CEA ejection leak area Ft^2 Top elev of UP part of inner vessel node Feet Bottom elev of UP part of IV node Feet UP geometric form loss coef, + flow Dimensionless UP geometric form loss coef, - flow Dimensionless Active core bot elev (rel to node bot) ý Feet Active core top elev (rel to node bot) Feet Active core flow area ,Ft^2 CEA to IV wall heat trans coef (hA) Btu/sec-degF Inlet path, UP to CEA guide tubes Pointer Exit path, CEA to UH Pointer Number of CEAs (65 max) Counts Traveling distance of CEAs Feet Excore detector elev, bottom (est) 'Feet Excore detector elev, top (est) - Feet Excore detector - RCS model mapping Pointer Fraction of vessel flow bypassing core Fraction Coeff. for cold leg to hot leg mixing Fraction Upper head to IV heat transfer coef (hA) Btu/sec-degF Restore-only pressurizer RCS plant data Partition Total number przr heater banks (6 max) Counts Heater burnout (set large remove limit) Btu Przr spray bleed line min area 'Ft^2 Heater gross heat capacity Btu/degF Heater overall heat transfer coef Btu/sec-degF Heater electrical resistance Ohms Top elev of przr heaters Feet Maximum przr heaters bus voltage Volts Level of przr rtd Feet Bottom level of przr reference leg Feet Top level of przr reference leg Feet



Index V a r i a b l e N a m e: No. Short Long

222 DVLREL LEVLRELIEF 223 DVGPOR DESIGN_FLOW_PORV 224 DVGPS1 DESIGNFLOWSAFETYI 225 DVGPS2 DESIGNFLOW_SAFETY2 226 DQTANK PLTRCSQT 227 DQPN2 PRESN2 228 DOVOL VOLUtQT 229 DQHT HEIGHT_QT 230 DQMASS MASSQTMAX 231 DQPRUP QTRUPTURESPOINT 232 DRCP PLTRCSRCP 233 DRNUM NUMPUMPS 234 DRFRAC FRACTABL 235 BAN BAN 236 BVN BVN 237 BAD BAD 238 BVD BVD 239 BAT BAT 240 BVT BVT 241 BAR BAR 242 BVR BVR 243 HAN HAN 244 HVN HVN 245 HAD HAD 246 HVD HVD 247 HAT HAT 248 HVT HVT 249 HAR HAR 250 HVR HVR 251 HANC HANC 252 HVNC HVNC 253 HADC HADC 254 HVDC HVDC 255 HATC HATC 256 HVTC HVTC 257 HARC HARC 258 HVRC HVRC 259 HVOID FRAC_HD_TABL 260 HMUL HD_DEG_TABL 261 RRSPDR RATEDPUMPSPEED 262 RRVFLO RATEDVOL_FLOW 263 RRDD RATED_PUMFL_DENS 264 RRPHD RATED_PUMP_HD 265 RRPHT RATEDPUMPTORQ 266 RRSYNC RATEDPUMPSYNCH 267 DRNPOL. NUMIPOLES 268 TTWIFR WIND_TORQJULT 269 DRVBUS RATED_BUS_VOLT 270 DRTNUM NPTS_TAB 271 DRSLIP SLIPTAB 272 DRTORQ TORQTAB 273 DRDTDW DTDW_TAB 274 DRCURR CURRENTTAB 275 DRPLEK PRESSLDN 276 DRVRAT RCP-VOLTRATED 277 DRFRAT RCP_FREQRATED 278 DCONST RCSCONST 279 DPCONS RCSCONSTPRZR 280 DPWMUL PRZRSPRAY_MULT 281 DPHMUL PRZRJHEATERMULT

282 DPPMUL PRZRPORVMULT 283 DPSMUL PRZRSAFETY_MULT 284 DPVMUL PRZR_VENT_MULT 285 DPRTAU PRZRRELIEFRTDTAU 286 DPQMUL PRZR_QT_MULT 287 DPFMUL RCS_PRZRFLASH_MULT 288 DPFLSH RCS_DM_FLASH_PRZR 289 DPLSAT RCS_LEVL_SAT_PRZR 290 DPDMAX RCSDFLASHMAX_PRZR 291 DVKUP VLVPRZR_KLOSSUP 292 DVKDWN VLVPRZRKLOSSDOWN 293 DUCONS RCSCONSTUHEAD 294 - DUKCOR RTRVKLOSSCORE 295 DUVMUL RTRV_VENT._MULT

Dimenn-, sions

RE RE RE RE RE 10 RE RE RE RE RE RE 450 IN RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 11 RE 4 RE 4 RE 4 RE 4 RE 4 RE 4 IN RE RE IN RE 22 RE 22 RE 22 RE 22 RE RE RE RE 200 RE 15 RE RE RE RE RE RE RE RE RE RE RE RE RERE RE RE

10

Definition

Level of relief valve noz (rel to bot) PORV design flow rate Safety valve 1 design flow Safety valve 2 design flow Restore-only quench tank RCS plant data QT nitrogen supply pressure QT total volume QT height assuming con circ cross sect QT maximum mass of water Q T. rupture disk setpoint pressure Restore-only main coolant pump plant dat Number of main coolant pumps (4 max) Ind var inter for RCP homologous curves RCP torq homolog curve (normal +f,+s) RCP torq homolog curve (normal +f,+s) RCP torq homolog curve (eng diss -f,+s) RCP torq homolog curve (eng diss -f,+s) RCP torq homolog curve (turbine -f,-s) RCP torq homolog curve (turbine -f,-s) RCP torq homolog curve (abnormal +f,-s) RCP torq homolog curve (abnormal ÷f,-s) RCP head homolog curve (normal ÷f,+s) RCP head homolog curve (normal ÷f,+s) RCP head homolog curve (eng diss -f.+s) RCP head homolog curve (eng diss -f,+s) RCP head homolog curve (turbine -f,-s) RCP head homolog curve (turbine -f.-s) RCP head homolog curve (abnormal +f,-s) RCP head homolog curve (abnormal .f,-s) RCP diffr head homolog (normal *f,+s) RCP diffr head homolog (normal .f,+s) RCP diffr head homolog (eng diss -f,+s) RCP diffr head homolog (eng diss -f,+s) RCP diffr head homolog (turbine -f,-s) RCP diffr head homolog (turbine -f,-s) RCP diffr head homolog (abnormal +f,-s) RCP diffr head homolog (abnormal .f,-s) RCP head degradation void frac (ind var) RCP head degradation multiplier Rated pump speed Rated pump volumetric flow Rated pump density Rated pump head Rated pump torque Pump synch speed at rated frequency Number of poles per putmp Windage/friction torque constant Rated bus voltage (for input units conv) Number of points in motor tables Electrical slip Electrical torque multiplier Unused Variable Electrical current multiplier Letdown line pressure (for RCP leaks) RCP rated voltage RCP rated frequency RCS tunable constants RCS pressurizer tunable constants Mult on przr. spray (excluding aux.) Multiplier on total pressurizer heat Multiplier on PORV relief flow rates Multiplier on safety valve flow rates Multiplier on przr vent valve flows First order lag constant - relief RTDs Mult on control flow from QT to przr Multiplier for przr flashing calc Flashing rate przr sat region Pressurizer sat level (u bound) Max del flash in przr per step Loss coeff, przr to przr-relzef-valves Loss coeff, przr-relief-valves to Q.T RCS upper head tunable constants Core pressure drop factor for buoyancy Multiplier on head vent valve flows

Unite

Feet Lbm/sec Lbm/s ec Lbm/sec Partition Psia Ft^3 Feet Lbm Psia Partition Counts Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Shaft RPM Ft^3/sec Lbm/ft^3 Feet Ft-lbf Shaft RPM Counts Ft-lbf Volts Counts Dimensionless Dimensionless Dimensionless Dimensionless Psia Volts Hertz Partition Partition Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Seconds Dimensionless Dimensionless Lbm/sec Feet Lbm/sec Composite Units Composite Units Partition Dimensionless Dimensionless



index No.

296 297 298 299 300 301 302 303 304 305 306 307 308 309 310 311 312 313 314 315 316 317 318 319 320 321 322 323 324 325 326 327 328 329 330 331 332 333 334 335 336 337 338 339 340

DVAVWT DVAUH DVAPOI DVAPS1 DVAMOI DVAPC0 DVAPQT DVAMSP DVAQTG DVAQTC DVANC

341 DM504 342 DPSDE 343 DPSEQ 344 DPHDT 345 DPTDT 346 DPDGMC 347 DPLRIC 348 DULRIC 349 DUFRIC 350 DPFRIC 351 DPLBOI 352 DSDP 353 DSDPl2 354 DSDPW 355 DSDPWI 356 DPCRFI 357 DRCMUI 358 DRCMIN 359 DPTMSI 360 DPM034 361 DVTMA3 362 DRFRUI 363 DRTRUI 364 DPHAXI 365 DPLSB( 366 DUORFL 367 DRFREF 368 DRAREI 369 DRDAMJ

PLT_VLVAREAUHEAD_CONT PLTVLVAREAUHEADQT

Z PLTVLVAREAPRZRSPORV P PLTVLVAREA_PRZR_SAFETY V PLTVLVAREA_.PRZRMOV 0 PLTVLVAREAPRZRSCONT SPLTSVLVAREAPRZRQT

P PLTVLVAREA.PRZRMSPRAY PLTVLVAREAQT.GWS PLTVLVAREAQTCONT PLTVLVAREAQT._NSUPPLY

RCSMOREVARIABLES_504-RO RCSPRZRDHSPRAYEQ RCSPRZRISPRAYEQ RCSPRZRSDT.SUBH RCSPRZR_.TAUDTSUB

X RCSDWSOLIDSDC G RCSPRZRVENTRIG G RCSJUHEADI.VENTRIG G RCS-UHEAD-VENTRIG-FRAC G RCSPRZR.VENT-RIG-FRAC L RCSPRZRL..BOIL

RCSSGDP_.ADD 2RCSSG1112_DPADD

RCS_SG_DPWMULT I RCSSG1112_DPWMULT L RCSCRITFLOW_CHECK L RCPCAVITSGDPtMULT I RCP_CAVITSGDPFRAC_.MIN P RCSPRZRJMSPRAYTAU 4 RCSPRESCOARSEJMAL034 C RCS_PRZR.VLVHIMAZTAU B RCPFRSPRUBRATCH B RCPTORQ..RUBRATCH W RCSPRZR_HA&_WALL 0 RCS-PRZRLVLDTSUBC L RCSP-ORING-FAIL F RCPFLOWREF F RCP..ADMIFLOWCORRMULT P RCPDELAMPS

DimenTyp EsE!n Definition

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

Units

Multiplier on head seal pressure Dimensionless Multiplier heat transfer CEA-core Dimensionless Multiplier uppper head ring seal area ' Dimensionless

2 Core-in mixg fctr: (l)lowflow, (2)high -Fraction 2 Core-out mixg fctr: (1)lowflow, (2)high Fraction

CEA in k factor multiplier Dimensionless 13 RCS coolant pump tunable constants Partition 4 Coolant pump rotor/flywheel interia 'Lbf*ft2

Coolant pump heat rate multiplier Dimensionless SFrac mom-inr to motor when sheared shaft Fraction

Unused Variable Dimensionless Unused Variable Dimensionless Unused Variable Dimensionless

-Unused Variable Dimensionless 4 Tunable constants for RCS loop varbl. Partition

--- Multiplier on cont. heat xfer rates 'Dimensionless SG tube rupt. flow multiplier Dimensionless

6 RCS quench tank addressable constants Partition Multiplier on nitrogen supply flow Dimensionless Multiplier on nitrogen flow to gws Dimensionless Multiplier on quench tank vent flow Dimensionless Fract. surge flow to QT to rupt. disk Fraction

133 General RCS addressable constants Partition


DUPMUL RTRV_.EAD_SEAL_.MULT DURMUL RCSQ...CEA.CORE_.MULT DUAMUL RCS_UHEAD_RINGSEAL_MULT DIIMIX RTRVMIXINLET DIOMIX RTRV_MIX_OUTLET DUKCEA RCS_CEAIN_KTERM

DRCONS RCS_CONSTPUMPS PPINER RCPMOM_INERTIA DRQMUL RCP_HEATMULT DRISPL RCPMOMINERTIASPLIT DRVNOR RCPVIBERNORM

DRVMAX- RCPVIBRMAX DRVTIM RCPVIBR_.TIME DRVSPD RCPSPEEDDERIVSHAKE

DLOOPC RCSCONST_LOOP DCONMU- RCS_CONTHEATMULT DSGTRM RCS_SGTR_FLOWMULT

DQCONS RCS_CONSTQT DQNMUL QTN2_MULT DQGMUL QTGWS_.MULT DQVMUL QT_VENT.MULT DQSFRC QTFLOW_FFRAC

DGENC RCSCONST_.GENERAL DNIDPE RCSITER_DP DNIDPN RCSITERDPJNE DNIDHN RCS_ITERDHNE DNDMUL RCSDROPCONDMULT

DPKMUL RCS_KLOSS_MULT DNSMUL RCS_CONDSURFMULT DLCONS RCSCONST-LEAKS

DLSPMU RCSSUPERCRITFLOWMULT DLSBMU RCSSUBCRITFLOWJ4ULT DGPMA CONVGP&_AREA

DVAREA PLT_RCS_VLVAREA

Equil. pressure search convergence band Psia Non-eq pres search conv band on pressure Psia Non-eq pres search conv band on enthalpy Btu/lbm Multiplier droplet condensation (node 'Dimensionless Geometric losses multipliers Dimensionless Surface condensation multiplier Dimensionless Constants for leak tables and correla Partition Multiplier supercritical mass flux Dimensionless Multiplier leak tables (subcrit. cond Dimensionless Gal/mnm-to-area (nom cond). l-3=SLHL,PR 'Composite Units RCS valve areas ,Ft^2

Area of vent valve from u-head to cont Ft^2 Area vents valves u-head to q-tank Ft^2 Area przr PORVs Ft^2 Area przr safety valves Ft^2, Area przr movs (in series with PORVs) Ft^2 Area vent przr to containment Ft^2 Area vents przr to q-tank (in series) Ft^2 Area main spray control valves Ft^2 Quench tank to gws vent valve area Ft^2

- Quench tank to contain, vent vlv area Ft^2 Valve area nitrogen supply to contain FtA2 RCS more variables spin 413 to 504 RO Partition Przr spray del-enth for equil. Btu/lbm Przr spray del-enth equil flag True False Przr del-temp boil heaters on Del-DegF Przr time constant del-temp subc. Seconds Fast time max SDC del flow przr solid Lbm/sec Przr vent rig flag T=inF=out True False Uhead vent rig flag T=in,F=out True False Frac. nucl. uhead vent rig Fraction Frac. nucl. przr vent rig Fraction' Boiling degradation parameters -Feet Tuning add. inst. SG. delp Psig Tuning add. instrum. SG. delp ,Psig

Multiplier SG delp (coarse, 1 phase) Dimensionless Mult. SO delp (detail. 1 phase) Dimensionless Mom. paths-crit. flow check True 'False Unused Variable Dimensionless Unused Variable Dimensionless Main spray flow time constant Seconds Press. for switch to coarse nodalzn Psia

RE RE RE RE 50 RE 100 RE 50 RE 5 RE RE RE 3 RE 25 RE RE 2 RE 4 RE 4 RE 4 RE RE 2 RE 2 RE RE RE RE 41 RE LO RE RE RE LO LO RE RE RE 2 RE RE RE RE LO RE RE RE RE RE RE RE RE RE 2 RE RE RE RE

-Seconds Fraction Composite Units Btu/sec-degF Feet Psia Dimensionless Dimensionless Dimensionless


Przr rel vlvs heat tran. max time cons "RCP frac speed pawls rub on ratchet RCP torque pawls rub on ratchet Przr walls axial overall htcoff. Przr level values for boil (subc.) Press. for vessel O-ring failure Unused Variable Unused Variable Unused Variable

G-196


Index No.

370 371 372 373 374 375 376 377 378 379 380 381 382 383 384 385 386 387 388 389 390 391 392 393 394 395 396 397 398 399 400 401 402 403 404 405 406 407 408 409 410 411 412 413 414 415 416 417 418 419 420 421 422 423 424 425 426 427 428 429 430 431 432 433 434 435 436 437 438 439 440 441 442 443

DimenTMM sions


DUFAST RCSDHEATFASTT_UHEAD FRAC DRVMUL RCPCAVITVI BRHMULT DRLMUL RCP__CAVITLOAD_MULT DEDGDT RCSDWSTPSIT DPTREV RCS_PRZR_VLVREVH_TAU DPPHMU RCS_PHTR.RLDJMULT

. DPBHMU RCSBHTRRLDWMULT - DPVVMU RCSPRZRVLVLVIB_MULT - DLBCLC RCSKTEMPCLLOCA DSGS PLTh_SGS

DSCSIN PLT_SGS INTERNAL DSGDES SG_DESIGN ASPTBL ASPTBL

ASPTB1 ASP_TBLDSGN1 ASPTB2 ASPTBLDSGN2

HSPTBL HSPTBL HSPTBI HSPTBLDSGN1 HSPTB2 HSPTBLDSGN2

. VSTTBL VST_TBL VSTTB1 VST_TBL_DSGN1 VSTTB2 VSTTBLDSGN2

TBL2NU TBL2_NUM HT3TBL HT3_TBL - HT3TB1 HT3_TBL DSGNl * HT3TB2 HT3_TBLDSGN2

V3TBL V3_TBL * V3TBl V3_TBLDSGN1 . V3TB2 V3_TBL-DSGN2 TBL3NU TBL3_NUM ASEPSG ASEP SG EVAPSS EVAPSS.ALPHA SPACE SPACE PERIM PERIM SFCONI SFCONCIO SGU12 SG_U12 SGU23 SG_U23

- SGV2AC SG_V2_ACTIVE SGV4MX SGV4_MAX SGV5MX SGV5_MAX TAURCI TAURCI TAUIO TAU_10 TAUPT TAUPT TAUXE TAU_XE VOLSGS VOLSGS HT4MAX SG_HT4_MAX W32FLC W32-FLOW-COEFF DSREFL SGCREFLEGS

DSNREF SGREFNUM DSBREF SGREFBOT DSTREF SG-REF TOP DSTDN TAUREFLGCDN DSTUP TAUREFLGOUP

DSATUB SGCTUBEAREA DSETUS ELEVTUBESHEET DSECON SG_ECONOMIZER

DSHEAT PLTSGS_HEAT DSAFLO ATUBESMAXCS DSAHT ATUBES_MAX_HT QSG100 QSGIOG QSGTBL QSG_TBL TMPTBL, TMP_TBL RTUBES RTUBES SGMTCP SGMTCP DSDHYD SGT__HYDDIAM DSHWAL SGCHCONV DSRWAL SG_RWALL DSAWAL WALLAREA DSMCPW WALLMCP DSAEHT ATUBESMAXECJHT

DMSLH PLT SGS_MSLH ASLMAX ASL_MAX

- DMHAWI HAWALLIMSLH - DMEAWO HAWALLO_MSLH - DMMCPW MCPWALLJMSLH

RE RE RE RE RE RE RE RE RE RE RE IN RE RE RE RE RE RE RE RE RE IN RE RE RE RE RE RE IN RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN RE RE RE RE RE RE LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

3 850 230 4 15,2 15 15 15,2 15 15 15,2 15 15 2 15,2 15 15 15.2 15 15 2 4 4 4 2

2 2 2

2 2 4 18 2 2,3 2,3 2 2 2 4

70 2 2 4 20 20 2 2 2

2 2 2 2 240 2,2

Definition

Frac const for uhead fastt heat Unused Variable Unused Variable SIT del flow per step (loop solid) Przr rel vlvs rev heat tr. time const Przr prop heater rld mult Przr backup heaters rld mult. Przr relief vlvs vabrat mult (slug flow LB LOCA CL2b temp constants Steam generator data constants SG data constants - SG internals Type of steam generator design (=1,2) Table c. s area of evaporator region Table CS area of evap region, design 1 Table CS area of evap region, design 2 Table height in evaporator region Table height in evap region, design 1 Table height in evap region, design 2 Table volume in evaporator region Table volume in evap region, design 1 Table volume in evap region, design 2 No of entries in evaporator geom table Table height in SG downcomer Table height in downcomer, design 1 Table height in downcomer, design 2 Table volume in SG downcomer Table volume in downcomer, design 1 Table volume in downcomer, design 2 No of entries in downcomer geom table Stm separation area at can deck, 100% ss SG evaporator void fraction at 100% s s Unused space Perimeter of tube shroud in lower SG Stripping factr for SG iodine nuc conc Heat trans coeff. between regions I & 2 H t. coeff regions 2 & 3; also 2/4, 3/4 Volume in region 2 to cover tubes Volume of SG economizer region Volume of quenching pool above can deck Time constant on recirculation flow W23 Decay const for iodine nuclide conc. Decay const for particulate nuclide conc Decay const for xenon nuclide conc. SG volume to rain steam isolation valve Height of SG economizer region Dcomer to tube bundle flow coeff, 100%ss SG level measurement taps Number of level instrum reference legs Lower tap ht abov tbsheet (design, leg#) Upper tap ht abov tbsheet (design, leg#) Time const , lvl instr ref leg cooldown Time const , lvl instr ref leg heat-up SG tube internal flow area, one tube Tubesheet elevation above cormmon refrnce SG economizer T=exist, F=none SG data constants - SG heat transfer Primary flow area through tubes SG tubes heat tsfr area, evaporator only Tube heat trans to each SG at 100% power Rosenow heat flux vs dT table, B/hr-ft2 Delta temp for Rosenow heat flux table Thermal resistance of SG tubes, 1/units Total heat capacity of tubes Hydraulic diam of SG tubes primary flow Convective htc outside SG wall Thermal resistance of SG wall, 1/units SG surface area for heat loss to cont. SG wall heat capacity SG tubes heat tsfr area, economizer only SG data constants - steamline & header Steamline flow area (design,line( Inside MSLH wall heat transfer hA Outside MSLH wall heat transfer hA Total heat cap of MSLH pipe wall


Units

Fraction Dimensionless Dimensionless Lbm/sec Seconds Dimensionless Dimensionless Dimensionless Composite Units Partition Partition Pointer Ft^2 Ft^2 Ft^2 Feet Feet Feet Ft^3 Ft^3 Ft^3 Counts Feet Feet Feet Ft^3 Ft-3 Ft^3 Counts Ft^2 Fraction Unused Feet Dimensionless Btu/secft^2degF Btu/secft^2degF Ft-3 Ft-3 Ft^3 Seconds Seconds Seconds Seconds Ft^3 Feet Ft/s*SQRT(lbm) Partition Counts Feet Feet Seconds Seconds Ft^2 Feet True False Partition Ft^2 Ft^2 Btu/sec Composite Units Del-degF Secft^2degF/Btu Btu/degF Feet Btu/secft^2degF Secft-2degF/Btu Ft^2 Btu/degF Ft^2 Partition Ft^2 Btu/sec-degF Btu/sec-degF Btu/degF

G- 197


index V a r i a b I a N a m :s No. Short Long

444 445 446 447 448 449 450 451 452 453 454 455 456 457 458 459 460 461 462 463 464 465 466 467 468 469 470 471 472 473 474 475 476 477 478 479 480 481 482 483 484 485 486 487 488 489 490 491 492 493 494 495 496 497 498 499 500 501 502 503 504 505 506 507 508 509 510 511 512 513 514 515 516 517

DMSLIC SLIFLOWCOEFF DMSLOC SLOFLOWCOEFF DMSLC UNUSED_.FLOW_COEFF VELl00 VEL100 DMVOL VOLMSLH DMAREA MSLB_AREA DIAMAX MSLHMSIV.AMAX DMABY MSLHHMSIVBYPASS-AMAX DMVAMX MSLHVALVE-AMAX DMVIN HSLH.VALVEINLET DMVEX MSLHVALVE-EXIT DMVNUM KSLHVALVENUM DMPATM PATMOSPHERE DMTATM MSLHTATM DMCHKV SLICHECKVALVE DMDPIl SLIDPI00 DMDPOl SLODPI00 ASLMIN ASL_.MIN NUMSL NUMSL

DFWS PLTSGSFWS FWCDEF FWCOEFF DFC10O _FWSYFLOW100 WFW100 WFW1O0 DFAFWB FWLBAREA HTNOZF FWSNOZ.HEIGHT

* . HTNOZ HTNOZ HTNOZE HTNOZECON HTNOZA HTNOZEFW

* DFNPMP NUM_FWSPUMPS DFNJUN NUMFWS.JUNCTIONS DFPJUN FWSPUMP'JUNCTION DFLJUN FWS-LINEJUNCTION

DFJUN FWSJUNCTION DFEJUN FWSECONJUNCTION

DFGTAB FWSPUMPFLOWTABLE DFHTAB FWS-PUMP..HEAD_TABLE DFSTAB FWSPUMPSPEEDTABLE DFGNUM FWSPUMPFLOWNPOINTS DFSNUM FWSPUMPSPEEDNPOINTS DFCPMP FWSPUMPCOEFF DFCVAL FWSVALVECOEFFS

DFCVL FWSVALVECOEFF DFCEVL FWSECONVALVECOEFF

DFCLIN FWSLINECOEFFS DFCLN FWSLINECOEFF DFCELN FWSECONLINE-COEFF

DFVLIN FWSLINEVOLUMES DFVLN FWSVOL DFVELN FWSECONVOL

DFDLIN FWSLINEDIAMS DFDLN FWS-DIAM DFDELN FWSECON_DIAM

DANPMP NUM_AFWPUMPS DSGDB PLTSGSSGBD

DBATNK SGBDACROSS DBHAWI HAWALLISGBD DBHAWO HA-WALLOSGBD DBMCPW MCPWALL_SOBD

.- DBVTNK SGBD_VOL DBCOEF SGBDSGCOEFF

DBSCUR SGBD_SURF_COEFF DBCBOT SGBDBOTSCOEFF

DBHNOZ SGBDSGHTNOZ DBHSUR SGBDSURFHTNOZ DBHBOT SGBDBOTJHTNOZ

* DBHOUT SGBDOUTHTNOZ DBCOUT SGBDOUT-COEFF DBAMAX SGBDRELIEFAMAX

DM2SLH PLT_SGS_HSLH2 DM2SLO NUMMSLH DM2AFR HSLHAFRSL DM2FKB MSLHJFKBRX DM2ACI MSLH-ACROSS DM2AC2 MSLHACROSST

Dimen-. TMme sions Definition,

RE 8 Flow coeff, stm nozzle to MSIV, at 100% RE '8 Flow coeff, MSIV to header, at 100% RE 8 Unused array RE 8 "Steamline velocity at 100% flow RE Header and SL vol from MSIV to turb stop RE Standard area for main steamline breaks RE 2.2 MSIV full-open flow area (design,line) RE 2,2 MSIBV full-open flow area (design,line), RE '50 Steamline ext valves fullopen flow areas IN 50 Steamline ext valves upstream region IN 50 Steamline ext valves downstream regions IN # of stmline ext valvs <50-NUMSG*NUMSL RE Atmospheric pressure RE Atmospheric temperature at MSLH

-LO 2,2 Steamline check valve: Y/N (design,line) RE 8 Press drop, stm nozzle to MSIV, at 100% RE 8 Press drop, MSIV to header, at 100% RE 2,2 Stln restrictor mn area upst(dsgn,line) IN Number of steamlines per steam generator RE 225 SO data constants - main & aux feedwater RE 4 -•FW coeff at 100%. used for #pumps=0 only RE 4 Feedwater flow at 100% power, each SG RE Feedwater flow at 100% power, all SGs RE Standard area for feedwater line breaks RE 2,3 Feedwater nozzle heights RE 2 Height of downcomer'feedwater nozzle "RE 2 Height of economizer feedwater nozzle RE 2 Height of aux. feedwater nozzle IN -Number of feedwater pumps (max 4) IN No. of feedwater flow junctions (max 4) IN '4 ID# of junction feeding from Nth pump IN 4,2 ID #s of junctions feeding'FW lines IN 4 ID# of junction feeding to nth DCFW line IN 4 ID# of 3unction feeding to nth ECFW line RE 15 Flows for FW pump flow/head/speed tables RE 15,8 Heads for FW pump flow/head/speed tables RE 8 Speeds for FW pump flow/head/speed table IN No. of flow entries in FW pump tables IN No. of speed entries in FW pump tables RE 4 Flow coeff, pump discharge to 3unction RE 4,2 Flow coeffs, junction to valve discharge RE 4 Flow coeff,jct to dcomer valve discharge RE 4 Flow coeff,jct to econzr valve discharge RE 4,2 Flow coeffs, valve discharge to SO RE 4 Flow coeff, valve discharge to downcomer RE 4 Flow coeff, valve discharge to econmizer RE 4,2 FW line volumes downstream of valves RE 4 FW line volume after downcomer valve RE 4 'FW line volume after economizer valve RE 2,2 FW line diameters RE 2 FW line diameter after downcomer valve RE 2 FW line diameter after economizer valve IN Number of AFW pumps (max 4) RE, 30 SG data constants - SG blowdown system' RE Cross section area of SGBD tank RE Inside SGBD tank heat transfer hA RE Outside SGBD tank heat transfer hA RE Total heat cap of SGBD tank wall RE -SGBD tank volume "RE 8 Flow coeffs, blowdown nozzles to tank RE 4 -Flow coeffs, surface blowdown nozzles RE 4 Flow coeffs, bottom blowdown nozzles RE 4 Hts of SO blowdown nozzles above tubesht RE 2 Height of SG surface blowdown nozzle RE 2 Height of SG bottom blowdown nozzle RE 2 -Hts above bottom, 2 BD tank outlet nozls RE 2 Flow coeffs, 2 BD tank outlet nozzles ' RE Bd tank relief valve full-open flow area REý 40 -SG data constants - new header model IN Number of MSLH nodes (1 or 2) RE 8 _Stmln restrictor mmn flowarea dnstrm RE 8 Stmln K factor from SO to MSLB RE Stm header cross tie flowarea RE Stm header cross tie flowarea w turbine


Units

Composite Units Composite Units Unused Ft/sec Ft^3 Ft^2 Ft^2 Ft^2 Ft^2 Pointer Pointer Counts Psia Degree F True False Psid Psid Ft-2 Counts Partition Composite Units Lbm/se6 Lbm/sec Ft'2 Partition Feet Feet Feet Counts Counts Pointer ,Pointer Pointer Pointer Gal/min Feet Shaft RPM ,Counts Counts Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Ft^3 ýFt^3 Ft^3 Feet Feet Feet Counts Partition Ft^2 Btu/sec-degF Btu/sec-degF Btu/degF Ft-3 Partition Composite Units Composite Units

'Partition Feet

'Feet Feet Composite Units Ft'2 Partition Counts Ft^2 Composite Units Ft^2 Ft^2

G-198


Index Variabl e Name: No. Short Long

518 . . - DM2KC1 MSLH_FKCROSS 519 . . . DM2KC2 MSLHFKCROSST 520 DCTL PLTCTL 521 . DCNCON CTL_CONTROLLERNUMBERS 522 . . . DCACON CTLAFWSCONTROLLERS 523 . . . DCRCON CTLCEACONTROLLER 524 . . - DCCCON CTLCHGSCONTROLLERS 525 . . . DCFCON CTLFWSCONTROLLERS 526 . . . DCFECN CTL_FWSECOCN_CONTROLLERS 527 - - - DCFPMP CTL_FWS_PUMPCONTROLLERS 528 . . . DCFCOT CTLFWSTRIPCONTROLLER 529 . . DCHCON CTL_HEATER_CONTROLLERS 530 DCLCON CTLLETDOWNCONTROLLERS 531 DCICON CTLMSIV_CONTROLLERS 532 . DCICOT CTL_MSIS_TRIPCONTROLLER 533 . . . DCMCON CTLMSLHCONTROLLERS 534 DCVPOR CTL_PORVOCNTROLLERS 535 DCVPSV CTLPSVCONTROLLERS 536 DCTCON CTLRPS_CONTROLLERS 537 . . . DCECOT CTLSIASTRIPCONTROLLER 538 . . . DCWCON CTL_SPRAYCONTROLLERS 539 . . . DCTACO CTL_TAVGCONTROLLER 540 . . - DCTRCO CTLT_REF_CONTROLLER 541 . . . DCGCOT CTLTURBTRIPCONTROLLERS 542 . . . DCTCOT CTLCORE_TRIPCONTROLLER 543 . . . DCKCUT CTLPOWERCUTBACKCONTROLLER 544 . . . DCGSET CTLTURB_SETBACKICONTROLLER 545 . . . DCGRUN CTLTURBRUNBACKCONTROLLER 546 . . . DCPCOE CTL_PRZRLVLERRCONTROLLER

547 . - . DCPCOP CTLPRZRPROGLVLCONTROLLER 548 . . . DCFBCN CTLFWSBYPSCONTROLLERS 549 . . . DCFICN CTL_FWS_ISOL_CONTROLLERS 550 . DCAVCN CTLAFWSVALVECONTROLLERS 551 DCDNUM CTLATMDUMPNUM 552 DCDPAT CTLATLDUMPPATH 553 DCTANU CTLTAV_NUM 554 DCTAPA CTL_TAV__PATH 555 DCBNUM CTLTURBBYPASSNUM 556 DCBPAT CTLTURB_BYPASSPATH 557 DBADD DBADD 558 DBCOM DBCOM 559 ELEMS ELEMS 560 ELIN ELIN 561 ELTYPE ELTYPE 562 GROUPS GROUPS 563 NOTAB NOTAB 564 PTTAB PTTAB 565 SEQNCE SEQNCE 566 XTAB XTAB 567 YTAB YTAB 568 UNUSED UNUSED 569 DCINIT CTL_INIT 570 INPED INPED 571 INEDSQ INPEDSEQNCE 572 INEDPG INPEDPAGE 573 CTLDBG CTL_DBG 574 DCCONS CTL_CONSTS 575 DCZERO CTLZERO 576 DCHALF CTLHALF 577 DCONE CTLONE 578 DCMONE CTLMONE 579 DCLIMS CTLLIMITS 580 ELMAX ELMAX 581 LSTMAX LSTMAX 582 INMAX INMAX 583 GRPMAX GRPMAX 584 . CTLMAX CTLMAX 585 . TABMAX TABMAX 586 FCTMAX FCTMAX 587 DCWARN CTL_WARN 588 . INEDFL INPEDFILE 589 CHT CHTCOMMON 590 CHTINP CHT_INPUTS 591 . - DTNRAD CHTNREGIONSRAD

DimnenTa slons

RE RE RE IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN IN RE

IN IN IN IN IN RE RE RE LO LO LO IN LO RE RE RE RE RE IN IN IN IN IN IN IN IN IN LO RE RE IN

Definition

Stm header cross tie flow resist Stm header cross tie flow resist w turb

20700 Control module variables 150 Controller numbers 4 AFWS flow controller number

Control rod reactivity controller number 4 Charging pump controller numbers 4 Main feedwater flow controller numbers 4 Economizer FW valve controller numbers 4 Main FW pumps speed controller numbers

Main feedwater trip controller number 2 PZr heater controller numbers propback 4 Letdown flow controller numbers 8 MSI valve controller numbers

MSI signal controller number 50 MSLH valve controller numbers 4 Pressurizer PORV controller numbers 4 Pressurizer safety valves controller #s 20 RPS channel controller numbers

SIAS trip controller number 2 Przr spray controller numbers

Controller number for loop avg temp Controller number for demand ref temp

2 Turb. trip controller nos. (trip/close) Core trip controller number Reactor power cutback controller number Turbine setback controller number Turbine runback controller number Przr level error calc. controller number Przr program level controller number

4 FWS Bypass valve controller number 4 FWS isol valve controller number 14 AFWS valve controller number

Number of MSLH atm. dump valves 10 Path number for MSLH atm. dump valve

Number of tubine admission valves 5 Path number for turbine admission valve

Number of turbine bypass valves 5 Path number for turbine bypass valve 100 Index of state variables in commson 100 Cue to commuon containing state variables 1000 No of elements per controller 10000 Inputs to controller elements 3000 Controller element type cues

Number of controllers 100 No. of entries in user function table 100 Pointer to start of user function table 1000 Order of exectuion of controllers 2000 Ind variable values for user function 2000 Dep variable values for user function

Unused Variable Control system initialization cue Control system structure display cue INPED display order T=seqnce, F=input Lines/page in inped output 0=no paging

1002 Controller debug edit cues 10 Useful constants

Floating point zero (0 0) Floating point one-half (0 5) Floating point one (1 0) Floating point minus-one (-1 0)

10 Dimensioned limits of the control system Maximum total number of elements Maximum total number of last-values Max total number of controller inputs Maximum number of controller groups Dimension of CTL_CONTROLLERNUMBERS Maximum number of user-defined functions Max tot no. of user-defined func entries Warnings display 0/l/2=none/once/always Inped output target T=file, F=console

1500 Core heat transfer segment 50 Core heat transfer model data constants

Number of radial regions in h t. mesh

Units

Composite Units Composite Units Partition Partition Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Counts Pointer Counts Pointer Counts Pointer Pointer Pointer Counts Pointer Pointer Counts Counts Pointer Pointer Undefined Undefined Dimensionless True False True False True False Counts True False Partition Dimensionless Dimensionless Dimensionless Dimensionless Partition Counts Counts Counts Counts Counts Counts Counts Pointer True False Segment Partition Counts



Index variable Name! No. Short Long

592 593 594 595 596 597 598 599 600 601 602 603 604 605 606 607 608 609 610 611 612 613 614 615 616 617 618 619 620 621 622 623 624 625 626 627 628 629 630 631 632 633 634 635 636 637 638 639 640 641 642 643 644 645 646 647 648 649 650 651 652 653 654 655 656 657 658 659 660 661 662 663 664 665

*DTROUT CORE.SADSOUT M4ATTYP MATTYP DTH2 COREJHYD-DIA DTDENS FUEL-DENSITY DTAHT COREJHTAREA TCFMUL CHTCONDSFUELJMULT TCGAP CHTSGAP_{CAP TPSPCR CHT-PRESSSUPERCRIT TCHFMU CHT_CHFMULT TCLEV CHT.CONST.LEV TGAPIN TGAPIN TFHTGN CHTFRACJHTGEN DTNZ CHTNNOD-BO * CHTNUM CHTJNUMNODE DTNFC CHT_.NNODFC

CHTPRP CHTPROPERTIES TESATP CHTrENTH_SATLIQ_M1 TESATL CHTSENTHSATLIQ TESATS CHT_ENTHSATSTM TSSATL CHTSVOLkSATLIQ TSSATS CHT-SVOLSATSTM TTSAT CHT_TEMP_SAT TDHFDP CHT.DHF..DP TDHGDP CHTDHGDP TDTDPS CHTDTSATDP TDTDHS CHT DTSATSDH TDVLDP CHTSDVSATLDP TDVGDP CHT DVSATGDP TDVLDH CHTDVSATLDH TDVGDH CHTDVSATGDH TUWAT CHT_VI SCOSWAT TUSTM CHT_VISCOSSTM TUSATS CHTVISCOSSAT-STM TKWAT CHT_COND_WAT TKSTM CHTSCOND-STM TKSATS CHTCONDSAT-STM TPRWAT CHTPRANWAT TPRSTM CHTPRANLSTM TPRSTS CHTPRANSATSTM TCWAT CHTSPECJHT.WAT TCSATS CHT-SPECHTSATSTM

CHTSTT CHTSTATE TLBOIL CHTDBOILING TOCRIT CUTFLUXCRIT TTERMT CHT-TERM TTERM2 CHT-TERM2 TTCRIT CHT_TEMP_CRIT THNB CHTJHTCOFJNB THSUB CHTHTCOFSUB TFLASH CHT_FLASHRATEJLAST TLMIXL CHT-LEVLMIXJLAST TQAVE CHT_AVGHEATFLUX TTFUEL CHT_TEMP_FUELAV

CHTAXL CHTAXIALOUTPUT CHTAXF CHT-AXIAL-DATAFC . TXFC CHTSQUAL T TTCROS CHTTEMPCROSS

* THFB CHTJHTCOFJFB * TQDNB CHT_FLXDNB * TTNBFC CHTTEMPNBFC

CHTAXB CHT_.AXIALDATA_BO TGSTMB CHT_FLOW_STIBO TKGAP CRT-GAPCOND TQZRWA CHT_HT_GEN_ZRWAT TIHT CHTJIHT TCSTM CHTSPECHTSTM THSTM CHTJHTCOFST TFLUX CHTHTFLUX TTSURF CHTTEMPSURF TQAXIL CFTH_RCSAXIAL_Q

* TQLIQ CHT.HEATLIQ • TQSTM CHTJHEATSTM CHTAXA CHTAXIAL.DATA&ALL * TECOOL CHTJENTHCOOL

DimenT sions

RE IN RE RE RE RE RE RE RE RE RE RE IN IN IN RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN RE RE RE RE RE RE RE RE RE

10 10

11

25

25

475 175 20 20 20 20 20 250 20 20 20 20 20 20 20 20 20 20 20 50 21

Definition

Outer radii of radial regs, C.H.T. mesh Rad reg material (l/2/3=Fuel/Clad/Gap) Core hydraulic diameter Density of uranium fuel Core heat transfer area, clad/coolant Multiplier fuel conductivity Fuel-clad gap thermal heat capacity Pressure for supercrit DNB calculation Multiplier on calculated crit heat flux Constant for level calculation Fuel gap conductance for all axial nodes Heat generated in fuel,gap,clad,coolnt Number of core nodes max 20 Number of core nodes max 20 Not used CHT steam and liquid properties Saturated liq enthalpy - prev time step Saturated liquid enthalpy Saturated steam enthapy Saturated liquid specific volume Saturated steam specific volume Saturation temperature Sat liq enth derivative wrt press Sat stm enth derivative wrt press Sat temp derivative wrt press Sat temp derivative wrt enthalpy Sat liq spec vol derivative wrt press Sat stm spec vol derivative wrt press Sat liq spec vol derivative wrt enthalpy Sat stm spec vol derivative wrt enthalpy Water viscosity Steam viscosity Saturated steam viscosity Water thermal conductivity Steam thermal conductivity Saturated steam thermal conductivity Water Prandtl number Steam Prandtl number Saturated steam Prandtl number Water specific heat Saturated steam specific heat CHT Core average state parameters Flag for heat trans mode TF=boil,fc Critical heat flux Transition boiling term Departure from nucleate boiling term Critical temperature Nucleate boiling heat transfer coef. Heat transfer coef. to subcooled liq. Flashing rate last time step Mixture level last time step Core-wide average heat flux Average temperature of fuel CHT Axially dependant outputs CHT Axially dependant outputs - FC Node coolant quality - fc mode only Crossover temperature Film boiling heat transfer coef. Critical heat flux - forced conv. mode Critical temp. - forced conv. mode CHT Axially dependant outputs - BO Steam flow rate - pool boiling mode. Fuel-clad gap thermal cond. Heat rate of Zr-water reaction Cue for ht. transfer regime by node Steam sp. heat st last prop. calc. Heat transfer coef. to steam Heat flux into moderator Node temp. at clad-moderator interface Total power in core axial section Rod heat transfer to liquid Rod heat transfer to steam CHT Axially dependant outputs - FC&BO Coolant enthalpy at bottom of section


Units

Feet Counts Feet Lbm/ft^3 Ft^2 Dimensionless Btu/ft^3-degF Psia Dimensionless Fraction Btu/hr-ft2-degF Fraction Counts Counts Dimensionless Partition Btu/Ibm Btu/lb•n Btu/ibm Ft^3/lbm Ft^3/lbm Degree F Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Lbmf/ft-sec Lbs/ft-sec Lbs/ft-sec Btu/sec-ft-degF Btu/sec-ft-degF Btu/sec-ft-degF Dimensionless Dimensionless Dimensionless Btu/lbm-degF Btu/Ibm-degF Partition True False Btu/sec-ft^2 Composite Units Composite Units Degree F Btu/secft^2degF Btu/secft^2degF Lbm/sec Feet MegBtu/hr-ft^2 Degree F Partition Partition Fraction Degree F Btu/secft^2degF Btu/sec-ft^2 Degree F Partition Lbm/sec Btu/sec-ft-degF Btu/sec Dimensionless Btu/Ibm-degF Btu/secft^2degF Btu/sec-ft^2 Degree F Btu/sec Btu/sec Btu/sec Partition Btu/lbm

G-200


Index Variabl a Name: No. Short Long

666 . . . TTCOOL CHTTEMPCOOL 667 TRADEX CHT_ROD_RADIAL 668 TTROD CHT_TEMP_-ROD 669 TKROD CHTCONDROD 670 TCROD CHTHTCAPROD 671 CHTSEO CHTSECTIONSOUTPUT 672 . . MCORES CHT_M_CORESECT 673 . . HCORE CHTHCORESECT 674 CTHHOP CHTUSE_-NEWENTMALPY_.OPTION 675 POW POWERCOMMON 676 KUSER POW_USER_COMMON 677 KUSERI POWUSERINP 678 . . POW01 UNUSED..VARPOW01 679 . KLUPOW POW..USERIFUPOW 680 . KWPOWZ POWUSER-POWZ 681 . KNPOWT POWUSER.NPOWT 682 KFPOWT POW_.USERPOWT 683 KTPOWT POW.USERTPOWT 684 KUSERS POWUSERSTATE 685 . . KFQC POWUSER.QC 686 . . KFQCD POW_USER_QCD 687 KKIN POW_KIN_COMMON 688 . KKINI POWKININP 689 . KALPHA POWKINALPHA 690 KDLAM POW_KINDLAM 691 . KBETA POW._KINBETA 692 . KPLAM POWKINPLAM 693 KBBAR POWKINBBAR 694 KBBARR POW._KINBBARR 695 KDKBOZ POWKIN_DKCONZ 696 . KDKMTZ POW_.KIN._DKCTMZ 697 KDKMDZ POWKINDKDENZ 698 KDKFTZ POW_.KIN._DKTMPZ 699 . KDKINZ POWKINDKINSZ 700 . . KLMOD POW_KINMODDK 701 . KNBO POWKINNDKCON 702 KNMT POWKIN._NDKCTM 703 KNMD POW_KINNDKDEN 704 KNFT POW.,KINNDKTMP 705 . KNQDK POWKIN._NQDK 706 KSIGD2 POWKINLSIGD2 707 KSTARL POWKINSTARL 708 KTSS POW_KINTSS 709 KDKBO POW_KIN_.DKCON 710 KTBO POW(_KIN_.TDKCON 711 . KDKMT POW_KINDKCTM 712 . . KTMT POWV_KINTDKCTM 713 KDKMD POWKINDKDEN 714 . KTMD POWKINTDKDEN 715 . . KDKFT POW_KIN..DKTMP 716 KTFT POWKNINTDKTMP 717 KQDK POW_.KIN._QDK 718 KTQDK POWKINý_TQDK 719 . KTFUEL POW_KINT 720 KDCORE POW_KIN_DENCOR 721 . . KDKIN POW_KINDKINS 722 . . KTDKIN POW_KINTDKINS 723 . KNDKIN POW_.KINNDKINS 724 . . KTUPOW POW_IFUPOWTIM 725 . KDKCT POWKIN_.CUTBACK 726 KTCT POW_KINTCUTBACK 727 KNCT POW_KIN.NCUTBACK 728 KDSRC POW_KINSOURCE 729 KDKSUB POW_KINDK3_INIT 730 KKINO POW_KINOUT 731 . KDKTOT POWKINDKT 732 . KDKUSR POWKIN_.DK 733 KDKBOR POW_.KINDKBOR 734 . . KDKMOD POW_.KINDKMOD 735 KDKDOP POWKINDKDOP 736 . KDKTMD POW_KINDKTMD 737 KDKROD POW_KIINDKROD 738 KDKSCR POW._KINDKSCRAM 739 KDKCUT POW_KINDKCUT

Dimen____ aion.

RE 21 RE 600 RE 10,20 RE 10,20 RE 10,20 RE 41 RE 20 RE 20 RE RE 1700 RE 80 RE 60 RE 12 LO RE IN RE 20 RE 20 RE 10 RE RE RE 630 RE 580 RE 11 RE 11 RE 6 RE 6 RE RE RE RE RE RE RE LO IN IN IN IN IN RE RE RE RE 30 RE 30 RE 30 RE 30 RE 30 RE 30 RE 30 RE 30 RE 30 RE 30 RE RE RE 100 RE 100 IN RE RE 10 RE 10 IN RE RE RE 10 RE RE RE RE RE RE RE RE RE

Definition

Coolant temperature at bottom of section Radial rod model variables Temperature. distribution in fuel rod Fuel rod thermal conductivity Fuel rod heat capacity CHT Axially Sections Mass and Enthalpy Mass in core sections: Steam+Liquid Average enthalpy in core sections 1.0 => Use new(Ver 02250) CHT Enth Calc Segment for core power variables Variables for user control of power User control input variables Unused Variable User option for using power table Initial steady-state power No. of pairs in power vs time table Power values for power vs time table Time values for power vs time table User power state variables Final kinetics fission power fraction Final decay power Power kinetics variables Kinetics input variables Fission products disintegration energies Decay constants for fission products Delayed neutron fractions Decay constants for delayed neutrons Total delayed neutrons fraction Delayed neutron effectiveness Reference boric acid reactivity Reference moderator temp reactivity Reference moderator density reactivity Reference Doppler reactivity Reference ctrl rod insertion reactivity Option: mod bor acid & temp reactivities No. pairs, react vs bor acid conc table No. pairs, react vs moder temp table No pairs, react vs moder density table No. pairs, Dopplr reac vs fueltemp table No pairs, reactivity vs time table Total fission (1.0 - sum POWKINALPHA) Prompt neutron lifetime Maximum kinetics time step Boric acid reacts, for bar vs conc table Concentration for bar vs conc table Mod temp react, for mtr vs temp table Temperature for mtr vs temp table Mod dens react. for mdr vs density table Mod dens. for mdr vs density table React. for dopplr react vs fuel temp tbl Fuel temp for Dop react vs fuel temp tbl Reactivity for react vs time table Time for react vs time table Average core fuel temperature Core average moderator density Reactivity for react vs CEA pos table Pos (steps) for react vs CEA pos table No. pairs in worth-vs position table Time elapsed since switch to user-power Reactivity for RPC react insertion table Times for RPC reactivity insertion table No. points in RPC react insertion table Kinetics source term - fraction of FP Initial subcriticality Kinetics output variables Total reactivity User-specified reactiv. (e.g. stuck rod) Boric acid reactivity Core moderator density reactivity Fuel temp Doppler reactivity Moderator temperature reactivity Control rods reactivity Scram rods reactivity Reactor power cutback reactivity

Units

Degree F Partition Degree F Btu/sec-ft-degF Btu/ft^3-degF Partition Lbm Btu/lbn Dimensionless Segment Partition Partition Dimensionless True False Megawatts Counts Fraction Seconds Partition Fraction Fraction Partition Partition Fraction 1/seconds Fraction 1/seconds Fraction Fraction Reactivity Reactivity Reactivity Reactivity Reactivity True False Counts Counts Counts Counts Counts Fraction Seconds Seconds Reactivity Parts/million Reactivity Degree F Reactivity Lbm/ft^3 Reactivity Degree F Reactivity Seconds Degree F Lbm/ft^3 Reactivity Counts Counts Seconds Reactivity Seconds Counts Fraction Reactivity Partition Reactivity Reactivity Reactivity Reactivity Reactivity Reactivity Reactivity Reactivity Reactivity


I

G-201


Index Variabl e Name: No. Short Long

740 . ..KDKHER POWKINLDKHERMC 741 . KKINS POWKINSTATE 742 . KCHI2 POWKIN_CHI2 743 . . KEX2 POWKINEX2 744 . . KQD2 POWKIN_QD2 745 . . KQF2 POW_KIN_QF2 746 . KEN2 POW_KIN&EN2 747 . . KFTRIP POWCORE_TRIP_FRACTION 748 KDKHT POW_DKHTCOMMON 749 . KDKHTI POW_DKHT_INP 750 . . KTDHC POVWDKHTSTIMDHT 751 . KFDHC POW.DKHTANSDHC 752 . . KNDHC POVLDKHTNDHC 753 . . KFDHC0 POWDKHT_DHCBEG 754 . ..KFDHCM POW_DKHT_.DHCFCT 755 . KDKHTS POWDKIT_STATE 756 . KFLGDH POW_DKHTSIFDHC 757 . . KTIMDH POW.DKHTTIMDHC 758 . . KFQCDT POWJUSER_QCDLOOKUP 759 . KZRH2 POWVZRH20COMMON 760 . . KZRH21 POW-ZRH20-INP 761 . . ..KNYZIR POWZRH20NYZIR 762 . . .. KFZBJ POW_ZRH2O FZBJ 763 . . .. KZRH2S POW_ZRH20_STATE 764 ....... KH2M POW_ZRH2OJ2M 765 KINCON POW_INITIALCONDITIONS 766 . KFRAIN KFRAIN 767 KHER3D POW_KIN_HERMITE_INPUT 768 . KPRHER POWKIN_JERMITE.PARAM 769 . . . KTDHER POWSKIN_HERMTD 770 . . . KMLHER POW_KINHER'CHULT 771 . . . KTLTMN POW_KKINTEMP_TILT_MIN 772 . . . KPTWMN POWJKINPOWTOFLOWJMIN 773 . . . KWFRMN POWJKIN.FLOWFRACMIN 774 . . . KTLTMX POW_KIN_TEMP_TILTAX 775 . . KPTWIMX POWKIN_POWTOFLOWVMAX 776 . . KPHER POWKINJHERM_POWREF 777 . . KWHER POWJKINJIERMFLOWREF 778 . . . KNWFR POW_KIN_HERMCN_FLOWFR 779 . . . KWFHET POW_KINCOREWFRACTAB 780 . KRHER POWVKIN.CHEIM_CREDITTAB 781 KMHER POW_KIN_MIXINGINPUT 782 KCONSC POW.KIJNIIX_CON_COLD 783 KCONSH POW_KIN_MIXCON_HOT 784 KWEDGE POWKINEDGEJWEIGHT 785 KFDH POWJKINDHLFACTOR 786 KOPFB POWKINFEEDBACK.OPTIONS 787 KOPROD POWJKINSCRAM_RODOPTION 788 KOPREG POWJCINREGRODOPTION 789 KOPCUT POWKIN_CUT_RODOPTION 790 KOPDOP POW_KIN_DOPPLER_FB_OPTION 791 KOPBOR POWKINBORONFBOPTION 792 KOPMOD POWKINMODTEMPFBOPTION 793 KOPDEN POWSKINJMODDENSITYSFBSOPTION 794 KFLDEN POWJIN_MODDENSITYS_OPTION 795 KOPHER POWKINJHERMCREDIT_OPTION796 797 798 799 Soo 801 802 803 804 805 806 807 808 809 810 811 812 813

CORE3D POWIEXCORESOUT XDISP POWEXCOREDISP

XPOWRD EXCOREPOWERD XPOWER EXCOREPOWER XOFFST EXCOREOFFSET

XPWRAV EXCOREPOWERAV XOFFAV EXCORE-OFFSETAV XTCONS EXCORE-TAU

KXDISP POW_.EXCOREDATA KXPOWD POWEXCOREPOWERD KXPOWR POWEXCORE-POWER KXOFFS POWLEXCOREOFFSET

KXPWAV POWSEXCOREPOWERAV KXOFFA POWEXCOREOFFSET.AV KXTAU POW.EXCORE.TAU

KXCALB POW-EXCORESCALIB * . KXTUNE POWEXCORETUNE * . KXGAIN POWEXCOREGAIN

DimensionsRM

RE RE RE RE RE RE RE RE RE RE RE RE IN RE RE RE LO RE RE RE RE LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN RE RE RE RE RE RE RE RE LO LO LO LO LO LO LO LO LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

Definition

Hermite 3-D credit reactivity 25 Kinetics state variables 11 Norm concentration for fission products 6 Norm concentration for delayed neutrons

Current kinetics decay heat fraction Current prompt power fraction Temporary prompt power fraction Core power fraction at time of trip

100 Partition for decay heat variables 85 Partition for decay heat inputs 40 Time for ans decay heat vs time table 40 Decay heat frac for decay ht vs time tbl

No. of pairs in decay heat vs time table Power fraction for switch to decay heat Multiplier on tabular decay heat

5 Partition for decay heat output Signal: switched to decay heat Time of switch to decay heat Decay power from table

8 Zirconium oxidation variables 5 Zr-H20 input variables

Option: calculate zirc-oxidation Multiplier on Baker-Just generated heat

1 Zr-H20 state variables Hydrogen release rate due to Zr-H20

20 Power initial conditions New initial core power fraction

380 Hermite-torq 3D fb reactivity input 30 Hermite-torq 3D fb reactivity param

Time delay for Hermite 3D feedback Fraction of Hermite 3D feedback taken Minimum temperature tilt Minimum power to flow ratio (3D fb) Minimum flow fraction (3D feedback) Maximum temperature tilt (3D feedback) Maximum power to flow ratio (3D fb) Power for normalization (3D feedback) Flow for normalization (3D feedback) Number of flow fractions (3D feedback)

8 Core frac flow for Hermite 3D feedback 350 Hermite react table trivariant (3D fb) 10 Hermite-torg 3D fb mixing input 4 Cold side mixing weight factors (3D fb) 4 Hot side mixing weight factors (3D fb)

Edge temperature geom weight (3D fb) Core enthalpy rise fraction (3D fb)

15 Core reactivity feedback options Scram control rod reactivity option Regulating rod reactivity option Cutback control rod reactivity option Doppler reactivity option Moderator boric acid reactivity option Moderator temp reactivity option Moderator density reactivity option Option flag - cold edge mod density fb Hermite 3D fb reactivity - option flag

74 Variables for excore detectors 25 Excore readings - used for display only 8 Tot excore power readings (display) 4 Tot excore power readings (display) 4 Excore axial offsets (display)

Average excore power (display) Average excore axial offset (display) Time const for excore response (display)

25 Excore readings. used by controls & RPS 8 Total excore power readings 4 Total excore power readings 4 Excore axial offsets

Average excore power Average excore axial offset Time const for excore response

10 Calibration constants for excores Calibration tuning constant for excores Decalibration gain for excores


Units

Reactivity Partition Fraction Fraction Fraction Fraction Fraction Fraction Partition Partition Seconds Fraction Counts Fraction Dimensionless Partition True False Seconds Fraction Partition Partition True False Dimensionless Partition Lbm/sec Partition Fraction Partition Partition Seconds Fraction Degree F Dimensionless Fraction Degree F Dimensionless Megawatts Lbm/sec Counts Fraction Partition Partition Fraction Fraction Fraction Fraction Partition Active Inactive Active Inactive Active Inactive Active Inactive Active Inactive Active Inactive Active Inactive True False Active Inactive Partition Partition Fraction Fraction Dimensionless Fraction Dimensionless Seconds Partition Fraction Fraction Dimensionless Fraction Dimensionless Seconds Partition Dimensionless Lbm/ft^3

G-202


Index V a r i a b I e N a m e: NO. Short Long

814 . KXSVR POWEXCORESVR 815 POWAX POWAXIALDATA 816 KFAXIL POWUSER_QAXL 817 KIZX POWZRH20_IZX 818 KPCZR POWZRH2O0PCZR 819 KZX POWZRH20_ZX 820 KQZRH2 POWZRH20QZRH20 821 KSHPIN KSHAPIN 822 ZSHPIN ZSHAPIN 823 SHPOPT AXPDINPUTOPT 824 NUMSHP AXPDNUMPOINTS 825 PRISHP AXPDPRINTNORMALIZATION 826 RCS RCSCOMMON 827 RMODEL MODEL-OFF 828 RmORCP MOD_OFFRCP 829 RMOOIL M0DOFF_RCPOIL 830 RMOCHT MODOFFCHT 831 RMORCS MODOFFRCS 832 RMOQT MODOFFQT 833 RMOPOW MODOFFPOWER 834 RINTER RCS_INTERNAL 835 . RNODEV RCSNODEVARIABLES 836 . RPNODE RCSNODEPRESSURES 837 . RPRESP PRESPRED 838 RPRESS PRESS 839 RENNOD RCSNODEENERGIES 840 . RENTOT ENGYTOT 841 . RENSTM ENGYSTM 842 . RMNODE RCS.NODE_MASSES 843 . RMTOT MASSTOT 844 .... RMLIQ MASSLIQ 845 .... RMSTM MASS-STM 846 .... RMBUB MASS-BUB 847 . . . RENODE RCS_NODEENTHALPIES 848 .... RETOT ENTH_TOT 849 . ... RELIQ ENTH_LIQ 850 .... RESTM ENTHSTM 851 . . . REMIX ENTHMIX 852 .... RELIQS ENTH_LIQ..SAT 853 .... RESRMS ENTHSTM_SAT 854 . . . RSNODE RCS_NODE_SPEC_VOLUME 855 .... RSTOT SVOL.TOT 856 .... RSLIQ SVOLLIQ 857 . . . RSSTM SVOLSTM 858 .... RSLIQS SVOL_LIQSAT 859 . RSSTMS SVOLSTMSAT 860 RTNODE RCSNODE.TEMPERATURE 861 .... TRTOT TEMPTOT 862 .... RTLIQ TEMPLIQ 863 .... RTSTM TEMPSTM 864 . . . RTSAT TEMPSAT 865 . ... RTWALL TEMP_WALL 866 .... RTSUBC SUBCLIQ 867 . . . RTCONT TEMP_.CONT 868 . . . RQNODE RCS_NODE_HEATRATES 869 .... RQWALL HEAT_WALL 870 . . RQCONT HEAT_CONT 871 . . . RQEXT HEAT_EXT 872 .... RQTOT HEATTOT 873 . ... RQSTM HEATSTM 874 .... RQLIQ HEATLIQ 875 . RQCOND HEATCOND 876 RLNODE RCS._NODELEVELS 877 .... RLMIX LEVL MIX 878 .... RLLIQ LEVLLIQ 879 . . . RXNODE RCS_NODESTEAMFRAC 880 . . . RXTOT QUALTOT 881 . RXMIX QUAL_MIX 882 . ... RVOIDF VOID_FRAC 883 . . . RDNODE RCSNODEDERIVATIVES 884 . . RDPDMT DPDMTOT 885 .... RDPDML DPDMLIQ 886 . RDPDMS DPDMSTM 887 . . . RDPDUT DPDU_TOT

Dimen

MM! sions

RE RE RE LO RE RE RE RE RE IN IN IN RE LO LO LO LO LO LO LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE


250 20 20 20 20 20 50 50

12000 10

8400 3100 100 50 50 100 50 50 200 50 50 50 50 300 50 50 50 50 50 50 250 50 50 50 50 50 350 50 50 50 50 50 50 50 350 50 50 50 50 50 50 50 100 50 50 150 50 50 50 650 50 50 50 50

G-203

Definition

Reference downccmer spec-vol for excores Power calculation - core axial variables Axial power shape Indicator: non-reacted clad is present Percent zirconium reacted Thickness of reacted cladding Zr-H20 heat generation flux Initial power shape (normalized to one) Fraction of core height for KSHAPIN AXPD Input option: 0=node avg l=end node Number of points in AXPD (SHPOPT=I only) 1=> Debug print initial AXPD normalize RCS global cormmon variables Turns off models Turns off RCP model Turns off RCPOIL model Turns off CHT model Turns off RCS model Turns off QT model Turns off POWER model RCS internal variables Node variables Node pressure arrays Predicted node pressures Node pressures Node energy arrays Node total energies Node steam energies Node mass arrays Node total masses Node liquid masses Node steam masses Mass of entrained bubbles Node enthalpy arrays Node average enthalpies Node liquid enthalpies Node steam enthalpies Node two-phase mixture enthalpies Node saturated liquid enthalpies Node saturated steam enthalpies Node specific volume arrays Node average specific volumes Node liquid specific volumes Node steam specific volumes Node saturated liquid specific volumes Node saturated steam specific volumes Node temperature arrays Node average temperatures Node liquid temperatures Node steam temperatures Node saturation temperatures Node wall temperatures Node liquid subcooling Node containment temperatures Node heat rate arrays Node wall to coolant heat rates Node wall to containment heat rates Node external heat rates Node total heat rates Node wall-to-steam heat rates Node wall-to-liquid heat rates Node condensation heat rates Node coolant level arrays Node two-phase mixture levels Subcooled (or collapsed) liquid level Node steam fraction arrays Node steam mass fractions (qualities) Two-phase mix mass fractions (qualities) Node void fractions Derivative arrays Pressure derivatives, on total mass Pressure derivatives, on liquid mass Pressure derivatives, on steam mass Pressure derivatives, on total energy

Units

Ft^3/ibm Partition Dimensionless True False Percent Feet Btu/sec-ft^2 Fraction Fraction Dimensionless Dimensionless Dimensionless Segment Partition True False True False True False True False True False True False Partition Partition Partition Psia Psia Partition Btu Btu Partition Lbm Lbm Lbm Lbm Partition Btu/lbm Btu/lbm Btu/ibm Btu/ibm Btu/lbm Btu/ibm Partition Ft^3/lbm Ft^3/lbm Ft^3/lbmn Ft^3/lbm Ft^3/lbm Partition Degree F Degree F Degree F Degree F Degree F Del-DegF Degree F Partition Btu/sec Btu/sec Btu/sec Btu/sec Btu/sec Btu/sec Btu/sec Partition Feet Feet Partition Fraction Fraction Fraction Partition Composite Units Composite Units Composite Units Composite Units

I


Index No.

888 889 890 891 892 893 894 895 896 897 898 899 900 901 . 902 903 904 905 906 907 908 909 910 911 912 913 914 915 916 917 918 919 920 921 922 923 924 925 926 927 928 929 930 931 932 933 934 935 936 937 938 939 940 941 942 943 944 945 946 947 948 949 950 951 952 953 954 955 956 957 958 959 960 961

Dimen

r sionsVariable Name: Short Long

. . RDPDUS DPDUSTM * . RDHDU DHDU • . RDHDM DHDM

. . RDVDPT DVDPTOT • . RDVDHT DVDH TOT

* . RDHFDP DHF.DP

• . RDHGDP DHG_.DP * . RDVHDP DVF._.DP . . RDVGDP DVGDP * RBNODE RCS-NODEBUBBLES • . RBRELE RELEBUB

• . RBDRFT DRFTBUB

* RCNODE RCSNODECONDENSATION - RCTOT CONDTOT

• . RCBOIL CONDBOIL * . RCSURF COND.SURF

* . RCINJ CONDINJ

* . RCBUB CONDBUB

* RNENOD RCSNODESTATES . . RNECAN NECANDIDATE • . RNESTA NON.EQSTATE • . RHETRO NHETERO

• VOLMIX VOLMIX RSECT RCSSECT-NODE_VARIABLES

RIBUBM RCSMBUBSS RIDBUB RCSRELEPRIME RIVTOP RCSVOIDTOP RIVTRN RCS_VOID_TRAN RIBCOR RCSTRANSCORR RIXMIX QUALJMIXSECT RIMBUB MASSB BUB_SECT RISLIP SLIP-SECT

RPATHV RCS_PATHVARIABLES RGPATH RCS_PATHFLOWRATES

. . . RPFLOW PFLOW . . . RGMOM RCS _P _FLOW _.MOM

. . . . RGNONM RCS_P._FLOW_NONM

S ..... RGEXT RCSPATHEXTFLOW S ...... RGRCP RCSRCPLEAK_FLOW S ...... RGCHGS RCS_CHGSFLOW S ...... RGLET RCSLDNSFLOW S ...... RGDRN RCS_RCW_FLOW S . . . . .. RGSDC RCS _SDC _FLOW S ...... RGSIS RCS_SIS_FLOW . . . . RGLEAK RCSPATHLEAKFLOW S ...... RGSGTR RCSSGTRFLOW S ...... RGSB RCSSBLOCAFLOW S ...... RGRODE RCSRODEJFLOW S ...... RGORNG RCSORINGFLOW S ...... RGLB RCS_.LBLOCA_FLOW S ..... RGINT RCSPATHINTFLOW S ...... RGSPRA RCSSPRAYFLOW S ...... RGBLED RCS_S PRAYBLEEDFLOW

S.. . ... RGPZRR RCS _PRZR _RELIEF _FLOW S ..... RGR RCSS_UHEAD._RELIEF_FLOW . . . PFLOWC PFLOWCRIT • . REPATH RCSPATKLENTHALPIES . . . RPENTH P_.ENTH S .... REMOM RCS_PENTH_MOM . . . RENONM RCS_P.ENTHNONM S..... REEXT RCS_PATHEXT_ENTH

S ...... RERCP RCSRCPLEAK_ENTH S ...... RECHGS RCSCHGSENTH S ...... RELET RCSLDNSENTH

S..... REDRN RCSRCWENTH S ...... RESDC RCSSDC_ENTH S ...... RESIS RCSSIS_.ENTH S..... RELEAK RCS_PATHLEAKENTH

S ...... RESGTR RCSSGTRENTH S ...... RESB RCSSBLOCAENTH S ...... RERODE RCSRODEJ..ENTH S ...... REORNG RCS_ORING_ENTH S. . . ... RELB RCS _LBLOCA _ENTH S ..... REINT RCS_PATHINT_ENTH

Definition

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN IN LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE


50 Pressure derivative on steam 50 Enthalpy derivatives, on internal energy 50 Enthalpy derivatives, on total mass so Pressure derivative on total spec volume 50 Enthalpy derivative on total spec volume 50 Pres. derivative of sat. liquid enthalpy 50 Pres. derivative of sat. steam enthalpy 50 Pres. deriv, of sat. liquid spec. volume 50 Pres. deriv, of sat. steam spec. volume 100 Node bubble release arrays 50 Node bubble release rates 50 Node bubble drift velocities 250 Steam to liquid condensation variables 50 Total steam condensation rate in node

50 Condensation rate due to vaporization 50 Liquid-steam surface condensation rate 50 Condensation rate due to incoming liquid 50 Condensation rate of entrained bubbles 150 Non-equilibrium and heterogeneity flags 50 Non-equilibrium state possible in node 50 Non-equilibrium state now in existence 50 Flag indicating node is heterogeneous 50 Volume of two-phase mixture in node 71 RCS sectionalized node variables

SS bubble mass sect. node Deriv. of bub. release rate SS surf, void fraction Trans. surf, void fraction Transient bub. rel. correction

1,22 Array of section two-phase mix qualities 1,22 Array of section bubble masses 1,22 Array of section slip ratios 2750 Path variables 250 Path flow rate arrays 150 Path mass flow rates 100 Momentum paths mass flow rate 50 Non momentum paths mass flow rate 25 External paths mass flow rate 4 RCP leak mass flow 4 Charging mass flow 4 RCS- letdown mass flow 1 RCS RCW drains flow 2 RCS shutdown cooling flow 8 RCS safety injection flow 17 Leak paths mass flow rate 8 RCS SG tube rupture flow 4 RCS small break LOCA flow

RCS rod ejection small break flow RCS O-ring seal flow RCS large break LOCA flow

8 RCS internal paths mass flow rate RCS przr spray flow

2 RCS przr spray bleed flow Przr relief valves flow Upper head relief valves flow

100 Path critical flow rates 400 Path flow enthalpies 150 Path average enthalpies 100 Momentum paths enthalpy 50 Non momentum paths enthalpy 25 External paths enth 4 RCP leak enth 4 Charging enth 4 RCS- letdown enth 1 RCS RCW drains enth 2 RCS shutdown cooling enth 8 RCS safety injection enth 17 Leak paths enth 8 RCS SG tube rupture enth 4 RCS small break LOCA enth

RCS rod ejection small break enth RCS o-ring seal enth RCS large break LOCA enth

8 RCS internal paths enth

Units

Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Composite Units Partition Lbm/sec Feet Partition Lbm/sec Llxr/sec Lbm/sec Lbm/sec Lbm/sec Partition Pointer Pointer True False Ft^3 Partition Lbm Composite Units Fraction Fraction Dimensionless Fraction Lbm Fraction Partition Partition Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Partition Btu/lbm Btu/lhbn Btu/lbm Btu/lbm Btu/lbm Btu/lbm Btu/Ibm Btu/ibm Btu/lbm Btu/lbm Btu/ibm Btu/ibm Btu/lbm Btu/lbm Btu/lbm Btu/lbm Btu/lbm

G-204


DinanT) sions

Index Va r i a b l e N a m e: No. Short Long

962 963 964 965 966 967 968 969 970 971 972 973 974 975 976 977 978 979 980 981 982 983 984 985 986 987 988 989 990 991 992 993 994 995 996 997 998 999

1000 1001 1002 1003 1004 1005 1006 1007 1008 1009 1010 1011 1012 1013 1014 1015 1016 1017 1018 1019 1020 1021 1022 1023 1024 1025 1026 1027 1028 1029 1030 1031 1032 1033 1034 1035

S....... RESPRA RCS.SPRAYENTH S....... REBLED RCS.SPRAYBLEEDENTH S....... REPZRR RCSPRZR.RELIEF-ENTH S...... REUHR RCSUHEADRELIEFENTH . . . . RPLIQ PENTHILIQ . . . . RPSTM P.ENTHSTM * . . RPSVOL P-SVOL . . . RXPATH RCSPATHQUALITIES - . . . RPQUAL PQUAL

.... . RXMOM RCSPQUAL__O0 S..... RXNMOM RCS_-PQUAL-_NONM S.. ... RXEXT RCS_.PATHEXTQUAL

S. RXRCP RCSRCPLEAKXQUAL S ....... RXCHGS RCSCHGSQUAL S.. . ... RXLET RCSLDNSQUAL S....... RXDRN RCSRCWQUAL S....... RXSDC RCSSDC-QUAL S.. . ... RXSIS RCSSIS.SQUAL

S.... RXLEAK RCSPATHLEAKQUAL S...... RXSGTR RCSSGTRQUAL

S....... RXSB RCS-SBLOCAQUAL S....... RXRODE RCS-RODEJ QUAL S... ... RXORNG RCSORINGO QUAL

S. . ... RXLB RCSLBLOCA&QUAL ..... . RXINT RCS-PATHINT-QUAL

S....... RXSPRA RCSSSPRAYQUAL S ...... RXBLED RCSSPRAYBLEEDQUAL S...... RXPZRR RCSPRZR.RELIEFQUAL S...... RXUHR RCSUHEADRELIEFQUAL

S. ... RPVOID P _VOID S.... PSTMUP PSTILUP S..... RFMOM RCS-PSTMUPJ4OM

S..... RFNONM RCSSPSTMUPNONM S...... RFEXT RCS_PATHEXTSTM_UP

S...... RFRCP RCS-RCPLEAKXSTM-UP S.. ... RFCHGS RCSCHGMSSTMUP

S... ... RFLET RCSLDNS-STMUP S....... RFDRN RCSORCW STMIUP S... ... RFSDC RCSSDCSTMUP

. RFSIS RCSSISSTM-UP RFLEAK RCS.PATHLEAKXSTMUP

S...... RFSGTR RCS 0SGTRSTMUP RFSB RCSSBLOCA-STMCUP .RFRODE RCSRODEJ.STMUP

.. RFORNG RCS-ORINGSTMUP S.. . .. RFLB RCSLBLOCA&STM_UP

.... . RFINT RCSPATHINT_.STMUP

S...... RFSPRA RCSSPRAYSTMUP ... . RFBLED RCSSPRAYBLEEDSTMWUP

S... ... RFPZRR RCSPRZRRELIEFSTMLUP S... ... RFUHR RCSUHEADRELIEFSTMJUP

-. . RSTDN P5ST0_DOWN . . . RDPPAT RCS-PATHPRESSDROPS . . . RDPMOM DPMOM S.... RDPFRC DPSFRIC S .... RDPELE DPELEV S. ... RDPLOS DPLOSS S.... RDPHED DPHEAD S.... RDPEXT DP EXT S.... RDPTOT DPTOT S .... RDPACT DPACTUAL

S.... RDOCHK DPCHECK . . . RPDER RCS-PATH-DERIVATIVES S. ... RESUBK ESUBK S. ... RFSUBK FSUBK . . . RPUPDN RCSPATHMUPDOWN S.... PATHUP PNODEUP S.... PATHDN PiNODEDOWN

. . . RELUP PELEVUP S.... RELDN PELEVDOWN

RCSSG RCS-STEAMGENERATOR . HEATSG HEAT.SG RCSRCP RCSPUMPS

. . . RRSPED SPEED-PUMP

Definition

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN IN RE RE RE RE RE RE

RCS przr spray enth 2 RCS przr spray bleed enth

Przr relief valves enth Upper head relief valves enth

100 Path liquid enthalpies 100 Path steam enthalpies 100 Path average specific volumes 500 Path flow qualities 150 Path average steam fractions (quality) 100 Momentum paths quality 50 Non momentum paths quality 25 External paths quality 4 RCP leak quality 4 charging quality 4 RCS- letdown quality 1 RCS RCW drains qual 2 RCS shutdown cooling qual 8 RCS safety injection qual 17 Leak paths quality 8 RCS SG tube rupture qual 4 RCS small break LOCA qual

RCS rod ejection small break qual RCS O-ring seal qual RCS large break LOCA qual

8 RCS internal paths quality RCS przr spray qual

2 RCS przr spray bleed qual Przr relief valves qual Upper head relief valves qual

100 Path average steam void fractions 150 Frac of fluid from upstream steam region 100 Steam frac from steam region (mom path 50 Steam frac from steam reg. (non mom 25 External paths stm quality 4 RCP leak stm quali 4 Charging stm quali 4 RCS- letdown stm quali 1 RCS RCW drains stm quali 2 RCS shutdown cooling stm quali 8 RCS safety injection stm quali 17 Leak paths stm quali 8 RCS SG tube rupture stm quali 4 RCS small break LOCA stm quali

RCS rod ejection small break stm quali RCS o-ring seal stm quali RCS large break LOCA stm quali

8 RCS internal paths stm quali RCS przr spray stm quali

2 RCS przr spray bleed stm quali Przr relief valves stm quali Upper head relief valves stm quali

100 Frac of fluid to downstream steam region 900 Path flow pressure drops 100 Momentum pressure drop 100 Friction pressure drop 100 Elevation pressure drop 100 Form loss pressure drop 100 Head pressure drop 100 Externally driven pressure drop 100 Total pressure drop 100 Actual pressure drop (adjacent nodes) 100 Pressure drop check (DP._ACTUAL-DP._TOTAL) 200 Path momentum terms 100 Path momentum time derivative 100 Derivative of esubk by flow rate 400 Path flow direction dependent arrays 100 Node currently upstream of path 100 Node currently downstream of path 100 Elevation of currently upstream end 100 Elevation of currently downstream end 16 Steam generator variables 8 Steam generator heat transfer rates 20 Main coolant pump variables 4 Main coolant pump speeds

WCAP- 15996-NP, Revision 0

Units

Btu/lhm Btu/lbm Btu/lbm, Btu/lbm Btu/lbm Btu/lbm Ft^3lbn Partition Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Partition Psid Psid Psid Psid Psid Psid Psid Psid Psid Partition Composite Units Composite Units Partition Pointer Pointer Feet Feet Partition Btu/sec Partition Shaft RPM

G-205


1036 1037 1038 1039 1040 1041 1042 1043 1044 1045 1046 1047 1048 1049 1050 1051 1052 1053 1054 1055 1056 1057 1058 1059 1060 1061 1062 1063 1064 1065 1066 1067 1068 1069 1070 1071 1072 1073 1074 1075 1076 1077 1078 1079 1080 1081 1082 1083 1084 1085 1086 1087 1088 1089 1090 1091 1092 1093 1094 1095 1096 1097 1098 1099 1100 1101 1102 1103 1104 1105 1106 1107 1108 1109

index V a r i a b 1 N a m e: No. Short Long

. RRHEAT HEAT-PUMP * RRTORQ TORQPUMP * RRHEAD HEADPUMP * RRDP DPPUMP RCSCOR RCSCORE

RKQ HEAT-CORE RKGIN FLOW-COREIN RKBORN BORON-CORE RILLIQ LEVLLIQ.VESSEL RILMIX LEVLMIXVESSEL RKLMIX LEVLJMIXCORE RKSANN SVOL-DOWNCOMER RKBOUY BOUYANCY-CORE RKDPUH DPLOSSUPLEN RKQCEA RCSQ.CEA-CORE RKEDIS ENTH-QUADCORE RKETLT RCS-DELHHLTILT RKQUH RCSQUHEAD_CORE

RCSPZR RCSPRESSURI ZER RHVOLT VOLT-HEATER RHADMI ADMI-HEATER RHQELE HEATELEC RHENGY ENGY-HEATER RHTEMP TEMPHEATER RHQHTR HEATHEATER RHQPZR HEAT-PRZR RPDPLV LEVLPRZRDP RPTREF TEMFPPRZR REF RPTSRG TEMPPRZRSURGE RPTRTD TEMPPRZRRTD RWGPAT PFLOW-SPRAY RWEPAT PENTHSPRAY RWBPAT PBORON_SPRAY RWGAUX PFLOWAUXS PRAY RWEAUX P_ENTHAUXS PRAY RWBAUX P_BORON_AUX_SPRAY RWGBLD P_FLOW_BLEED RVGREL P_FLOWRELIEF RVEREL PENTHRELIEF RVSREL P_SVOL_RELIEF RVVRLE VIBRVALVERELIEF RVTREL TEMPVALVERELIEF RPNCON P-NONCPRZR.CONT RPNOT PNONCPRZRQT RPGSQT PFLOWPRZRQT RPGQT2 RCSPFLOW.PRZRQT2 RPPLOC RCSPRZR.PRES RWEBLD PENTHBLEED RVPUP VLVPRZRPRESUP RVPDN VLVPRZRPRESDOWN

RCSUH RCSUPPER.HEAD * RUGQT P_FLOW_UHEADQT * RUEQT PENTH_UHEADQT * RUGCON PFLOWUHEADCONT * RUECON PENTH_UHEADCONT

RUETOP ENTH-UHEAFDTOP * RUSTOP SVOLUHEAD_TOP * RUMNON MASSNONUHEAD

RUVNON VOLUNON-UHEAD RUPNON DPNON_UHEAD RUNDIL NONCDILU-RATE RUNCON P-NONCUHEADCONT RUNOT PNONCUHEADQT RUPLOC RCS-UHEADPRES RCKMUL RCSCEAMULT RCLCEA RCSCEAAV

RCSQT RCSQUENCHTANK RQPRES PRESQT RQENTH ENTHQT RQENGY ENGYQT RQLEVL LEVL.QT RQMWAT MASSS_WATQT RQMGAS MASS_GAS_QT ROTEMP TEMP_QT

Dimen

RE 4ions

RE 4 RE 4 RE 4 RE 4 RE 80 RE RE RE RE RE RE

RE 2,10 RE RE RE RE 4 RE 4 RE RE 80 RE 6 RE 6 RE 6 RE 6 RE 6 RE 6 RE RE RE RE RE RE RE RE RE RE RE RE 4 RE RE RE RE 4 RE 3 RE RE RE RE RE RE 4 RE RE RE 25 RE RE RE RE RE RE RE RE RE RE RE RE RE RE 2 RE RE 20 RE RE RE RE RE RE RE


Definition

Main coolant pump heat rates Unused Variable Main coolant pump heads Main coolant pump pressure rises Reactor core variables Total core-to-coolant heat transfer rate Core inlet flow rate (totl minus bypass) Core average boron concentration Collapsed liquid level in vessel Two-phase mixture level in vessel Two-phase mixture level in core Downcomer sp. vols. at excore detectors Core coolant bouyancy ratio Pressure loss in vessel upper plennum Heat transfer rate CEA to core node Core inlet radial enthalpy distribution Hot leg inlet delta enthalpy tilt Heat transfer rate u-head to core node Pressurizer variables Pressurizer heater effective voltages Pressurizer heater admittances Przr. heater electrical heat rates Pressurizer heater stored heats Pressurizer heater temperature Pressurizer heater-to-coolant heat rates Total pressurizer heater heat rate Pressure drop for level instrument Pressurizer reference leg temperature Surge line temperature Pressurizer rtd temperature Pressuizer spray total flow rate Pressurizer spray enthalpy Pressurizer spray boron concentration Auxiliary spray flow rate Auxiliary spray flow enthalpy Auxiliary spray flow boron concentration Spray bleed flows from cold legs Total pressurizer relief flow rate Pressurizer relief flow enthalpy Pressurizer relief flow specific volume Array of relief valve vibration signals Array of relief valve exit temperatures Non-cond flow przr to cont Non-cond flow przr to quench tank Pressurizer surge to QT flow rate PORVs and safeties flow przr to Q.T. Pressurizer pressure (local variable) Spray bleed enthalpies from cold legs Upstream pressure at przr relief valves Downstream pressr at przr relief valves Reactor vessel upper head variables Upper head to quench tank flow rate Upper head to quench tank flow enthalpy Upper head to containment vent flow rate Upper head to containment vent enthalpy Enthalpy in top of upper head Specific volume at top of upper head Non-condensbl gas mass in upper head nu Non-condens gas volume in upper bead nu Upper head non-cond gas partial press Dilution of noncondensible u.h. bubble Non-cond flow from upper head to contmt Non-cond flow from upper head to quench Upper head pressure (local variable) CEA paths k factor multipliers CEA average position Quench tank variables Quench tank pressure Quench tank enthalpy Quench tank liquid energy Quench tank liquid level Mass of water in quench tank Mass of nitrogen in quench tank Quench tank temperature

Units

Btu/sec Dimensionless Feet Psid Partition Btu/sec Lbm/sec Parts/million Feet Feet Feet Ft^3/lbm Fraction Psid Btu/sec Btu/Ibm Btu/lbm Btu/sec Partition Volts Mho admittance Btu/sec Btu Degree F Btu/sec Btu/sec Feet Degree F Degree F Degree F Lbm/sec Btu/Ibm Parts/million Lbs/sec Btu/lbm Parts/million Lbm/sec Lbm/sec Btu/ibm Ft^3/llbs Volts Degree F Lbm/sec Lbm/sec Lbm/sec Lbm/sec Psia Btu/lbm Psia Psia Partition Lbm/sec Btu/lbm Lbs/sec Btu/i]bm Btu/lbm Ft^3/lbm Lbm Ft^3 Psia Lbm/sec Lbs/sec Lbms/ec Psia Dimensionless Feet Partition Psia Btu/Ibm Btu Feet Lbm Lbs Degree F

G-206


Index V a r i a b I e N a met No. Short Long

DimenTyM sion.

1110 1111 1112 1113 1114 1115 1116 1117 1118 1119 1120 1121 1122 1123 1124 1125 1126 1127 1128 1129 1130 1131 1132 1133 1134 1135 1136 1137 1138 1139 1140 1141 1142 1143 1144 1145 1146 1147 1148 1149 1150 1151 1152 1153 1154 1155 1156 1157 1158 1159 1160 1161 1162 1163 1164 1165 1166 1167 1168 1169 1170 1171 1172 1173 1174 1175 1176 1177 1178 1179 1180 1181 1182 1183

* RQTSUR TEMPQTSURGE . RQLRUP RUPTUREQT . RQSOLU CONCSOLU_QT • RQNCON PJNONCQTCONT

RCSGLO RCS-GLOBALAVERAGE RGPRES PRESGLOB RGMASS MASS-GLOB RGENTH ENTHGLOB RGENGY ENGYSGLOB RGSENG SENGSGLOB RGSVOL SVOL-GLOB RGQUAL QUAL-GLOB RGELQS ENTHLIQSAT._GLOB RGESTS ENTH_STMSATGLOB RGSLQS SVOLLIQ.SATGLOB RGSSTS SVOLSTM_SAT_GLOB RGTSAT TEMPSAT-GLOB RGDP DP_.GLOB

RCSSOL RCSSOLUTE • RPSOL RCS-PSOLU

RPBOR RCS_P..BORON • . . RPHYD RCSPSHYD * . . RPIOD RCS_P_IOD . . . RPPART RCSJPJPART * . . RPXEN RCS.PXEN

* RWAHYD RCSPJHYDAUXSPRAY . RWAIO RCS_P..IODAUXSPRAY

RWAPT RCSPPARTAUXSPRAY RWAXE RCS_P_XEN_AUX_SPRAY RNREL RCSRELEJNONC

• RNSOL RCSCONCSOLU * . . RNBOR RCSSCONC-BORON • . . RNHYD RCSCONCJHYD • . . RNIOD RCSSCONCJIOD • . . RNPART RCSCONCPART

. * RNXEN RCSCONCXEN * RSREL RCSSRELE_.SOLU . RKSREL RCSRELESOLUCORE . . RKBREL CORE_BORON_.REL

• . . RKHREL COREHYDREL . . . RKIREL COREIOD-REL . . . RKPREL COREPART.REL . . . RKXREL COREJXEN-REL * . RDSPAR RCSDOSEVARIABLES . . . RDMIIO RCSDOSEINITIOD . . . RDMFSH RCSJDOSEFLASH . . . RDMBF RCSDOSEBF . . . RDMCF RCSSDOSESCF • *. RDMXQ2 RCSDOSE_XOQ2 • . * RDMXQ8 RCSDOSE_XOQ8 • * RDMCLR RCSDOSECONT LEAK * . . RDMCDF RCSDOSECONDDF • . . RDMTCU RCSDOSETOT_CURIE • . . RDM2HR RCSDOSE_2HR

* RDM8HR RCSDOSE.8HR RPASTV RCSJPASTVALUES

RLENST ENGY.STM&LAST RLENTO ENGYTOTLAST RLMLIQ MASSLIQLAST RLMSTM MASS_STILAST RLMBUB MASSBUB-LAST RLMTOT MASSTOTLAST RLPRES PRESLAST RLELIQ ENTHfLIQLAST RLESTM ENTHSTMLAST RLELQS ENTH_LIQSATLAST RLFLOW PFLOWLAST RLKFLS RCSCOREFLASH_LAST

RCSSTA RCSSTATUS • RLIERR FATAL.INPUT_.ERROR

RLOERR FATAL-OUTPUTERROR * RLHOMO RCSHOMOGENEOUS * RLEQUI RCS-EQUILIBRIUM . RMBUBP MASSBUBPRED

RE 5 RE RE 18 RE RE RE RE RE RE RE RE RE RE RE RE RE RE 1030 RE 50,5 RE 50 RE 50 RE 50 RE 50 RE 50 RE RE RE RE RE RE 50,5 RE 50 RE 50 RE 50 RE 50 RE 50 RE 50.5 RE 5 RE RE RE RE RE RE 20 RE RE RE RE RE RE RE RE RE RE RE RE 651 RE 50 RE 50 RE 50 RE 50 RE 50 RE 50 RE 50 RE 50 RE 50 RE 50 RE 150 RE RE 156 LO LO LO LO RE 50

Definition

Quench tank in-surge temperature Rupture disk ruptured when *TRUE. Solute concs in Q.T.: B,H,ICsXe Quench tank to cont vent non-cond flow Global variables (excludes pressurizer) Global pressure Global mass (excludes pressurizer) Global specific enthalpy Global internal energy Global specific internal energy Global specific volume Global quality Global saturated liquid enthalpy Global saturated steam enthalpy Global saturated liquid spec volume Global saturated steam spec volume Global saturation temperature Change in global press. during last step Coolant solute variables Non mom. paths solute concentrations Non mom. paths boron concentration Non mom paths hydrogen Non mom. paths iodine Non mom. paths particulates Non mom. paths xenon Aux spray hydrogen concentr. Aux spray iodine concentr. Aux spray particulate concentr. Aux spray xenon concentr. Hydrogen release rate to u-head Node solution concentrations Node boron concentrations Node hydrogen concentrations Node iodine concentrations Node particulates concentrations Node xenon concentrations Node solute accumulation rates Core solute releases. 1-5:BoHylo,Ce,Xe Core boron release (=0.0: unused) Core hydrogen release Core iodine release Core particulate (cesium) release Core xenon release Dose Model variables Dose Model Initial RCS Iodine Conc. Dose model flashing factor flag Dose model breathing factor Dose model conversion factor Dose model 2Hr site dispersion factor Dose model 8hr site dispersion factor Dose Model Containment Leak Rate Dose Model Turb & cond Decon Factor Dose Model Total Curies Iodine Released Dose Model Total 2 Hour DOSE Accum. Dose Model Total 8 Hour DOSE Accum Retained variables from last execution Node steam energy at last time step Node total energy at last time step Node mass of liquid at last time step Node mass of steam at last time step Node mass of bubbles at last time step Node total mass at last time step Node pressures from last execution Node liquid enthalpies from last exec Node steam enthalpies from last exec Saturated liquid enthalpy, last step Path flow rates at last time step Core flashing rate at last execution Variables associated with RCS abort RCS model abort on input data error(s) RCS model abort on calculation error(s) Forces all nodes to be homogeneous Deactivates RCS non-equilibrium calc Predicted bubble masses for path props.


Units

Degree F True False Composite Units Lbm/sec Partition Psia Lbm Btu/lbm Btu Btu/lbm Ft^3/lbm Fraction Btu/lbm Btu/Ibm Ft^3/lbm Ft^3/lbm Degree F Psid Partition Composite Units Parts/million Lbm/Ibm Microcurie/lbm Microcurie/Ibm Microcurae/ibm Lbm/Ibm Microcurie/Ibm Microcurie/lbm Microcurie/lbm Lbm//sec Composite Units Parts/million Lbm/ lbm Microcurie/lbm Microcurie/Ibm Microcurie/lbm Composite Units Composite Units Composite Units Lbm/sec Microcurie/sec Microcurie/sec Microcurie/sec Partition Microcurae/lbm Dimensionless FT^3/sec Rem/Curie sec/FT^3 sec/FT^3 Frac./day Dimensionless Curies REM REM Partition Btu Btu Lbm Lbm Lbm Lbm Psia Btu/lbm Btu/lbm Btu/ibm Lbm/sec Lbm/sec Partition True False True False True False True False Lbm

G-207


Index V a r i a b I e N a n ei NO. Short Long

LO IN IN RE RE RE RE RE RE RE RE LO LO LO RE RE RE RE RE RE

1184 1185 1186 1187 1188 1189 1190 1191 1192 1193 1194 1195 1196 1197 1198 1199 1200 1201 1202 1203 1204 1205 1206 1207 1208 1209 1210 1211 1212 1213 1214 1215 1216 1217 1218 1219 1220 1221 1222 1223 1224 1225 1226 1227 1228 1229 1230 1231 1232 1233 1234 1235 1236 1237 1238 1239 1240 1241 1242 1243 1244 1245 1246 1247 1248 1249 1250 1251 1252 1253 1254 1255 1256 1257

DisnM .ions

50 50

25 25 3 15 2 3 20

17 10 4 4

• RLLBMP RCSLOCA-MAPPING • RPITER RCSSEARCH-ITER * RPTYPE RCSSEARCHTYPE

. RKASUR CORE-SURF_.AREALAST RCSVLV RCSVALVES . RVAREA RCSVLV.AREA

. . . RUAVLV AREA.VALVE-UHEAD

. . . RPAVLV AREA.YALVEPRZR

. . . RWAVLV AREAVALVESPRAY

. . . RQAVLV AREAVALVE0QT RCSMAL RCSJMALFUNCTION * RLRODE FLAGRODEJ * RLLB FLAGLOCA * RLBLOW LOCA-BLOWDOWN * RALEAK PAREALEAK

RPVLV RCSPRZRFLOW.VALVES * RPGPOR RCS_P_FLOWPORV * RPGSAF RCSPFLOW_SAFETY * RPGCON PFLOWPRZRCONT * RPGQT1 RCSPFLOW_PRZRQT1 RCPCOM RCPCOMMON * RCPINT RCPINTERNAL

. . . RCPELE RCPELECTRIC . . . . RRVOLT RCPVOLT S . .. RRFREQ RCPFREQ . . . . RRADRE RCPADMI-RE . . . . RRADIM RCPADMIIM * . . . RRSLIP RCPSLIP . . . . RRPF RCPPF . . . RCPMEC RCP MECHANICAL . . . . RRTHYD RCPTORQHYD . . . . RRTELE RCPTORQ.ELEC

. . . . RRTFRI RCPTORQFRIC

. . . . RRQRCP RCPHEAT

. . . . RRVIBR RCPVIBR

. . . . RRSPMP RCPSPEEDPUMP

. . . . RRSMOT RCPSPEEDMOTOR

S .... RRAVIB RCPVIBRAMP . . . RRDSPD RCPSPEEDDERIV • . . RCPMAL RCP._ALFUNCTION

. . . . RRBREK RCPBREAK

. . . . RRHIVI RCPHIVIB

. . . . RRLOCK RCPLOCKED • . . RCPLEK RCPRCSLEAK . . . . RRLEAK RCPSEALSLEAK RCSOPT RCSOPTIMIZATION

RPNCAL RCSNSTEP-CALCULATIONS * RPITRP RCSICOUNT_MUKPRP * RPNTRP RCS_NUM_MUKPRP * RPVISC RCS_P_VISCOS RPCOND RCSPCONDUCT RPPRAN RCS-P-PRANDTL RPICRT RCS-ICOUNT-FLOWLIM-P RPNCRT RCSRNUMFLOWLIMP RMORA RCSMORE-VARIABLESA . RMORI RCSMORE_.ARIABLESI

• . . RPEMIN- RCSMIN-EXT-ENTH

. . RPEMAX RCS-MAXEXTENTH * . . RPQCMU RCSPRZR.CONT_HEATMULT . . . RTHSMU CHTH-SUPERJMULT

. . . RTFRAC CHTHEATFRAC • . . RLSPIK RCS-PSPIKEOUTPUT

. . RFLHET RCSFTIMEHEATER

. . . RHTIME RCSDELT-HEATER • . RTTMSC CHTTIME-SCALE • . . RTDEL CHTDELT • . . RTFDEL CHTFDELT • . RFLCHT CHTFTIME

. . . RTDELT CHTDELTAT

. . . RFLSPR RCSFTIMESPRAYS

. . . RPTFLS RCSPRZRFLASHTAU

. . . RUQCMU RCSUHEADCONT_HEAT_MULT

. . . RCRMOD RCSCRIT.MODEL

. . RMOR2 RCS.MOREVARIABLES-II

Definition

Enables LOCA super-node mapping each Number of iterations in pressure search Pressure search used Vessel flow area at two-phase boundary Variables associated with RCS valves RCS valve areas Array of upper head vent valve areas Array of presssurizer relief valve areas Array of presssurizer spray bleed valves Array of quench tank valve areas Malfunction flags and variables Rod ejection malfuntion in effect Large break LOCA in effect Blowdown part of LOCA in progress Leak flow path areas Pressurizer valves flow PORVs mass flow rate Przr safety valves mass flow rate Przr to containment vent flow rate Przr to quench tank vent flow rate Coolant pump model global common Pump model internal variables Coolant pump motor electrical variables Pump motor input voltages Pump motor electrical frequencies Unused Variable Unused Variable Coolant pump motor slip Unused Variable Coolant pump mechanical variables Coolant pump hydraulic torques Coolant pump electrical torques Coolant pump friction torques Coolant pump fluid heat rates Coolant pump vibrations Coolant pump impeller speed Coolant pump motor speed Pump vibration amplitude at rated speed Coolant pump speed derivatives Coolant pump malfunction variables Unused Variable Unused Variable Logical indicating pump shaft locked RCP seals leak partition RCP seals leakage rated cond. RCS optimization partition Partition vars updated every n steps Counter mu-k-Pr calculations Number steps for mu-k-Pr calc. Path liquid viscosity Path liquid conductivity Path liquid Prandtl number Counter for critical flow calculations Number steps for crit. flow calc. RCS_.more variables A RCS more variables partition I nu External paths min. enth. bound nu External paths max. enth. bound Mult. wall heat przr to cont. Supercrit. heat coeff. mult. Total core heat transfer to coolant nu Flag for press spike output message nu Heaters fast time control nu Heaters time step CHT time scale CHT standard time step nu CHT fast time delt CHT fast time flag CHT time step nu Sprays fast time flag Time constant for przr flashing Multiplr on uppr head heat loss to cont. Liq/2-phs choked flow model: 0=HEM, l=HF RCS more variables partition II

units

True False Counts Pointer Ft^2 Partition Ft^2 Ft^2 Ft^2 Ft^2 Ft 2 Partition True False True False True False Ft^2 Partition Lbm/sec Lbm/sec Lbm/sec Lbm/sec Partition Partition Partition Volts Hertz Dimensionless Dimensionless Fraction Dimensionless Partition Ft-lbf Ft-lbf Ft-lbf Btu/sec G's vibration Radians/second Radians/second G's vibration Composite Units Partition True False True False True False Partition Gal/min Partition Partition Counts Counts Lbm/ft-sec Btu/sec-ft-degF Dimensionless Counts Counts Partition Partition Btu/Ibm Btu/Ibm Dimensionless Dimensionless Fraction True False True False Seconds Dimensionless Seconds Seconds True False Seconds True False Fraction Dimensionless Pointer Partition


RE 100 RE 88 RE 28 RE 4 RE 4 RE 4 RE 4 RE 4 RE 4 RE 40 RE 4 RE 4 RE 4 RE 4 RE 4 RE 4 RE 4 RE 4 RE 4 RE 12 LO 4 LO 4 LO 4 RE 4 RE 4 RE 820 RE 160 IN IN RE 100 RE 100 RE 100 IN IN RE 153 RE 20 RE RE RE RE RE LO LO RE RE RE RE LO RE LO RE RE IN RE 28

G-208


Index Variable Name: No. Short Long

DimenTM sions

1258 1259 1260 1261 1262 1263 1264 1265 1266 1267 1268 1269 1270 1271 1272 1273 1274 1275 1276 1277 1278 1279 1280 1281 1282 1283 1284 1285 1286 1287 1288 1289 1290 1291 1292 1293 1294 1295 1296 1297 1298 1299 1300 1301 1302 1303 1304 1305 1306 1307 1308 1309 1310 1311 1312 1313 1314 13151316 . . . REINIT RCSREINITIALIZE 1317 . . . . RPPINT RCSINIT_P 1318 . . . . RPLINT RCS_INIT._LEVEL_PRZR 1319 . . . . RPLAIR RCSINITAIR-PRZR 1320 . . . RPGVCN RCSWPRZRCONT 1321 . . . . RPGVQT RCSWfPRZR.QT 1322 . . . . RPXREL RCSPRZRQUALRELIEF 1323 * . . . RPTINT RCSINITT_PRZR 1324 . . . . RLTINT RCSINITT-LOOP 1325 .*. . . RSDCGF RCS_.DRAINSSDC 1326 . . . . RSDCGM RCS_MAX&DRAINSDC 1327 . . . RPFAIR RCS-PRZRJFRAC-AIR 1328 . . . . RKHSTM RCSPRZR_KH_STM 1329 . . . . RKPSTM RCSJPRZRIKPSTM 1330 . . . RM504 RCSMORE-VARIABLES_504_SR 1331 . . .*. RRFCAV RCPCAVIT_.SGDPFRAC

Definition

* RWEFF RCSSPRAYEFF RWEFFM RCSSPRAYEFFSMULT

* RWLEFF RCSJLEFFSPR * RTTSRG RCS-TSURGETAU • RELVLB RCS-MAL038 - REDTLB RCSDTFOPENLB • REFLB RCSFRACSIT-12B • REGLB RCSwj.SITCONT - REELB RCSHSITCONT - RTTMAX CHT.TERMMAX * RTESRG RCSJHLSURGESTAU * RFLSDC RCSJFTIMESDC - RCHGMX RCSJMAXMCHGS - RSITMX RCSJMAX.SIT * RLETMX RCSJMAXJLDNS • RDRNMX RCSMAX_WDRAIN - RSDCMX RCSJMAX.WSDC * REXBMX RCSJMAX.BC.EXT • RFLBUB RCSSFTIMEBUB - RWDELH RCSSPRAYDELH_DEG • RWEFFi RCSSPRAY _EFF1

• RWLPRS RCSSPRAYSPRESDEG • RWEFF2 RCSSPRAYEFF2 • RPLLOP RCS_PRZR_LOWPCONDLOG SRNEXM RCSQUALJMIN_NE * RPLCOF RCS_PRZRLCOND._OFF * RWPDEG RCSSPRAY-PDEGTERM

RMOR3 RCS.MORESVARIABLESIII * RPCORS RCS_HIGHP_COARSENODES * RSDPMU RCSSGDP_MULT * RPHWMU RCS-PRZR_HWALLFMULT * RPCWAL RCSPRZRCONDWALL

RMOR3A RCSMOREVARIABLESIIIA * RPHLMU RCSPRZRJHLIQJMULT * RFLPZR RCSSFTIME-PRZR * RPTAUR RCSSPRZRSTREFSTAU . RKHRMX RCSSCOREJHYDJREL_MAX

RMOR3B RCS.MORE-VARIABLESIIIB - RHVBSP RCSVOLTHTRBUS . RPLREF RCS.PRZRLLEVEL

RMOR4 RCSMORE3VARIABLESIV * RPDTBL RCS_PRZRDTBOIL * RPDTSB RCSPRZR.DTSUBC

RRADMU RCP_.ADMIMULT * RRDSLO RCPDELSPEEDLOCKED • RRCFRC RCP_FRIC_COEFF * RPPMOD RCSP_ELEV_MOD_SURGE * RDHFMN RCSDHF_MIN

RPDPMD RCSDPELEVSURGE * RITDPL RCSSITER&DPL * RELTST RCSSDCSITCONSISTTEST RMOR5 RCSJMOREVARIABLESV • RDWSDC RCSDW_SDC

RDWSTP RCSDWSTPSDC * RRSTAR RCPf_RCPSTART * RPMSTM RCSPRZR.MASSSTM * RPMAIR RCSPRZRMASSAIR RMOR6 RCSMOREVARIABLESVI

RE Spray efficiency RE Spray efficiency multiplier RE 2 Levels for spray effic. calc. RE Time constant surge temp. RE Local variable malf. 38 (LBLOCA) RE Delta t for full open of LBLOCA RE Fraction SIT CLl2b to RCS (LB only) RE CL 12b SIT flow to containm (LB only) RE CLI2b SIT enthalpy to contain (LB onl) RE Max. term for transition boiling RE Time constant surge line enth. LO Flag shutd. cool fast time contr. RE RCS bound on charging flow RE RCS bound on SIT flow RE RCS bound on letdown flow RE RCS bound on drain flows RE RCS bound on SDC flow RE RCS bound on ext. boron conc. LO nu Flag fast time bub. rel. RE Del enthalpy for spray degrad. RE Spray eff. term (flash red.) LO Sprays press dep. degrad RE Sprays press. dep eff. frac LO Przr low press. cond. logic RE Min quality for non eq. calc. RE Level cut-off przr. surf cond. RE Spray degrad. press. term RE 6 RCS more variables III post 406A. RE High press switch to coarse nodes(atws RE RCS SO del press mult.(coarse nodes) RE Mult for przr cond on wall hcoff RE Przr condensation on wall RE 5 RCS more variables IIIA RE Przr wall htcof to liq. mult. LO Przr fast time flag (condens.) RE 2 Przr ref. leg time constants RE Maximum core hyd. rel (single ph.) RE 4 RCS more variables IIIA RE 2 Voltage przr prop heater buses RE RCS przr level (inch from ref.leg bot. RE 10 RCS more variables IV RE Przr delt temp for boiling RE Przr. delt temp for flash. RE Unused Variable RE RCP locked rotor del-speed (rad/sec) RE RCP windage and fract. coeff. RE nu Press. for surge lin mod elev test. RE Subcooling del. enthalpy (low press.) RE nu Surge line modified dp RE Dp for converg. low press.(equil.) LO Flag to test SDC-SIT consist RE 8 RCS more variables V RE SDC- SIT delta flow RE Del flow / step SDC-SIT test RE 4 Unused Variable RE Przr steam mass RE Przr air mass RE 14 RCS more variables VI LO Control variable for reinitialization RE Przr pressure (reinitialization) RE Przr level reinitialization LO Remnit. with air in przr control RE Mass flow przr to contain RE Mass flow przr to quench tank (valves) RE Przr relief quality RE Przr liquid temp (reinitializ.) RE Loop temperature (reinitializ.) RE Drains from SDC line (fast time only) RE SDC drain flow bound (fast t RE Air mass fraction in przr. RE K for p degrad. of hcof stm. RE P for p degrad. of hcof stm. RE 58 RCS more variables spin 413 to 504 SR RE Unused Variable


Units

Fraction Dimensionless Feet Dimensionless Percent Seconds Fraction Lbm/sec Btu/lbm Dimensionless Dimensionless True False Lbm/sec Lbs/sec Lbm/sec Lbs/sec Lbs/sec Parts/million True False Btu/lbm Fraction True False Fraction True False Fraction Feet Dimensionless Partition Psia Dimensionless Dimensionless Lbm/sec Partition Dimensionless True False Seconds Lbm/sec Partition Volts Inches Partition Del-DegF Del-DegF Dimensionless Radians/second Composite Units Psia Btu/lbm Psig Psig True False Partition Lhm/sec Lhb/sec Dimensionless Lbs Lbm Partition True False Psia Inches True False Lbs/sec Lhm/sec Fraction Degree F Degree F Lbs/sec Lbm/sec Fraction Dimensionless Psia Partition Dimensionless

G-209


Dimen

Tn sions

1332 1333 1334 1335 1336 1337 1338 1339 1340 1341 1342 1343 1344 1345 1346 1347 1348 1349 1350 1351 1352 1353 1354 1355 1356 1357 1358 1359 1360 1361 1362 1363 1364 1365 1366 1367 1368 1369 1370 1371 1372 1373 1374 1375 1376 1377 1378 1379 1380 1381 1382 1383 1384 1385 1386 1387 1388 1389 1390 1391 1392 1393 1394 1395 1396 1397 1398 1399 1400 1401 1402 1403 1404 1405

Definition

* . RPTSB RCSPRZR.DTSUB_.BOIL * . RRVOID RCSRCP.VOIDF * - RRDTTP RCPDT..LASTSTRIP * . RRSTOP RCPSTOPPED * . RRTRIP RCPTRIPPED * . RPCSUR RCSSPRZRSCOND.SURF * . RPLLAS RCS-PRZR._LEVLLAST * . RPTWAL RCSPRZRTWALL * . RPQCON RCS-PRZRSCONT * . RPQAXW RCS.PRZRQAXWALL * . RPDTSS RCSPRZR__DTSUBSS . . RUPORG RCSP-ORING * . RULORG - RCSORINGOFAIL * . RRADFC RCP_.ADMI-FLOWCORR • . RRAMPS RCPAMPS * * RRSVOL RCS-RCP.SVOL * . RRLCAV RCS.RCPSCAVITAT * . REGSIT RCSWLSIT * . REDGST RCSSDWSIT * . RTC12B RCS-TEMP-CL12B

. * RQPJ4 QT J4 _P * . RRLTHI RCPTBEARINGJ{IGH

RFAIL RCSJFAI LURESTATUS * RNEVER RCSJNEVERSTOP.AUTO * RSFAIL RCSSTEP.FAILURE * RSRECV RCSSTEP.RECOVERY

RTIMEC RCSTIMESCONTROL RTIMSC RCSTIMESCALE RDEL RCSDELT RFDELT RCSJFDELT RDELTA RCS-DELTAT RDELWL RCS-DELT-WALL RFLWAL RCSFTIMEWALL RFLCOL RCSFTIMEHEAT RFLNON RCSFTIMEPATHS RFQHT RCSJHEATJFASTT RFLCVC RCSSFTIMECVCS RFLSIT RCSJFTIMESIT RFDQHT RCSDHEATSFASTT RFDQMX RCSDHEATMAXFASTT RFSDQS RCSDHEATSTEPFASTT

RCSLB RCSLARGE.BREAK RLBEL PENTHILIQLB RLBES PENTHLSTMLB RLBVFR PVOID-LB RLBS PSVOLLB RLBALS RCSAREALBLAST RLBLDR RCS-LBSGDRAIN RLBDPL RCSDP.LEAKLASTLB RLBQMX RCSJHEATSGOJ(AXLB RLBLDP RCSSFLAGDPLEAKLB RLBDTS RCSDELTEMSG_.LB RSHAOV RCSJHAPRIM RSTPRE RCSTEMPSGPRE TSTLST RCS-TEMPSGLAST RLBCOS RCSJFLAG.COARSEJNODES RLBRCS RCSLB-LOCAFIRST RCSLBL RCS-RCSLBJFIRST

ROUTPT RCSMOD.OUTPUTS * ROPUMP RCSMODOUTPUTSINSTRUM • * RR1DP RCSL.PMPLDP * * RR2DP RCSLPMP2_DP

* . RR3DP RCSL.PMP3_DP * . RR4DP RCSLPMP4_DP * ROCORE RCSJMODOUTPUTSCORE * . RKTAV CHT.TCOOL-AV * . RKSAV CHTSVOLCOOLAV * . RRBORL RCS.BORON-CORE * ROCHT RCSJMODOUTPUTSSCHT * * RTPRES RCSSCHTSPRESS * * RTELIQ RCS-CHTENTHLIQ * . RTESTM RCSSCHTENTHSTM * . RTQUAL RCSSCHT.QUAL . . RTGIN RCS-CHT-FLOWIN

RE LO RE RE RE RE LO LO LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

4 4 4 4

Max SG heat rate (steam, large break) LB LOCA leak flag Delta temperature SG primary - tube SG overall heat trans. coeff (prim) SG predicted temperature Last step temp for SG heat transfer RCS coarse nodalization flag Flag first time coarse nodal (RCS) Flag first time coarse nodal (RCSLB)

60 RCS model global cormmon outputs 4 RCS model outputs for instruments

Main coolant pump 1A pressure rise Main coolant pump lB pressure rise Main coolant pump 2A pressure rise Main coolant pump 2B pressure rise

3 RCS outputs to 1-D core Core coolant average temperature Core coolant average spec vol. Core node boron concentration

53 RCS modified outputs to CHT RCS core pressure RCS core liquid enthalpy RCS core steam enthalpy RCS core quality RCS core inlet flow (total minus bypass)

Index V a r i a b l a N a m e No. Short Long


RE Przr del-temp for boiling RE 4 RCP void fraction RE 4 Delt since RCP trip (0 RCP running) LO 4 Unused Variable LO 4 Unused Variable RE Przr cond. on liq. surface RE Przr. level last step RE 2 Przr walls temp. l.liq, 2- stm RE 2 Przr walls heat to containment RE Przr walls axial heat transf. RE Przr. ss subcooling to start boil. RE Inner O-ring region pressure LO Vessel O-ring failure flag RE 4 Unused Variable RE 4 Unused Variable RE 4 RCS RCP specific volume LO 4 Unused Variable RE 4 Safety injection tank flow RE 4 SIT delta flow RE CL2b temperature RE Quench tank press down of LO 4 Unused Variable LO 3 RCS failure status partition LO RCS never stop (bomb) control option LO RCS step failure flag LO RCS step recovery flag RE 45 Time control partition RE Time scale for RCS RE Master delt for RCS RE Fast time delt for RCS RE RCS integration delta t RE Walls integration delta t LO Walls fast time control LO Heat to coolant fast time control LO Non mom. paths fast time control RE 30 Fast time heat transfer LO CVCS paths fast time control LO SIT-shutd-cool fast time control RE Net delta heat fast time RE Max. net delt heat fast time RE Max del heat per step fast time RE 30 RCS large break variables RE Large break leak liquid enthalpy RE Large break leak steam enthalpy RE Large break leak void fraction RE Large break leak specific volume RE Large break last step break area LO Large break SG drain flag RE Last step leak delta press (large brk)

Units

Del-DegF Fraction Seconds True False True False Lbmfsec Feet Degree F Btu/sec Btu/sec Del-DegF Psia True False Dimensionless Dimensionless Ft^3/brn True False Lbm/sec Lbm/sec Degree F Psia True False Partition True False True False True False Partition Dimensionless Seconds Seconds Seconds Seconds True False True False True False Btu/sec True False True False Btu/sec Btu/sec Btu/sec Partition Btu/lbm Btu/l ibm Fraction Ft^3/lbm Ft-2 True False Psig Btu/sec True False Del-DegF Btu/sec-degF Degree F Degree F True False True False True False Partition Partition Psid Psid Psid Psid Partition Degree F Ft^3/lbm Parts/million Partition Psia Btu/lbm Btu/lbrn Fraction Lbm/sec

G-210


Index Vari able Name: DimenNO.- Short Long Type gions Definition

1406 1407 1408 1409 1410 1411 1412 1413 1414 1415 1416 1417 1418 1419 1420 1421 1422 1423 1424 1425 1426 1427 1428 1429 1430 1431 1432 1433 1434 1435 1436 1437 1438 1439 1440 1441 1442 1443 1444 1445 1446 1447 1448 1449 1450 1451 1452 1453 1454 1455 1456 1457 1458 1459 1460 1461 1462 1463 1464 1465 1466 1467 1468 1469 1470 1471 1472 1473 1474 1475 1476 1477 1478 1479

S .... RTEIN RCS.CHTENTHIN S .... RTXIN RCSCHTQUALIN . . RTLMIX RCSCHTLEVMIX S .... RTLSAT RCS.CHTLEVSAT .... RTQWAL RCSCHTQWALL S .... RTTWAL RCS-CHTTWALL S .... RTMLIQ RCS-CHT._MASSLIQ S .... RTMBUB RCS-CHTMASSBUB

RINPUT RCSMODINPUTS . RINBOP RCS-MOD-INPUTSBOP

S. RCFLOW CHGS-RCSFLOW . . RCENTH CHGSRCSENTH . . RCBORN CHGS-RCSBORON S. . RCHYD CHGSRCSHYD . . RCIOD CHGSRCSIOD

RCPART CHGSRCSPART S. .RCXEN CHGS.RCSXEN . . . RGASPR CHGSASPRAYFLOW . . . RLETG LDNSRCSFLOW . RDRNG RCWRCSFLOW . . RSDCG SDCRCSFLOW . . RSISG SISRCS-FLOW . . RSISE SISRCS-ENTH S. .RSISB SISRCSBORON

. RSITG SITANKFLOW * RIVLVC RCS.MODINPUTSVLVCONTR

. RVPOS VLVRCSPOS S .. . RVFUHC VLVUHEADCONT

S.. . RVFU`HQ VLVUHEADQT . . . RVFPOR VLVPRZR PORV

S . .. RVFSAF VLVPRZR_.SAFETY . . . . RVFMOV VLVPRZR_MOV

. . . RVFPC VLVPRZR CONT S .... RVFPQT VLVPRZRQT S .... RVFSPR VLVPRZRMSPRAY

S.... RVFQTG VLVQT GWS S.. . RVFQTC VLVQTCONT S .... RVFQTN VLVQTNSUPPLY • . . RVFSIG VLV_RCSSIG S .... RVSSPR VLV-PRZRMSPRAYSIG S .... RVSPOR VLVPRZRPORVSIG

* RIVOLT RCSMODINPUTSVOLTCONTR RHFVLT PRSIHEATERVOLT-FRAC

. . RRFVLT RCPIVOLT-FRAC • RHVBUS RCSHEATERVOLTBUS

RRFFRQ RCPIFREQFRAC RIMAL RCS_MOD_INPUTSJMALFUNCTIONS

RMSB MALSB LOCA RMLB MAL-LBLOCA

S. RMSGTR MALSGTR DUM001 DUMOOl RMRODE MALRODEJECT RMVALV MALRCSVALVE •RMVUHC MAL VLVUHEADCONT • RMVUHQ MALVLV_UHEADQT

S .... RMVPOR MALVLVPRZRPORV S .... RMVSAF MALVLVPRZRSAFETY S .... RMVMOV MALVLVPRZRMOV S.... RMVPCR MALVLVPRZRCONT

S .... RMVPQT MALVLVPRZRQT S .... RMVSPR XALVLVPRZRMSPRAY

. RMVQTG MALVLVQTGWS • RMVQTC MAL_VLVQTCONT

. . . RMVQTN MALVLVQTNSUPPLY RMRSHB MALRCPSHAFTBREAK RMRLOC MALRCP_.LOCKED

. RMRVIB MALRCPHIVIB . RMROD MALROD_CORE RICONT RCSMODINPUTSCONT . RPCONT CONTPRES

* RIQT QT_.MODINPUTS S.. RQGDMW DMWQTFLOW . . . RQEDMW DMWQTENTH S.. RQGRCW RCWQTFLOW

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE LO LO LO IN RE RE RE RE RE RE

22 205 50 4

4 1 2 8 8 8 4 30 24

2 4 4 4

2 2

6 2 4 20 6 4 6 4 52 4

4 4

25

2 4 4 4

2 2

4 4 4

2

5

RCS core inlet enthalpy RCS core inlet quality RCS core mixture level RCS core saturation level RCS lower plenum wall heat RCS lower plenum wall temperature RCS lower plenum liquid mass RCS bubble mass in core sections RCS modified inputs RCS modified inputs bop systems Charging system flows (RCS connections Charging system enthalpy (RCS connect. Charging system boron conc.(RCS connec Charging system hydrog. conc.(RCS conn Charging system iodine conc (RCS conn Charging sys particulate conc (RCS conn. Charging system xenon conc.(RCS connec Charging aux. spray flow Letdown system flow (RCS connections) Drain flow to waste syst (RCS connect. Shutdown cooling out flow (RCS connec. SIS flows (RCS connections) SIS enthalpy (RCS connections) SIS boron concentration (RCS connectio Safety injection tank flow RCS mod inputs from valve controllers RCS valve positions (fraction) Upper head to contain valve pos. Upper head to quench tank valve pos. Przr PORV position Przr safety valves position Przr mov position(in series with PORVs Vent valve przr to containment Przr to quench tank vent vlvs(in serie Main spray control valves Quench tank to gws vent vlv. position Quench tank to contain. vent vlv pos. Nitrogen supply to QTank valve pos. RCS valve signals Przr main spray valve signal Przr pressure relief valve signal RCS mod inputs voltage controllers Przr heaters voltage (fraction) RCP voltage (fraction) Heater bus voltages RCP electric motor frequency (frac.) RCSmodified malfunctions Small break LOCA areas Large break LOCA area SG tube rupture leaks (numb of tubes) Dummy variable Rod ejection plus CEDM rupture (fract) RCS valves malfunction Upper head to contain valve pos. (malf) Upper head to quench tank valve pos (ma Przr PORV pos. (malf) Przr safety valves pos (malf) Przr mov pos (malf) Vent valve przr to containment (malf) Przr to quench tank vent vlvs(malf) Main spray control valves (malf) Q tank to gws vent vlv. pos. (malf) Q tank to contain, vent vlv pos. (malf) Nitrogen supply to QTank valve pos. (mal RCP shaft break malfunction RCP locked rotor malfunction Unused Variable Rod number to eject (+) or drop C-) RCS modified inputs from containment Containment pressure Quench tank modified inputs Demineralized water flow to quench tan Demineralized water enthalpy Mass flow QT to RCW


Unit.

Btu/lbm Fraction Feet Feet Btu/sec Degree F Lbm Lbm Partition Partition Lbm/sec Btu/Ibm Parts/million Lbm/I bm Microcurie/lbm Microcurie/lbm Microcurie/lbm Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Btu/ibm Parts/million Lbm/sec Partition Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Partition Fraction Fraction Partition Fraction Fraction Volts Fraction Partition Ft^2 Ft^2 Pointer Unused Fraction Partition Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction True False True False True False Pointer Partition Psia Partition Lbm/sec Btu/lbmn Lbm/sec

G-211


DimenTa aiona

Index V a r i a b I a N a m ei No. Short Long

1480 1481 1482 1483 1484 1485 1486 1487 1488 1489 1490 1491 1492 1493 1494 1495 1496 1497 1498 1499 1500 1501 1502 1503 1504 1505 1506 1507 1508 1509 1510 1511 1512 1513 1514 1515 1516 1517 1518 1519 1520 1521 1522 1523 1524 1525 1526 1527 1528 1529 1530 1531 1532 1533 1534 1535 1536 1537 1538 1539 1540 1541 1542 1543 1544 1545 1546 1547 1548 1549 1550 1551 1552 1553

. . . RQPGWS GWSQTPRES

. . . RQGGWS GWSQTFLOW

. . RIPZRR RCSINPUTSPRZRRELIEF S.. RVXPZR VLVPRZRQUALDF . . . RVOPZR VLVPRZRFLOWOPTION S.. RVNPZR VLVPRZRNPOINTSTAB . . . RVGPZR VLVPRZRFLOW_.TABLE . . RVPPZR VLVPRZRPROP-TABLE

RINCON RCSINITIALCONDITIONS RPINIT RPINIT RLINIT RLINIT RWINIT RWINIT RTCLIN RTCLIN RBINIT RBINIT RKPUMP RKPUMP RSINIT RSINIT

SGQPAR SGCTUBE-SECTIONS SGQNSE NUM_SGCSECT SGONNS RCSSGCNSECT SGODH RCSSGSECTDH SGODW RCS_SG_SECTDW SGQLH RCSSGSECTLH SGQLW RCSSGSECTLW SGQSET RCS_SGSECT-TEMP SGQQP RCS_SG_SECTQP SGQQS RCSSGSECT_QS SGQTTB RCSSGCSECTTTUBE SGQPR RCSSGSECT.PRESS SGQNSS SGSNSECT SGQOPT RCS_SGSECTTOPT SGQSEH RCSSGSECTEN'H

SGTRP SGTR DATA SCTLEN SGTR.TUBE-LENGTH SGTRK SGTRTUBE-ENTRANCEK SGTHT SGTRBREAKELEV SGTSLT SGTRSLOTBREAKOPT SGTSAR SGTRSLOT-BREAKAREA

SBPDAT SBLOCAPIPEDATA * SBPAR SBPIPEAREA . SBPLOD SBPIPELOD * SBPKG SBPIPEKGEOM * SBPKE SBPIPEKENT * SBPDZ SBDELTAELEV

CVDAT CVCSDATA . LDPDAT LDNPIPEDATA

. . . LDPAR LDNPIPEAREA LDPLOD LDNPIPELOD

. . . LDPKG LDNPIPE_KGEOM . . . LDPKE LDNPIPEKENT . . . LDPDZ LDNPIPEDELTAELEV . . . RMLDNB MALLDN_BREAK . . CVRHX CVCSREXDATA . . CVRHTL CVCS_RHX_TLDN . . . CVRHTC CVCSRHXTCH . . CVRHHL CVCSRHXHLDN * . CVRH•C CVCSRHXHCH . . . CVRHWL CVCSRHX WLDN . . . CVRHWC CVCSRHXWCH . . . CVRHQ CVCS_RMX_HEAT . . LDRCH LDNRCSENTH

LDRCP LDNRCSPRES SGS SGS_COMMON

SGSINT SGSINTERNAL SBOTP SGS-BOTP SCIOl SGS_CON_I01 SC102 SGSCON.IO2 SCPT1 SGS_CONPT1 SCPT2 SGSCON..PT2 SCXE1 SGS_CON_XEl SCEX2 SGS_CONXE2 SCBOR1 SCS-CON-BORON1 SCBOR2 SGS_CON_.BORON2 SDELTV SGS-DELTV SDP SGS_DP


RE RE RE RE IN IN RE RE RE RE RE RE RE RE RE RE RE IN IN RE RE LO LO RE RE RE RE RE IN IN RE RE RE RE RE LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

33

15 15 15

4

1051 16 16

16 16 20,8 20,8 20,8 20,8 20.8 8

11.16 28 8 8 4 4 4 20 4 4 4 4 4 50 20 2 2 2 2 2

30 2 2 2 2

4 4 1536 400 4 4 4 4 4 4 4 4 4 4 3,4

G-212

Definition

GWS pressure Gas flow quench tank to GWS Przr relief valves discharge model Opt 2/3 below this quality only, above=l Opt 0-3: crit.crit/bernbern/cd(dt),f(p) No. of points in discharge table Discharge table: dependent variable Discharge table: independent variable RCS initial conditions New initial pressurizer pressure New initial pressurizer level New initial total loop flow rate New initial cold leg temperature New initial boron concentration Pump head multiplier Pump initial speed Partition for SG tube model Number of sections in SO node (request) Number of sections in SG node (dynamic) Tolerance for SC node satn hysteresis Tolerance for SO node flow hysteresis State of SG node saturation hysteresis State of SG node flow hysteresis Pri temperatures of tube sections Pri heat rates of tube sections Sec heat rates of tube sections Tube temperatures of tube sections Pri pressures of tube sections Number of sections in each SC side Tube section primary T. 0=Exit, l=LMTD Section-bottom enthalpies (sectionnode) Data for SGTR Model SGTR tube length. 2 values/SG SGTR Entrance K fact-use 0.5-2 values/SC SGTR Elev above tube sheet - 1 value/SG SGTR Calculate slot break flow SGTR Slot area for Slot break option Data for SBLOCA pipe loss model SBLOCA pipe flow area SBLOCA pipe length/diameter SB pipe geom k-factor, excl entrance SBLOCA pipe entrance loss k-factor SB break elev above RCS connection CVCS model data Input data for letdown line loss model Ldn line flow area (pre,post RHX) Ldn line length/diameter (prepost RHX) Ldn line Kg, excl entry (pre,post RHX) Ldn line entry loss k-factor (@RCS,RHX) Ldn line elevation rise (prepost RHX) Ldn line break area (<0:pre, >O.postRHX) CVCS model calculated data Letdown temperature at RHEX inlet/exit Charging temperature at RHEX inlet/exit Letdown enthalpy at RHEX inlet/exit Charging enthalpy at RHEX inlet/exit Letdown mass flow rate Charging mass flow rate Regenerative heat exchanger heat load Enthalpy at letdown line RCS connections Pressure at letdown line RCS connections SG secondary global conmmon variables SG secondary internal variables Fluid pressure at SC tube sheet SC steam node iodine concentration SC evaporator node iodine concentration SC steam node particulates concentration SC evaporator node partic. concentration SC steam node xenon concentration SC evaporator node xenon concentration SC steam node boron concentration SG evaporator node boron concentration Multiplier on steam velocity Level instrum. delta press (refleg, sg)

Units

Psia Lbm/sec Partition Fraction Pointer Counts Undefined Undefined Partition Psia Feet Lan/sec Degree F Parts/million Fraction Shaft RPM Partition Counts Counts Btu/lbm Lbm/sec True False True False Degree F Btu/sec Btu/sec Degree F Psia Counts Pointer Btu/lbm Partition Feet Dimensionless Feet True False Ft^2 Partition Ft^2 Dimensionless Dimensionless Dimensionless Feet Partition Partition Ft^2 Dimensionless Dimensionless Dimensionless Feet Ft-2 Partition Degree F Degree F Btu/lbm Btu/lbm Lbm/sec Lbm/sec Btu/sec Btu/lbh Psia Segment Partition Psia Microcurie/liss Microcurie/lbln Microcurie/Ibn Microcurie/lbn Microcurie/lbm Microcurie/lbm Parts/million Parts/million Dimensionless Psid


Index No.

1554 1555 1556 1557 1558 1559 1560 1561 1562 1563 1564 1565 1566 1567 1568 1569 1570 1571 1572 1573 1574 1575 1576 1577 1578 1579 1580 1581 1582 1583 1584 1585 1586 1587 1588 1589 1590 1591 1592 1593 1594 1595 1596 1597 1598 1599 1600 1601 1602 1603 1604 1605 1606 1607 1608 1609 1610 1611 1612 1613 1614 1615 1616 1617 1618 1619 1620 1621 1622 1623 1624 1625 1626 1627

DimenTXM sions


SDVDP SGS_DVDP SENTHi SGSENTHI SENTH2 SCSENTH2 SENTH3 SGS_ENTH3 SENTH4 SGSENTH4 SENTH5 SGS_ENTH5 SOSEl SOSE1 SGSE2 SOSE2 SGSE3 SGSE3 SGSE4 SGSE4 SGSE5 SGSE5 SGSHF SGSHF SGSHG SGS.HG SHLEVL SGSJLEVEL SGSHT2 SGSHT2 SGSHT3 SGSHT3 SGSHT1 SGSHTI SGSMI1 SGS_.M SGSM2 SGS_M2 SGSM3 SGSM3 SGSM4 SGSM4 SGSM5 SGSM5 SGSP SGS_P SRECIR SGSRECIRC SRHO1 SGS-RHOI SRH02 SGSRH02 SRH03 SCS-RH03 SRHO4 SGS-RH04 SRH05 SGS_RH05 SGSSVI SGS_SVI SGSSV2 SGSSV2 SGSSV3 SGSSV3 SGSSV4 SGS_SV4 SGSSV5 SGSSV5 STREFL SGS_TREFLG STWALL SGS_TWALL SGST1 SGS_T1 SGST2 SGS_T2 SGST3 SGST3 SGST4 SGS_T4 SGST5 SGST5 SUSTM SGSUSTM SGSVF SGS_VF SGSVF2 SGS_VF2 SGSVF3 SGS_VF3 SGSVF4 SGS_VF4 SGSVF5 SGSVF5 SGSVG SGSVG SGSVI SGSV1 SGSV2 SGSV2 SGSV3 SGS_V3 SGSV4 SGSV4 SGSV5 SGS_V5 SGSWFI SGS_WF1 SGSWF2 SGSWF2 SGSWF3 SGS_WF3 SGSWF4 SGS_WF4 SGSWF5 SGSWF5 SGSWGI SGSWGI SGSWG2 SGSWG2 SGSWG3 SGS_WG3 SGSWG4 SGS_WG4 SGSWG5 SGS_WG5 SGSW13 SGS_W13 SGSW21 SGS_W21 SGSW23 SGS_W23 SGOSW31 SGSW31 SGSW32 SGS_W32 SGSW51 SGS_W51 SGSW25 SGS._W25 SCSW53 SGSW53 SGSW42 SGS_1W42 SWOUT SGS_WOUTSG SGSX1 SOSXI

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4.3 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 8 4

Definition

Slope of volume(pressure) curve SG steam node average specific enthalpy SG evaporator node average sp. enthalpy SG downcomer node average sp. enthalpy SG economizer node average sp. enthalpy SG quench-pool node average sp. enthalpy SG steam node total energy SG evaporator node total energy SG downcomer node total energy SG economizer node total energy SG quench-pool node total energy SO saturated liquid specific enthalpy SG saturated steam specific enthalpy SO coolant level SG evaporator coolant level SG downcomer coolant level Instrumnt-measured water levels (SG,1eg) SG steam node total mass SG evaporator node total mass SG downcomer node total mass SG economizer node total mass SG quench-pool node total mass SG steam node pressure SG evaporator to downcomer flow ratio SG steam node density SG evaporator node density SG downcomer node density SG economizer node density SG quench-pool node density SG steam node average specific volume SG evaporator node average spec volume SO downcomer node average spec. volume SG economizer node average spec volume SG quench-pool node average spec. volume SG reference leg water temperature SG wall metal temperature SG steam node temperature SG evaporator node temperature SG downcomer node temperature SG economizer node temperature SG quench-pool node temperature Steam velocity leaving separators SG saturated liquid specific volume SG evaporator node liquid spec. volume SG downcomer node liquid specific volume SG economizer node liq specific volume SG quench-pool node liq specific volume SG saturated steam specific volume SG steam node total volume SG evaporator node total volume SG downcomer node total volume SG economizer node total volume SG quench-pool node total volume SG steam node liquid mass SG evaporator node liquid mass SG downcomer node liquid mass SG economizer node liquid mass SG quench-pool node liquid mass SG steam node steam mass SG evaporator node steam mass SO downcomer node steam mass SG economizer node steam mass SG quench-pool node steam mass Stm node to dcomer condensation flowrate SG evaporator to steam node flow rate Evaporator to downcomer circulation flow Dcomer to steam node vapzation flow rate SG downcomer to evaporator flow rate Quench-pool to dome vaprzation flow rate Evap to quenchpool circulation flow rate Quench-pool to downcomer flow rate SG economizer to evaporator flow rate SG steam outlet nozzle flow SG steam node quality


Unit.

Composite Units Btu/Ibm Btu/lbm Btu/lbm Btu/lbm Btu/Ibm Btu Btu Btu Btu Btu Btu/Ibm Btu/ibm Feet Feet Feet Feet Lbm Lbm Lbm Lbm Lbm Psia Dimensionless Lbm/ ft^3 Lbm/ft^3 Lbm/ft^3 Lbm/ft^3 Lbm/ft^3 Ft^3/Ibm Ft^3/lbm Ft^3/llxn Ft^3/lbm Ft^3/lbm Degree F Degree F Degree F Degree F Degree F Degree F Degree F Ft/sec Ft^3/lbm Ft^3 /lbn Ft^3/lbm Ft^3/1bm Ft^3/Ibm Ft^3/lbn Ft^3 Ft^3 Ft^3 Ft^3 Ft^3 Lbm Lbm Lbm Lbm Lbm Lbm Lbm Lbm Lbm Lbm Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Lbm/sec Fraction

I

G-213


index Variabl a Name: No. Short Long

1628 1629 1630 1631 1632 1633 1634 1635 1636 1637 1638 1639 1640 1641 1642 1643 1644 1645 1646 1647 1648 1649 1650 1651 1652 1653 1654 1655 1656 1657 1658 1659 1660 1661 1662 1663 1664 1665 1666 1667 1668 1669 1670 1671 1672 1673 1674 1675 1676 1677 1678 1679 1680 1681 1682 1683 1684 1685 1686 1687 1688 1689 1690 1691 1692 1693 1694 1695 1696 1697 1698 1699 1700 1701

DimanMa siono

. SGSX2 SGSX2

. SGSX3 SGS_X3

. SGSX4 SGSX4 * SGSX5 SGSX5 . SGCHOK SGSFLOW_.CHOKED SHEAT SGSJHEAT

SQHOTR SGTRCSQHOT SQHOTS SGTSGOQHOT SQCLDR SGT RCSQCOLD SQCLDS SGTSGSQCOLD SQRECN SGTRCSQECON SQSECN SGT_SG_QECON STHOT SGTTEMPJHOT STCOLD SGTTEDPCOLD STECON SGTTEMP._ECON SQLOAD SGSHEATLOAD SQCONT SGSQCONT SQWALl SCS_._WALLI SQWAL3 S0S.Q..WALL3

MSLH SGS.STEAMLINE M.ODE MSLHKSTATE . MSLBO MAL.MSLBOUT

. . . MGSLBO MSLBOUTFLOW

. . . MCIO MSLKCONIO0 . . . MCPT MSLH.CONLPT

. . . MCXE MSLHCONXE

. . . MDVDH MSLHDVDH D . . M=P MSLHDVDP

. . . MSLHH MSLHH . . . HSLHHF MSLH_HF . . . MSLHHG MSLHHG . . . MSLHM MSLH_M . . MSLHML MSLHJL . . . MSLHP MSLHLP . . . MSLHQ MSLHQ . . . MQARM MSLHQ._ATM . - MSLHSV MSLEV . . . MSVF MSLH_SVF . . * MSVG MSLHiVG . . * MSLHT MSLH_T

. . . MTWALL MSLHLTWALL

. . . MWIN MSLHWIN S. . MSLHX MSLH_X - . MSLIN STEAMLINESTATE . . . MSLBI MALMSLBEIN - . . MGSLBI MSLBINJFLOW . . * MHSL MSLIHSL . . * MPSL MSLHJPSL . * . MTSL MSLHETSL . . . MISL MSLH-ISL . . . MCSL MSLHLCSL

MXSL MSLHXSL MIPOS MSLHIMSIVPOS MISIG MSLHMSIVSIG

. . MIBYPO MSLHLMSIV.BYPASSPOS

. . . MVPOS MSLIL/VALVESPOS

. * SMVSIG MSLHLVAL•/ESIG S* ESLPFLO SLPFLOW . . * MAOUT MSLHAOUT

S.*. . MAATM MSLHAOUTATM ..*. . MACOND MSLHAOUT_COND S.*. . MACONT MSLHIAOUTCONT . . . MATURB MSLHHAOUTTURB . . . MWOUT MSLH_WOUT

* . . MWATM MSLLWOUTATM * .*. . MWCOND MSLH_WOUT_COND . .-. . MWCONT MSLHMWOUTCONT

. . . MWTURB MSLHWOUTTURB . . . MGOUT MSLH0OUTFLOW S.. . MGATM MSLIFLOWLATM

. . . MEATM MSLILENTHATM

. . . MIATM MSLHIO.ATM

. . . MPATM MSLH_PTATM .. . . MXATM MSLHXEATM

RE RE RE RE LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

4 4 4 4 8 60 4 4 4 4 4 4 4 4 4

4 4 4 390 40

8

350 8 8 8 8 8 8 8 8 8 8 8 50 50 50 9,4 9 9 9 9 9,4 9 9 9 9 5,4

Definition

SG evaporator node quality SG downcomer node quality SG economizer node quality SG quench-pool node quality Flag: steam flow choked at restrictor SG heat transfer variables SG hot side RCS-to-tube heat transfer Hot side tube-to-secondary heat transfer SG entire cold side RCS-to-tube heat tr. Entire cold side tube-to-secy heat trans SG economizer RCS-to-tube heat transfer Economizer tube-to-secondary heat transf SG hot side tube metal temperature SG cold side tube metal temp, evaporator SG cold side tube metal temp, economizer Total secondary side heat load SG wall-to-containment heat rate SG steam node steam-to-wall heat rate SG downcomer node liq-to-wall heat rate SG steam line variables Steamline header variables Int:Stmline break in MSLH- 0=>no i=>yes Stmline break outside contment flowrate MSLH node iodine concentration MSLH node particulates concentration MSLH node xenon concentration MSLH node partial sp. vol with enthalpy MSLH node partial sp. vol. with pressure MSLH node enthalpy MSLH node saturated liquid enthalpy MSLH node saturated steam enthalpy MSLH node mass MSLH node liquid mass MSLH node pressure MSLH coolant-to-wall heat rate MSLH wall-to-atmosphere heat rate MSLH node specific volume MSLH node saturated liquid specific vol. MSLH node saturated steam specific vol. MSLH node temperature MSLH node pipe metal temperature Steamline steam flow into the header MSLH node quality Steamlines & stmline ext. valves SLB in stmln 0©No. l-3=various locations Steamline break inside contment flowrate SG steamline enthalpy SG steamline pressure SG steamline temperature SG steamline iodine concentrations SG steamline partic concentrations SG steamline xenon concentrations MSIV fraction open MSIV signal MSIV bypass fraction open Steamline external valves fraction open Steamline external valves signal Steamline external valves flow rates Steamline ext. valves combined areas Ext valves flow area, stmlines-atmospher Ext valves flow area, stmlines-condenser Ext valves flow area, stmlines-contnment Ext valves flow area, strnlines-turbine Steamline ext. valves combined flowrates Ext valves flow rate, stmlines-atmospher Ext valves flow rate, stmlines-condenser Ext valves flow rate, stmlines-contnment Ext valves flow rate, stmlines-turbine Steamline outflow quantities, inc. break Total flow rate, steamline to atmosph Total flow enthpy, steamline to atmosph Tot flow iodine conc, stmline to atmosph Tot flow partic conc, stmline to atmosph Tot flow xenon conc, stmline to atmosph


Units

Fraction Fraction Fraction Fraction True False Partition Btu/sec Btu/sec Btu/sec Btu/sec Btu/sec Btu/seec Degree F Degree F Degree F Btu/sec Btu/sec Btu/sec Btu/sec Partition Partition Flag Lbm/sec microcurie/lbm Microcurie/lbm Microcurie/ibm Composite Units Composite Units Btu/Ibm Btu/ibm Btu/lbm Lbm Lbm Psia Btu/sec Btu/sec Ft^3/lbm Ft^3/ ibm Ft-3/ibm Degree F Degree F Lbm/sec Fraction Partition Pointer Lbm/sec Btu/lbm Psia Degree F Microcurie/lbm Microcurie/lbm Microcurae/Ibm Fraction Fraction Fraction Fraction Fraction Lbm/s ec Partition Ft^2 Ft^2 Ft^2 Ft-2 Partition Lbm/sec Lbm/sec Lbm/sec Lbm/sec Partition Lbm/sec Btu/ibm Microcurie/ ibm Microcurie/Ibm Microcurie/l bm

G-214

Table G.2: Variables DictionarV in Tree Structure

Index Variabl e Name: No. short Long

DimenT @ions

1702 1703 1704 1705 1706 1707 1708 1709 1710 1711 1712 1713 1714 1715 1716 1717 1718 1719 1720 1721 1722 1723 1724 1725 1726 1727 1728 1729 1730 1731 1732 1733 1734 1735 1736 1737 1738 1739 1740 1741 1742 1743 1744 1745 1746 1747 1748 1749 1750 1751 1752 1753 1754 1755 1756 1757 1758 1759 1760 1761 1762 1763 1764 1765 1766 1767 1768 1769 1770 1771 1772 1773 1774 1775

. . . MOCOND MSLCFLOW.CSOND S . .. MECOND MSLH.SNTFLCOND . . . . MICOND MSLHM10_COND . . . . MPCOND MSLILPTCOND * . . MXCOND MSLHXECOND S . MGCONT MSLHLFLOW..CONT .. . . MECONT MSLHENTHCONT . . . MICONT MSLHIOSCONT S .. . . MPCONT MSLTCPTCONT .. . . MXCONT MSLHLXECONT S.. . MGTUR MSLHFLOC..TURB . . . METUR MSLHENTHTURB * . . . MITUR MSLHIO..TURB S .*. . MPTUR MSLHPTKTURB . . . MXTUR MSLHMXETURB . . . NETIOU MSLHIOJINTFLOW .. . . ITOTAT MSHEM10_INT_ATM * . * ITOTCD MSLHIOINTCOND . * ITOTCT MSLILIOJINTCONT . . . ITOTTU MSLMIOINT_TURB . * . IOCTLK MSLHLIO-CONTLEAK * . . . IOCTL MSLIOCONTINT-LEAK

. * MSCHOK HSLHFLOWCHOKED • SGSFWS SGSOFWS * . FPPIN FWSPUMPPIN . * FPPMP FWSPUMPS

FPJUN FWtSJUNCTION-P * FPVALV FWSVALVE&PRESSURES . . . FPVAL FWSEVALVEP

.- FPEVAL FWSECONYVALVE-P * . FSPMP FWSPUMPSPEED

FHPMP FWSPUMP-HEAD FGPMP FWSSPUMPFLOW

* . FGLINE FWSLINEJFLOWS FGLIN FWSEFLOW

. - FGELIN FWS-ECONFLOW * . FGTOT FWSFLOWJTOT * FWSENT FWSENTH * . FELINE FWS-LINEENTHALPIES

FELIN FWSLINE&H * FEELIN FWSECONLINEJH FIOCO* FWSCON-1IO

* FPTCON FWSCON_PT * FXECON FWSCON_XE

FGNOZZ FWSNOZZLEFLOW . FGNOZ FWSNOZJFLOW

. . . FGENOZ FWSECONNOZFLOW FENOZZ FWSNOZZLEENTHALPY . FENOZ FWS.NOZENTH

. . . FEENOZ FWSECON..NOZENTH FXNOZZ FWSENOZZLEQUALITY * FXNOZ FWSNOZQUAL * FXENOZ FWSEECONJNOZQUAL FTNOZZ FWS.NOZZLE-TEMP

* . * FTNOZ FWSNOZT . . . FTENOZ FWSECON NOZT . . FWLBIN FWLEIN . * FLBIN MALFWLBEIN . . FLBEIN MALJFWLBEECONJIN - * FWLBOU FWLBEOUT

.. . FLBOU MALFWLBOUT . . * FLBEOU MALFWLBECONOUT . * FWLBLO FWLBLOCATION . . . FWLBF FWLBF . . . FWLBEF FWLBECONWF . * FWLBW FWLB_W * * FLBW FWLBEFLOW . . * FLBEW FWLBECONWFLOW * * FWLBH FWLBEH . . * FLBH FWLBENTH . . * FLBEH FWLBECONENTH

FWLBX FWLBEQUALITY . FLBX FWLBQUAL * FLBEX FWLBECON!QUAL

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

Definition

Total flow rate. steamline to condnsr Total flow enthpy, steamline to condnsr Tot flow iodine conc, stmline to condnsr Tot flow partic conc, stmline to condnsr Tot flow xenon conc, stmline to condnsr Total flow rate, steamline to contmnt Total flow enthpy, steamline to contont Tot flow iodine conc, stmline to contmnt Tot flow partic conc, stmline to contrmnt Tot flow xenon conc, stmline to contnmt Total flow rate, steamline to turbine Total flow enthpy, steamline to turbine Tot flow iodine conc, stmline to turbine Tot flow partic conc, stmline to turbine Tot flow xenon conc, stmline to turbine Integrated iodine flows Integrated iodine flow to atmo Integrated iodine flow to cond (w/o DF) Integrated iodine flow to cont Integrated iodine flow to turb (w/o DF) Iodine leak rate from containment Integrated iodine leak from containment Flag: flow choked between header & MSLB SG feedwater system variables Main FW pumps suction pressure, constant Main feedwater pump discharge pressure Main FW piping junction pressure Main FW valve discharge pressure FW downcomer valve discharge pressure FW economizer valve discharge pressure Main feedwater pump speed Main feedwater pump head Main feedwater pump delivered flow Flow through main FW control valves Main FW flow rate at downcomer valves Main FW flow rate at economizer valves Total MFW flow to SG thru dc & ec valves Main feedwater flow spec. enthalpy Inventory enthalpies in main FW lines Downcomer feedwater line enthalpy Economizer feedwater line enthalpy Main feedwater supply iodine concent. Main feedwater supply partic concent. Main feedwater supply xenon concent. Main FW flow rates at SG feed nozzles Main FW flow rate at downcomer nozzle Main FW flow rate at economizer nozzle Main FW flow enthalpy at SG feed nozzles Main FW flow enthalpy at downcomer nozzl Main FW flow enthalpy at economiZr nozzl Main FW flow quality at SG feed nozzles Main FW flow quality at downcomer nozzle Main FW flow quality at economiZr nozzle Main FW flow temp at SG feed nozzles Main FW flow temp at downcomer nozzle Main FW flow temp at economizer nozzle Cues for feedline break inside chk valve Feedline break inside chk valve, DC line Feedline break inside chk valve, EC line Cues for feedline brk outside chk valve Feedline brk outside chk valve, DC line Feedline brk outside chk valve, EC line Feedline break locations- 0=valve l=nozz Feedline break location, downcomer line Feedline break location, economizer line Feedline break flow rates Downcomer feedline break flow rate Economizer feedline break flow rate Feedline break flow enthalpies Downcomer feedline break flow enthalpy Economizer feedline break flow enthalpy Feedline break flow qualities Downcomer feedline break flow quality Economizer feedline break flow quality

Units

Lbm/sec Btu/lbm Microcurie/lbm Microcurie/lbm Microcurie/Ibm Lbm/sec Btu/lbm Microcurie/lbm Microcurie/lbm Microcurie/lbm Lbm/sec Btu/lbm Mxcrocurie/lbm Mxcrocurie/ibm Microcurie/lbm Partition Curie Curie Curie Curie Microcurie/sec Curie True False Partition Psia Psia Psia Psia Psia Psia Shaft RPM Feet Gal/min Lbm/sec Lbm/sec Lbm/ sec Lbm/ sec Btu/lbm Btu/ibm Btu/Ibm Btu/ ibm Microcurie/lbm Microcurie/ibm Microcurie/lbm Lbm/sec Lbm/sec Lbm/sec Btu/lbm Btu/lbm Btu/lbm Fraction Fraction Fraction Degree F Degree F Degree F Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Lbm/sec Lbm/sec Lbm/sec Btu/Ibm Btu/lbm Btu/lbm Fraction Fraction Fraction


10

8 180

4 4 4,2 4 4 4 4 4 4,2 4 4 4 4 4,2 4 4 4 4 4 4,2 4 4 4,2 4 4 4,2 4 4 4.2 4 4 4,2 4 4 4,2 4 4 4,2 4 4 4,2 4 4 4,2 4 4 4,2 4 4

G-215


Dimenn sions

Var i a bl e Name: Short Long

Index NO.

1776 1777 1778 1779 1780 1781 1782 1783 1784 1785 1786 1787 1788 1789 1790 1791 1792 1793 1794 1795 1796 1797 1798 1799 1800 1801 1802 1803 1804 1805 1806 1807 1808 1809 1810 1811 1812 1813 1814 1815 1816 1817 1818 1819 1820 1821 1822 1823 1824 1825 1826 1827 1828 1829 1830 1831 1832 1833 1834 1835 1836 1837 1838 1839 1840 1841 1842 1843 1844 1845 1846 1847 1848 1849

FWLBIO FWLBJIODINE FLBIO FWLBIJO FLBEIO FWLBECON-JO

FWLBPT FWLB-PART . FLBPT FWLBPT . FLBEPT FWLBECONPT FWLBXE FWLBJXENON . FLBXE FWLBXE . FLBEXE FWLBSECONXE SGNAFW AFWSNOZJFLOW SEAFWS AFWSENTH

SGBD SGS0SGBD SBITNK SGBDCONSIO SBPTNK SGBDOCON..PT SBXTNK SGBDCONXE SBDVDH SGBDDVDH SBDVDP SGBDDVDP SGBDH SGBDOH SGBDHF SGBDOHF SGBDHG SGBD..EG SGBDL SGBD0L SBBDM SGBD_M SGBDML SGBDML SGBDP SGBD0 P SGBDSV SGBDOSV SVSVF SGBD0SVF SBSVG SGBDSVG SGBDT SGBDT SBTWAL SGBDTWALL SGBDX SGBDX SBVPOS SGBD_SGPOS . SBVSUR SGBD.SURF.POS

SBVBOT SGBDBOTPOS SBG SGBDSGtFLOW

* . . SBGSUR SGBDSURFSFLOW SBG.OT 0SGBDBOTFLOW

SBENTH SGBDSGENTH . . . SBESUR SGBDSURF.ENTH

. SBEBOT SGBD5BOTENTH SBIO SGBDOSGQ1O

SBISUR SGBDSURFIO SBIBOT SGBD0BOT.I0

SBPT SGBDSGPT . SBPSUR SGBDSURFPT . SBPBOT SGBDBOTPT SBXE SGBD.SGCXE . SBXSUR SGBDOSURFXE . SBXBOT SGBDBOOTCXE SBVSNK SGBDSINKSPOS . SBVOUT SGBDOUTPOS . SBVREL SGBDRELIEF-POS SBGSNK SGBDSINKFLOW . SBCOUT SGBDOUTSFLOW . SBGREL SGBDRELIEFFLOW

. SBESNK SGBDSINK-ENTH . SBEOUT SGBDOUTNTH . SBEREL SGBD5RELIEFENTH SBISNK SGBDOSINK-10

. . . SBIOUT SGBDOUTIO • SBIREL SGBD-RELIEF-10 SBPSNK SGBD0SINKPT

. . . SBPOUT SGBD_0OUT_PT . SBPREL SGBDRELIEFPT SBXSNK SGBDSINKXE . SBXOUT SGBD0_OUTXE . SBXREL SGBDRELIEFJXE SBPRSN SGBDSINKP

S.. SBPROT SGBD5OUTSP . DBPRRL SGBDCRELIEFP SBMODF MOD_OFF0SGBD

STUNE SGSTUNE STCONT CONTSGOTEMP MFTMAX MSLMFTIMEMAX

- MPRESC PCONDENSER

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RELO RE 50 RE 4 RE RE

4,2 4 4 4.2 4 4 4,2 4 4 4 4 100

8 4 4 8 4 4 8 4 4 8 4 4 8 4 4 8 4 4 3 2

3 2

3 2

3 2

3 2

3 2

3 2


Definition

Feedline break flow iodine concentratins Downcomer feedline brk flow iodine conc Economizer feedline brk flow iodine conc Feedline break flow partic concentratins Downcomer feedline brk flow partic conc Economizer feedline brk flow partic conc Feedline break flow xenon concentrns Downcomer feedline brk flow xenon conc Economizer feedline brk flow xenon conc Auxiliary feedwater flow to separate noz Auxiliary feedwater flow spec. enthalpy SG blowdown system variables SGBD tank iodine concentration SGBD tank particulates concentration SGBD tank xenon concentration SGBD tank partial sp. vol with enthalpy SGBD tank partial sp. vol. with pressure SGBD tank specific enthalpy SGBD tank saturated liquid enthalpy SGBD tank saturated steam enthalpy SGBD tank water level SGBD tank total mass SGBD tank liquid mass SGBD tank pressure SGBD tank specific volume SGBD tank sat. liquid specific volume SGBD tank sat. steam specific volume SGBD tank fluid temperature SGBD tank wall metal temperature SGBD tank quality SG blowdown line valves Surface blowdown lines valve positions Bottom blowdown lines valve positions SO blowdown line flow rates Surface blowdown line flow rates Bottom blowdown line flow rates SG blowdown line flow enthalpies Surface blowdown line flow enthalpies Bottom blowdown line flow enthalpies SG blowdown line flow iodine concs Surface blowdown line flow iodine concs Bottom blowdown line flow iodine concs SO blowdown line flow partic concs Surface blowdown line flow partic concs Bottom blowdown line flow partic concs SG blowdown line flow xenon concs Surface blowdown line flow xenon concs Bottom blowdown line flow xenon concs SGBD tank discharge line valves SGBD tank outlet lines valve positions SGBD tank relief line valve position SGBD tank discharge line flow rates SGBD tank outlet lines flow rates SGBD tank relief line flow rate SGBD tank discharge line flow enthalpies SGBD tank outlet lines flow enthalpies SGBD tank relief line flow enthalpy SGBD tank disch. line flow iodine concs SGBD tank outlet lines flow iodine concs SGBD tank relief line flow iodine conc SGBD tank disch. line flow partic concs SGBD tank outlet lines flow partic concs SGBD tank relief line flow partic conc SGBD tank disch. line flow xenon concs SGBD tank outlet lines flow xenon concs SGBD tank relief line flow xenon conc SGBD tank disch. line dwnstrm pressures SGBD tank outlet lines dwnstrm pressures SGBD tank relief line dwnstrm pressure Turns off SGBD model SG adjustable constants Containment temperature at SGS Maximum time step size for MSLH model Condenser pressure

Units

Microcurie/lbmn Microcurie/lbm Microcurie/lbm Microcurie/lbm Microcurie/lbm Microcurie/lbm Microcurie/lbn Microcurie/Ibm Microcurie/lbn Lbm/sec Btu/llbn Partition Microcurie/Ibm Microcurie/lbm Microcurie/lbm Composite Units Composite Units Btu/Ibm Btu/lbh Btu/lbm Feet Lbm Lbm Psia Ft'3/llm Ft^3/ lbm Ft'3/lbm Degree F Degree F Fraction Partition Fraction Fraction Partition Lbm/sec Lbm/sec Partition Btu/lbm Btullbm Partition Microcurie/lbm Microcurie/lbm Partition Microcurie/lbs Microcurie/lbm Partition Microcurie/lbm Microcurie/Ibm Partition Fraction Fraction Partition Lbm/sec Lbm/sec Partition Btu/lbm Btu/lbm Partition Microcurie/lbm Microcurie/lbn Partition Microcurie/lbm Microcurie/Ibm Partition Microcurie/lbm Microcurie/Ibm Partition Psia Psia True False Partition Degree F Seconds Psia

G-216


Index No.

1850 1851 1852 1853 1854 1855 1856 1857 1858 1859 1860 1861 1862 1863 1864 1865 1866 1867 1868 1869 1870 1871 1872 1873 1874 1875 1876 1877 1878 1879 1880 1881 1882 1883 1884 1885 1886 1887 1888 1889 1890 1891 1892 1893 1894 1895 1896 1897 1898 1899 1900 1901 1902 1903 1904 1905 1906 1907 1908 1909 1910 1911 1912 1913 1914 1915 1916 1917 1918 1919 1920 1921 1922 1923

M2CIO M2CPT M2CXE M2DVDH M2DVDP M2SLHH M2SLHF M2SLHG M2SLM M2SLML M2SLP M2SLQ M2QARM M2SLSV M2SVF M2SVG M2SLT M2TWAL

MSLH2_CON_I0 MSLH2_CONPT MSLH2_CONJXE MSLH2_DVDH MSLH2_DVDP MSLH2JH MSLH2MHF MSLH2_HG MSLH2_M MSLH2JML MSLH2_P MSLH2-0 MSLH2_Q__ATM MSLH2_SV MSLH2_SVF MSLH2_SVG MSLH2_T MSLH2JTWALL


SASEPT SGS-ASEPTUNE SGSM SGSDELTVJAX SFK3T SGS_FK3_TUNE SFTIME SGSFTIME SFPMAX SGS_FTIMEPMAX SLHASB SGSJHASUBSOPTION SPCONV SGSPCNVRG SPMIN SGSPMIN SDVREC SGSRECIRCDELVOL SRECMN SGS_RECIRCJMIN SSEPMN SGSSEPSPHIN STRTUN SGSTAURC1-TUNE STRMAX SGS_TAURC2_MAX STGMAX SGSTAUJWOUTSG SPERIM SGSUADROP-PERIM SFDMIN SGSUADROPWFDMIN SUSTMN SGSUSTM_MIN SVCONV SGSVCNVRG SWFMIN SGS_WFMIN SX2RG1 SGSX2_1 SCOLDT SGTJHTCRTC SHOWT SGT_HTCRTH SH22SUB SGT_HTCSCW SH2STM SGTHTCSTM SQMULT SGTQJMULT MDPMIN MSLM_DPMILMULT SVFREF SGSSVF.REF SVGREF SGSVGREF SVLEGR SGS_VLEGOREF SGTAU SGSTAUFLOW SGXTAU SGSXTAU_FLOW SCRMOD SGS_CRIT_MODEL

SHORE SGS_MORE_VARIABLES SINCON SGS_INITIALCONDITIONS * SPINIT SPINIT

SLINIT SLINIT * FHINIT FHINIT * SKAMUL SKAMUL SADEG SGSSTUBE.AREASDEGRAD - SADGOP SGSTUBEAREAOPTION * SADFUL SGSJIASSFULLTUBE-AREA * SADZER SGS_MASS_ZEROTUBEAREA FHTBL FWS_ENTHLTABLE * FHENTH FWSITABLEENTH - FHLOAD FWSHTABLE_.LOAD * FHNUM FWSJHTABLEJNUM SECON SGS_ECONVARS

STPINE SGS_ECO1_TPIN STPOTE SGS-ECONTPOUT STFINE SGS_ECONTFIN STFOTE SGS_ECO?_TFOUT SASUBE SGSECONASUB STCAVE SGS_ECONTCAV SCNVRG SGS_ECONCNVRG SFLIME SGSECON_FLIM

MNODE2 MSLH2_STATE

DimenTM• sions

RE RE RE RE RE LO RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE 4 RE 4 RE RE RE 4 RE RE RE RE RE 2 RE 2

IN RE 120 RE 15 RE RE RE RE 4 RE 10 LO RE 4 RE 4 RE 50 RE 20 RE 20 IN RE 40 RE 4 RE 4 RE 4 RE 4 RE 4 RE 4 RE RE RE 40 RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE

MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2 MSLH2

node iodine concentration node particulates concentration node xenon concentration node partial sp. vol with enthalpy node partial sp. vol. w pressure node enthalpy node saturated liquid enthalpy node saturated steam enthalpy node mass node liquid mass node pressure coolant-to-wall heat rate wall-to-atmosphere heat rate node specific volume node saturated liquid spec. vol. node saturated steam specific vol. node temperature node pipe metal temperature

Definition

SGS steam separator area tuning factor Multiplier for maximum steam velocity SGS downcomer flow coeff. tuning factor SGS models fast-time step size Max pressure for fasttime w/ MSIV open Option for calculating subcooled region Pressure convergence criterion Minimum secondary-side pressure Delta volume for adjusting recirc flow Minimum recirculation for crossflow Minimum pressure for separation model SGS recirc flow time const tuning factor SGS downcomer flow max time constant Unused spare Perimeter of the feedring MHn feedflow below which condens eff = 1 Minimum steam separation velocity Volume convergence criterion Reg. 2 liq mass for single-region switch Reg. 2 quality to re-establist reg. 1 SG cold side heat transfer tuning factor SG hot side heat transfer tuning factor H.t. coeff if region 2 is subcooled H.t. coeff in region 2 if surface is ste Multiplier on SG tube heat transfer area Min del-P for flow coeff, frac of DP100 Liquid sp.vol for level instrum calibr Steam sp.vol for level instrum calibr Ref-leg spvol for level instrum calibr Steamflow time const @ lo/hi valve rates Fractional valve rates for SGStau_flow LiqI2-phs choked flow model: 0=HEM, l=HF SGS misc additional variables SGS initial conditions New initial steam generator pressure New init SG sec side mixture level New initial feed water enthalpy SG tube area multiplier Secondary tube area degradation model Option to degrade secondary tube area Min mass for full sec tube area Mass for zero secondary area Table of main feedwater enthalpy vs load Table: MFW norm enthalpy, (h-Hl)/(H2-HI) Table: turbine normalized load, W/Wrated Table: number of entries More vars for the SG economizer model Economizer primary inlet temperature Economizer primary outlet temperature Economizer feedwater inlet temperature Economizer feedwater outlet temperature Economizer area in subcooled heat trans SG cold side average primary temperature Converg criterion for econ ht iteration Min MFW flow to econ Below: model off Steamline header node 2 variables


Units

Dimensionless Dimensionless Dimensionless Seconds Psia True False Psia Psia Ft^3 Dimensionless Psia Dimensionless Seconds Unused Feet Lbm/sec Ft/sec Fraction Lb. Fraction Composite Units Composite Units Btu/secft^2degF Btu/secft^2degF Dimensionless Fraction Ft^3/lbm Ft^3llbm Ft^3/lbm Seconds Fraction Pointer Partition Partition Psia Feet Btu/lbm Fraction Partition True False Lbs Lbm Partition Dimensionless Dimensionless Counts Partition Degree F Degree F Degree F Degree F Ft^2 Degree F Dimensionless Lbm/sec Partition Microcurie/lbm Microcurie/lbm Microcurie/lbm Composite Units Composite Units Btu/lbm Btu/lbm Btu/lbm Lbm Lbm Psia Btu/sec Btu/sec Ft^3/lbm Ft^3/lbm Ft^3/lbs Degree F Degree F

I

G-217


index Va riable Name: No. Short Long

Dimen

im sions

1924 1925 1926 1927 1928 1929 1930 1931 1932 1933 1934 1935 1936 1937 1938 1939 1940 1941 1942 1943 1944 1945 1946 1947 1948 1949 1950 1951 1952 1953 1954 1955 1956 1957 1958 1959 1960 1961 1962 1963 1964 1965 1966 1967 1968 1969 1970 1971 1972 1973 1974 1975 1976 1977 1978 1979 1980 1981 1982 1983 1984 1985 1986 1987 1988 1989 1990 1991 1992 1993 1994 1995 1996 1997

. . M2SLX MSLH2_X RE CTL CONTROL-COMMON RE

CTIME CTLTIMESTEP RE CTCONT CTLSCORE-CONTROL RE . CTSET CTLCORESETPOINTSFOR.TRIP RE

. CTPOHI CTLCORE-HIIPOWERFRAC-TRIP RE

. CTSRHI CTLCORE_.HIPOWERSUR_.TRIP RE

. CTPPLO CTLCORELOW-PRZRPRESTRIP RE

. CTPPHI CTLCORE-HI-PRZRPRES-TRIP RE

. CTLPHI CTLCOREHIPRZRLEVELTRIP RE

. CTTMAR CTLCOREOVER_TEMP_MRGNTRIP RE

. CTWMAR CTLCOREOVER.POWER_4RGNTRIP RE

. CTGRCS CTLCORERCSFLOW-FRACTRI P RE

. CTSIAS CTLCORE-SIAS-TRIP RE

. CTPSGL CTLCORELOWSGPRESTRIP RE

. CTLSGL CTLCORELOWSGLEVELTRIP RE

. CTLSGH CTLCOREHISGLEVELTRIP RE

. CTGSGM CTLSTEAM-FEED-MI SMATCHTRI P RE

. CTDTUR CTLCORETURBTRIPDELAY RE

. CTPCHI CTLCOREHICONT-PRES.TRI P RE

. CTUSER CTL_COREUSERDEFINED_TRIP RE

. CTGKSP CTL RCPFLOWSTPOINT RE

. . CTSRBY CTLCORE-HI-POWER.SUR-BYPS RE CTPORA CTLCOREPOWER.RATIO RE CTGSBY CTLSTEAMFEED_-MISMATCIBYPS RE CTTUBY CTL_CORETURBTRIP_BYPS RE

. CTUSBY CTLCOREUSERDEFINEDBYPS RE * COVER CTLCORETRIPOR RE . . COPOHI CTLCOREHIPOWERFRACTRIP0OR RE - COSRHI CTLCORE-HIPOWERSUtRTRIP_OR RE . . COPPLO CTLCORELOW.PRZRPRES-TRIP-OR RE . COPPHI CTLCORE_HI_PRZRPRES_TRIP _OR RE . . COLPHI CTLCOREHI_PRZRLEVEL_TRIPPOR RE . COTMAR CTLCOREOVERTEMPRGN TRIPOR RE . COWMAR CTLCOREOVERPOWERMRGNTRIP-OR RE . COGRCS CTLCORE-RCSFLOW-FRACTRIP_OR RE . COSIAS CTLCORESIASTRIPOR RE . COPSGL CTLCORELOW_SG_PRES_TRIPOR RE . COLSGL CTLCORE-LOW-SGLEVEL-TRIP-OR RE . COLSGH CTL_CORE_HI_SGLEVELTRIP_OR RE . COGSGM CTLSTEAM-FEEDMISMATCHTRIPOR RE . CODTUR CTLCORE_TURB.TRI PDELAYOR RE . COPCHI CTLCOREHICONT-PRESTRIPOR RE . COUSER CTL_CORE_USERDEFINEDTRIPOR RE

CKTRPT CTLTIMECORETRIP RE COREQ CTLCOREPOWER RE COREOT CTL_QCORETRIP RE CPOWFR CTLCORE-POWER-FRACTION RE CPOWFL CTLCOREPOWERFRACLAST RE CNRPS CTLNUMRPS IN CKAUTO CTLSCORECONTROL.AUTO LO CKTRP CTLCORETRIP LO CKTRPS CTLCORETRIPSIG LO CKTRPP CTL CORE-PTRIP LO

CCEA CTL_CEACOMMON RE CRSET CTLCEA-SETPOINTS RE . CRTNO CTLCEATREF.NO RE

. . CRTFUL CTLCEA.TREF-FULL RE

. * CREXP CTLCEA&GAIN.EXP RE

. CRGAIN CTLCEA_TURBLDGAIN RE CRFPOS CTLCEAPOSITION..FRAC RE CRMOTL CTLCEA.LAST-TIME RE CRMAX CTLCEAMAX RE CRMIN CTLCEA-MIN RE CRPOS CTLCEAPOS RE CRSPD CTLCEASPEED RE CRSTEP CTLCEASTEP RE CAUTO CTLCEA-AUTO LO CRPERF CTLCEAPERFECT LO CRACCM CTLCEAACCUM RE CRSPDL CTLCEA.SPEEDLAST RE

CCVCS CTL_CVCSCOYXON RE . CPSET CTLPRZRLEVELSETPOINTS RE

.* CPTEM CTLPRZRPLEVELTEMP RE

5120

110 45

10 5 2

10 25

10

25

20 6

85 9 2

Definition

MSLH2 node quality Control, protective, and bop systems Time step delt available to controllers Core control partition Partition for RPS setpoints Hi power fraction scram setpoint High power SUR scram setpoint Low przr pressure scram setpoint High przr pressure scram setpoint High przr level scram setpoint Thermal margin setpts for over temp trip Thermal margin setpts for over pwr trip Low loop flow scram setpoint Scram due to SIAS Low SG pressure scram setpoint Low SQ level scram setpoint High SG level scram setpoint Steam-feed flow mismatch scram setpoint Scram due to turb trip. time delay Hi cont. pressure scram setpoint Space for other scram setpoints Low primary flow scram setpoints Hi power SUR scram-inhibit setpoints Logrithmic rate of power change Scram on flow mismatch, inhibit setpoint

-Scram on turbine trip: inhibit setptoint Space for other scram inhibit setpoints Partition for scram overrides Hi power fraction scram override High power SUR scram override Low przr pressure scram override High przr pressure scram override High przr level scram overrides Over-temp thermal margin scram override Over-power thermal margin scram override Low loop flow scram override Scram due to SIAS override Low SG pressure scram override Low SG level scram override High SG level scram override Steam-feed flow mismatch scram override Scram due to turb trip override Hi cont. pressure scram override Space for other scram overrides Time elapsed after scram Core power Core power at time of trip Core power, fraction of rated Core power fraction, last step Number of RPS channels Flag: automatic control of core Core tripped flag Scram signals Scram signal at last time step Control-element assembly model Setpoints for reactor regulating system Reference (avg) primary temp at no load Reference (avg) primary temp, full load Exponent for nonlinear gain=demand**exp Nonlinear gain for crr system Fractional average rod position CEA motion time Maximum CEA withdrawal position Minimum CEA withdrawal position CEA withdrawal position CEA motion speed and direction Step size of control rod motion Flag: auto/manual CEA control Flag: CEA perfect controller CEA control accumulated signal CEA speed and direction, last step Chemical & volume control system Przr level setpoints Przr level-program temperature setpoints


Units

Fraction Segment Seconds Partition Partition Fraction Decades/mmn Psia Psia Fraction Del-degF Del-degF Fraction Fraction Psia Fraction Fraction Lbm/sec Seconds Psia Undefined Lbm/sec Fraction Dimensionless Fraction Lbm/sec Undefined Partition Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Override Normal Seconds Btu/sec Btu/sec Fraction Fraction Counts Auto Manual Trip Normal Active Inactive True False Partition Partition Degree F Degree F Dimensionless Dimensionless Fraction Seconds Steps Steps Steps Steps/min Inches True False True False Steps Steps/min Partition Partition Degree F

G-218


Index V a ria b I e N a m e: No. short Long

1998 . . . CPLEV CTL_PRZRPLEVEL 1999 . . . CPSLIQ CTLPRZR_.LIQ_.SPVOLREF 2000 . . . CPSSTM CTLPRZR_.STMCSPVOLREF 2001 . CLSET CTLJLETDOWNSETPOINTS 2002 . CLLSP CTLCVCSLDNMZSPOINT 2003 . CLGSP CTLCVCS_LDN._.LGPM 2004 . CCSET CTL_CHARGING_SSETPOINTS 2005 - CCLSP1 CTL_.CVCSCHMSSPOINT 2006 . . CCLSP2 CTLCVCS.CH2_SPOINT 2007 . CCLSP3 CTLCVCSCH3_SSPOINT 2008 . CCLSP4 CTLSCVCSSCH4_SPOINT 2009 . . . CCGRAT CTLCHPUMPRWATED 2010 . CPPROG CTLCVCSCONTROL 2011 . . . CPLPRG CTLPRZRPROGLEVEL 2012 . . CPLERR CTLPRZRLEVELSERROR 2013 . . . CPLINS CTLPRZRLEVELINST 2014 . CTAVG CTL_T_AVG 2015 . . . CTREF CTLS...REF 2016 . . . CCFPMP CTL_CH_PUMP_FRAC 2017 . . CCAUTO CTLCHPUMPP_AUTO 2018 . . . CCPMPO CTL_CHPUMPON 2019 CLAUTO CTLLDNAUTO 2020 CCVALV CTLCVCSRCSVALVES 2021 . CCFVAL CTLSCHV.FRAC 2022 . . . CCAVAL CTLCHVRAREA 2023 . CXREG CTL_CVCSTHSVARIABLES 2024 . . . CXHA CTL_HA_REGJHEATX 2025 CLFLOW CTLLDNLFLOW 2026 CLTEMP CTLLDN_T

2027 . . . CLENTH CTL-LDNJH 2028 . . . CLFRAC CTLaLETDOWNFRAC 2029 . . . CCFLOW CTLCH_FLOW 2030 . . CCTEMP CTL_CH_T 2031 . . . CCENTH CTLCHJH 2032 CHEATR CTLHEATERSCONTROL 2033 . CHSET CTLPRZRRHEATERSETPOINTS 2034 . . . CHLBSP CTLPRZRBHLEVEL_SPOINT 2035 . . . CHLOFF CTLLEVELJHEATEROFF 2036 . . . CHPPOF CTL_.PRESPHEATER.OFF 2037 . . . CHPPON CTLPRESSPHEATER0ON 2038 . . . CHPBOF CTLPRESBHEATER_OFF 2039 . . . CMPBON CTLkPRES_BHEATER_ON 2040 . . CHPREF CTLPRZRREFPRES 2041 CHVPRP CTL3VOLT-PROP 2042 CHVBAK CTL.VOLTBACK 2043 CHVRAT CTLSPRZRHEATERSVOLT 2044 CHAUTO CTL_HEATERSCONTROLAUTO 2045 CSPRAY CTLPRZRSPRAY_CONTROL 2046 . CWSET CTLPRZR.SPRAY,_SETPOINTS 2047 . . . CWPON CTLPRZRSPRAY_PRES_ON 2048 . . CWPOFF CTLPRZRSPRAYPRESOFF 2049 . CWAUTO CTL3PRZRSPRAYCONTROLAUTO 2050 CVRELF CTL PRESSURIZER_RELIEF 2051 . CVSET CTLPRZRRELIEFSETPOINTS 2052 . . . CVPSET CTL PORVJPSET 2053 . . . CVOPEN CTLPSVPSETOPEN 2054 . . CVCLOS CTLPSV_PSETSCLOSE 2055 . . . CVBLDN CTLPSVPSET_BLDN

2056 . CVAUTO CTL&PORV.AUTO 2057 CECCS CTL.SISCOMMON 2058 . CESET CTLSIASSETPOINTS 2059 . CEPLO CTLSIAS-PRZR_.PRESLOW 2060 . CEDPSL CTL_SSIASSL_.SH_DP 2061 . . . CEPCHI CTL_.SIAS_HICONT_PRES 2062 . . CETAVL CTLSIAStLOWtTAVG 2063 CEPSLL CTLSIASLOW.SLPRES 2064 CESIS CTL SISCONTROL 2065 . . . CENHPS CTLHPSINPOINTS_TAB 2066 CEGHPS CTLJPSIFLOWtTABLE 2067 . . . CEPHPS CTL_HPSIPRESTABLE

2068 . . . CEHNUM CTLHPSIPUMP-NUM 2069 . . CESHPS CTLHPSI_SPLIT 2070 . . . CENLPS CTLLPSINPOINTS_TAB 2071 . . CEGLPS CTLLPSIFLOWTABLE

DimenT!U siona

RE 2 RE RE

Definition

Przr level-program level setpoints Przr instrum. ref. liquid specific-vol Przr instrum. ref steam specific-vol

6 Letdown control setpoints 2 Letdown level control setpoints 2 Letdown flow setpoints 15 Charging pump control setpoints 2 Charging pump 1 control setpoints 2 Charging pump 2 control setpoints 2 Charging pump 3 control setpoints 2 Charging pump 4 control setpoints 4 Charging pump rated flow 24 CVCS control variables

Pressurizer programnmed level Pressurizer level error Przr instrumentation level reading Average primary coolant temperature Demand reference temperature

4 Charging pump fractional flow 4 Flags' charging pumps automatic control 4 Charging pumps on-off indicator

Flag- letdown automatic control 10 CVCS-RCS valve connections 5 Fractional opening of charging valve 5 Charging valve relative flow areas 15 CVCS thermal-hydraulic variables

Regen. heat exchanger overall ht coeff. Letdown mass flow rate

2 Letdown temperature at RHEX inlet/exit 2 Letdown enthalpy at RHEX inlet/exit 4 Letdown flow fraction

Total charging pumps delivery 2 Charging temperature at RHEX inlet/exit 2 Charging enthalpy at RHEX inlet/exit 18 Heaters control partition 10 Heater control setpoLnts 2 Przr heaters hi-level on/off setpoints

Heaters low-level cutoff setpoint Prop heaters high pressure setpoint Prop heaters low pressure setpoint Backup heaters high pressure setpoint Backup heaters low pressure setpoint Reference p for przr pressure control Proportional heaters voltage Backup heaters voltage Przr heaters rated voltage Flag. automatic ctrl of przr heaters

5 Pressurizer main spray controls 4 Przr spray control setpoints

Przr spray ctrl high-press. on-setpoint Przr spray ctrl low-press off-setpoint Flag: automatic control of przr spray

26 Przr PORV and SV control variables 20 Przr relief and safety valve setpoints 4 PORV opening pressure setpoints 4 Przr safeties full-open setpoints 4 Przr safeties full-closed setpoints 4 Przr safeties re-closing setpoints 4 Flags: automatic control of PORVs 200 Safety injection system 8 Safety injection syst setpoints

Low pressure setpoint for SIAS Steamline flow trip setpoint High containment press setpoint for SIAS Low temperature setpoint for SIAS Low steamline pressure setpoint for SIAS

150 Safety injection syst control variables No. of pairs in HPSI flow vs press table

45 Flows for HPSI flow-vs-pressure table 15 Back press for HPSI flow-vs-press table

Number of operating HPSI pumps 8 HPSI flow split to injection points

No. of pairs in LPSI flow vs press table 45 Flows for LPSI flow-vs-pressure table

Units

Fraction Ft^3/lbm Ft^3/lbm Partition Fraction Gal/min Partition Fraction Fraction Fraction Fraction Gal/min Partition Fraction Fraction Feet Degree F Degree F Fraction Auto Manual Active Inactive Auto Manual Partition Fraction Dimensionless Partition Btu/sec-degF Lbm/sec Degree F Btu/lbm Fraction Lbm/sec Degree F Btu/ibm Partition Partition Fraction Fraction Psia Psia Psia Psia Psia Volts Volts Volts Auto Manual Partition Partition Psia Psia Auto Manual Partition Partition Psia Psia Psia Psia Auto Manual Partition Partition Psia Psid Psia Degree F Psia Partition Counts Gal/min Psia Counts Fraction Counts Gal/min



index V a r i a b I N a m e: No. Short Long

2072 CEPLPS CTLLPSIIPRES_TABLE 2073 CELNUM CTLLPSI_PUMPNUM 2074 CESLPS CTL.LPSISPLIT 2075 CETRPT CTL_SIASTIME 2076 CEDEL CTL_SISDELAY 2077 CEAUTO CTLSIAS_CONTROL_AUTO 2078 CETRP CTLSIASTRIP 2079 . CETRPP CTL_SIASPTRIP 2080 . CEKISC CTLSISFLOW 2081 . CEBHLP CTLSISHLPSIBC 2082 . CEHHLP CTLSISHLPSIH 2083 . CEBSIT CTLSISSITBC 2084 . CEHSIT CTLSISSITH 2085 CENSIT CTLSITNUM 2086 . CEELEV CTL.SITELEV_PRES 2087 CEFLCO CTLS ITFLOWCOEFF 2088 CECGAS CTLSITGASCONST 2089 CEPSIT CTLSITGASPRES 2090 . CEVGAS CTL_SITGASVOLUME 2091 . CEIVAL CTL_SIT_ISOVALVE 2092 CESLIQ CTLSITLIQSPVOL 2093 CEVLIQ CTLSITLIQVOLUME 2094 CSDCCN CTLSDCCONTROL 2095 . CSDCDH CTLSDCDH 2096 . CSDCHM CTL_SDC_H_MIN 2097 . CSDCSP CTLSDCSPLIT 2098 CTURB CTL_TURB_CONTROL 2099 CGSET CTLTURBSETPOINTS 2100 . CGTCLS CTkLTURB.TRIP_VALVE_TIME 2101 . . CGVTC CTLTURBAOUT_TC 2102 . CGTRPT CTLTURBTRIPTIME 2103 . CGFDEM CTLTURBDEMAND 2104 . CGGRAT CTLTURBSTEAMRATED 2105 CGCAUT CTLTURB_CONTROLJAUTO 2106 CGLOAD CTL_TURB_CONTROLLOAD 2107 CGTRP CTLTURBTRIP 2108 CGTAUT CTL_TURBTRIPAUTO 2109 CGTRPP CTLTURB_PTRIP 2110 CMSIS CTLMSISCONTROL 2111 CISET CTLMSI S_SETPOINTS 2112 . CIPSLO CTL_MSIS_SGPRES_TRIP 2113 . CIPCHI CTLMSJIS_CONTPRESS_TRIP 2114 . CIGSLO CTLMSISSGSLFLOWTRIP 2115 CIAUTO CTL_MSIS_CONTROL_AUTO 2116 CITRP CTL._MSIS_TRIP 2117 CDUMP CTLATMDUMPSCONTROL 2118 . CDSET CTLATMDUMP-SETPOINTS 2119 . . CDTSP CTLATM-DUMPSPOINT 2120 . CDAUTO CTLATMDUMPCONTROLAUTO 2121 CBYPAS CTLTURBBYPASSCONTROL 2122 . CBSET CTLTURBBYPASSSETPOINTS 2123 . CBPOPN CTLTURB-DUMPOPEN 2124 CBDELP CTL_TURB_DUMP_.DELP 2125 CBQOPN CTLTURBDUMPQOPEN 2126 . CBNOPN CTLTURBDUMP._NOPEN 2127 . CBQCLS CTLTURB-DUMP-OCLOSE 2128 . CBNCLS CTLTURB_DUMPNCLOSE 2129 CBMODE CTL_TURBDUMP_.ODE 2130 . CBAUTO CTL_TURBBYPASSCONTROL..AUTO 2131 CSAFE CTL_SG_SAFETIES 2132 CSSET CTLSGSVSETPOINTS 2133 . CSOPEN CTL_SGSV_PSETOPEN 2134 . CSFULL CTL_SGSV.PSETFULL 2135 . CSCLOS CTLSGSVPSETCLOSE 2136 . CSAOPN CTLSGSVASETOPEN 2137 CFWS CTLFWS_CONTROL 2138 . CFSET CTLFWSSETPOINTS 2139 . CFLPRG CTL_FWS_SGLEVELLOAD 2140 . CFLLO CTL_FWSSG_LEVEL_LOW 2141 . CFLHI CTLFWSSG_LEVELHIGH 2142 . CFRAMP CTLFWSTURBTRIPFRAC 2143 . CFDELA CTLFWS_TURBTRIPDELAY 2144 . CFGMAX CTL_FWSMAX_FLOW 2145 . CFSMUL CTLFWSSPEEDMULT

DimenD sions

RE 15 IN RE 8 RE RE LO LO LO RE 36 RE RE RE RE IN RE 4 RE 4 RE RE 4 RE 4 LO 4 RE 4 RE 4 RE 6 RE RE RE 4 RE 14 RE 7 RE RE RE RE RE LO LO LO LO LO RE 14 RE 10 RE RE RE 4 LO LO RE 6 RE 4 RE 2 LO RE 11 RE 10 RE RE RE RE RE RE RE LO RE 120 RE 120 RE 24 RE 24 RE 24 RE 24 RE 70 RE 15 RE 2 RE RE RE RE RE RE 4

Definition Units

Back press for LPSI flow-vs-press table Psia Number of operating LPSI pumps Counts LPSI flow split to injection points Fraction Time elapsed since SIAS Seconds SI pumps time delay after SIAS Seconds Flag: automatic control of SIAS Auto Manual Safety injection actuation signal Active Inactive SI signal at last time step True False Safety injection system flow variables Partition HPSI/LPSI flow boron concentration Parts/million HPSI/LPSI flow enthalpy Btu/Ibm SI tank flow boron concentration Parts/million SI tank flow enthalpy Btu/lbm Number of SI tanks Counts

'SI tank elevation heads Psid SI tank flow coefficients Composite Units

-SI tank gas constant Dimensionless SI tank gas pressures Psia

,SI tank gas volumes Ft^3 SI tank isolation valves Open Closed SI tank liquid specific volumes Ft^3/lbm SI tank liquid volumes Ft^3 Shutdown Cooling control variables Partition Shutdown Cooling enthalpy drop Btu/lhm Shutdown Cooling min return enthalpy Btu/lbrn SDC flow split to injection points Fraction Turbine controls Partition Turbine control setpoints Partition TAV full-range closing time on turb trip Seconds Turb admission valve time constant Seconds Time elapsed since turbine trip Seconds Turbine steam demand Fraction Rated turbine steam flow Lbm/sec Flag: automatic turbine control Auto Manual Flag to match st. demand with heat load Auto Manual Signal. turbine tripped Trip Normal Flag: automatic trip of turbine Auto Manual Turbine trip signal at last time step True False Main steam isolation signal controls Partition MSIS control setpoints Partition Low SG pressure MSIS trip setpoint Psia Containment pressure MSIS trip setpoint Psia High steamline flow MSIS trip setpoint Lbm/sec Flag- MSIS automatic control Auto Manual Main steam isolation signal Active Inactive Atmospheric dump valves controls Partition Przr ADVs setpoints Partition Atm. dump valves temperature setpoints Psia Flag: automatic ctrl of atm-dump valves Auto Manual Turbine bypass controls Partition Turbine bypass valves setpoints Partition Pressure to open bypass valves Psia Press. range of turb bypass ctrl system Psid Quick-opening time for turb bypass valve I/seconds Normal-open time for turb bypass valve 1/seconds Quick-close time for turb bypass valve 1/seconds Normal-close time for turb bypass valve I/seconds Bypass control mode: 0=p-temp, 1=s-pres Pointer Flag: automatic turbine-bypass control Auto Manual SG safety valves control variables Partition SG external safety valve setpoints Partition SG safeties design-open press. setpoints Psia SG safeties full-open pressure setpoints Psia SG safeties closing pressure setpoints Psia SG safeties design-open fraction Fraction Feedwater system controls Partition FWS control setpoints Partition SG level program load setpoints Fraction Main feedwater lo-level control setpoint Fraction Main feedwater hi-level control setpoint Fraction Main FW rampdown flow frac after trip Fraction Main FW rampdown time after turb trip Seconds Max feedwater flow to each SG Lbm/sec Multp on FW pump speed signl: =0 to trip Dimensionless



Index V a r i a b 1 e N a m e: No. Short Long

2146 . . CFTLO CTL_FWSTRIPSP 2147 . CFENTH CTL.FWS_H 2148 . CFEMAX CTLFWSJHMAX 2149 . CFETC CTLFWS_HTC 2150 . CFTRP CTLFWSTRIP 2151 CFAUT CTL_FWS_AUTO 2152 . . CFAUTO CT1_FWSCONTROLAUTO 2153 . . CFVAUT CTL.FWS-VALVEAUTO 2154 . . CFEAUT CTLFWS_ECON_VALVE.AUTO 2155 . . CFPAUT CTLFWSPUMPAUTO 2156 . . CFTAUT CTLFWSTRIPAUTO 2157 CFVSIG CTL FWSVALVELSIG 2158 . . CFVSI CTLFWSSIG 2159 . CFVESI CTL FWSECON-SIG 2160 CFVPOS CTLFWSVALVE._POS 2161 . CFVPO CTLFWSPOS 2162 . . . CFVEPO CTL_FWSECONrPOS 2163 CFSSIG CTLFWS_SPEED_SIG 2164 CFSFRC CTLFWS-SPEEDFRAC 2165 CFSMAX CTLFWSSPEED-MAX 2166 CFVISO CTLFWSIS0_POS 2167 CFVBYP CTLFWSBYPSIG 2168 CAFWS CTLAFWS_CONTROL 2169 . CASET CTLAFWS-SETPOINTS 2170 . . . CALLO CTLAFWSSGLEVELLOW 2171 . . . CALHI CTL AFWSSGLEVELJIIGH 2172 . CAGMAX CTLAFWSTOTFLOW 2173 CADPMI CTLAFWSSGDPJHIIGH 2174 . CADELA CTL.AFWSDELAY 2175 . CAFMUL CTL AFWSFLOW-MULT 2176 . CATURB CTLAFWSTURBPUMP 2177 . CAMOTR CTL._AFWSMOTOR-PUMP 2178 CAAUTO CTLAFWSCONTROLAUTO 2179 CASSIG CTLAFWSSPEEDSIG 2180 CRPCS CTLRPCSCONTROL 2181 . CQSET CTLRPCSSETPOINTS 2182 . CQAUTO CTLRPCS_CONTROL_AUTO 2183 . CQTRP CTLRPCSTRIP 2184 . CQTRPP CTLRPCSPTRIP 2185 . CQTRPT CTLRPCSTRIPTIME 2186 CGSCON CTLTURB.SETBACKCONTROL 2187 . CGSSET CTL_TURBSETBACKSETPOINTS 2188 . CGSAUT CTLTURB_.SETBACK_AUTO 2189 CGRAUT CTLTURBRUNBACKAUTO 2190 . CGSTRP CTLTURB_SETBACK_TRIP 2191 CGRTRP CTLTURB RUNBACK 2192 CSETPT CTLMISCSETPOINTS 2193 . SETT CTLSETTEMP 2194 . SETDT CTLSETDELTEMP 2195 SETDDT CTLSET_DELTEMPD 2196 SETP CTLSETPRES 2197 SETDP CTL_SET_PRESD 2198 . SETDM CTL_SETNODIM 2199 . SETW CTLSET_.FLOW 2200 . SETWD CTL_S ETFLOWD 2201 . SETRT CTLSETPERTIME 2202 CTIMCN CTLTIM-CONSTANTS 2203 COUT CTLOUTPUT 2204 COUTIN CTLOUTPUTINTERVAL 2205 COUTOP CTLOUTPUT-OPTION 2206 COUTCT CTLOUTPUTCOUNT 2207 COUTTI CTLOUTPUT_NTITLE 2208 COUTGR CTLGRAPHINTERVAL 2209 COUTFI CTLGRAPH_FILE 2210 COUTLO CTLOUTPUTLOOP 2211 COUTCL CTLOUTPUTOPCL 2212 COUT3D CTLOUTPUT.3DMAP 2213 CSPAR2 CTLSPARE2 2214 CBLOCK CTLTIMEBLOCK 2215 . DELT DELT 2216 . FDELT FDELT 2217 . TBASE TBASE 2218 . TIME TIME 2219 . . TSCALE TIME-SCALE

Di ci__

RE RE RE RE LO LO LO LO LO LO LO

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE LO RE RE RE RO RO RO RE RE RE RO LO LO RO RE RE RE RE RE RE RE RE RE RE RE RE IN IN IN IN IN

IN IN IN t0 RE RE RE RE RE RE RE

mn_ Lns Definition

Feedwater trip setpoint 2 Steady state FW enth: 1 at CST, 2 at SGS

Maximum feedwater enthalpy Feedwater enthalpy time constant FWS trip signal

14 Flags for automatic control of FW system Master FW flag: T=separate, F=all manual

4 Flags: auto control of downcmr FW valves 4 Flags: auto control of econmzr FW valves 4 Flags: auto control of main FW pumps

Flag: automatic main feedwater trip 4,2 Main FW valve demand signals 4 Main FW downcomer valve demand signal 4 Main FW economizer valve demand signal 4,2 Main FW valve positions 4 Main FW downcomer valve position 4 Main FW economizer valve position 4 Main FW pumps speed demand signals 4 Main FW pumps normalized speed, actual

Main FW pumps reference speed 4 Main FW isolation valve position 4 Main FW Bypass valve demand signal 25 Aux feed system controls 20 AFWS control setpoints 4 Low level setpoint for aux feed 4 High level setpoint for aux feed

Total aux-feed flow capacity, all SGs SO press.-difference to cutout aux. feed AFW time delay after trip

4 Multiplier on aux feedwater flow rate AFWS turb-driven pump switch: 0=off,l=ok AFWS motor-drivn pump switch: 0=offl=ok Flag: automatic control of aux feed

4 AFW pumps speed demand signals 15 Reactor power cutback system 5 RPCS setpoints

Flag: automatic RPCS control Signal. RPC engaged RPC signal at last time step Time elapsed since RP cutback engaged

20 Turbine setback and runback systems 10 Turb setback & runback system setpoints

Flag: automatic turbine setback control Flag: automatic turbine runback control Signal. turbine setback engaged Signal turbine runback engaged

200 Miscellaneous user-defined setpoints 20 Miscellaneous temperature setpoints 20 Miscellaneous delta-temp setpoints 20 Miscellaneous per-delta-temp setpoints 20 Miscellaneous pressure setpoints 20 Miscellaneous per-pressure setpoints 60 Miscellaneous dimensionless setpoints 10 Miscellaneous flowrate setpoints 10 Miscellaneous per-flowrate setpoints 20 Miscellaneous per-time setpoints 150 Miscellan. user-defined time constants 16 Output control partition

Output frequency for line output Line output option

4 Output counter: calls/line/graph/title Line output title frequency Output frequency for graphics output Suffix nn for graphics file graphnn dat

2 Select loops for std output & graphics Increment for 2nd cold leg in loop Flag to produce a 3-D power map

600 Not used 10 Time step control information for CENTS

Master time step variable Fast DELT used for scaled time operation Base time step (set to 1.0) Simulation time Time scaling ratio >1 is faster than rt

Units

Undefined Btu/lbm Btu/lbm Seconds Active Inactive Partition Auto Manual Auto Manual Auto Manual Auto Manual Auto Manual Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Shaft RPM Fraction Fraction Partition Partition Fraction Fraction Lbm/sec Paid Seconds Dimensionless Pointer Pointer Auto Manual Fraction Partition Partition Auto Manual Trip Normal Trip Normal Seconds Partition Undefined Auto Manual Auto Manual Trip Normal True False Undefined Degree F Del-degF Per-degF Psia Per-psia Dimensionless Lbm/sec Sec/Ibm 1/seconds Seconds Partition Counts Pointer Counts Counts Counts Pointer Dimensionless Dimensionless True False Unused Partition Seconds Seconds Seconds Seconds Per unit



index V a r i a b I a N a = a: No. Short Lon

2220 TSTOP TSTOP 2221 MODELQ MODELQUEUE 2222 TIMQUE TIMQUE 2223 . MODQUE MODQUE 2224 . FLGQUE FLGQUE 2225 CINCON CTLINITIALCONDITIONS 2226 . CTLUN CTLUNUSED 2227 . CLCONT CLCONT 2228 CSPARE CTLSPARE 2229 INIFLG INIT_FLAG 2230 CEINIT INITALL 2231 MODOFF INITOFFMODELS 2232 . RCSOFF INITOFFRCS 2233 . CHTOFF INITOFF-CHT 2234 . POWOFF INITOFF_POW 2235 . SGSOFF INITOFFSGS 2236 . CONOFF INITOFF_CCN 2237 CORINI INITCORE 2238 NINIT INITITER 2239 CLEVEL CTLILEVEL 2240 CLEVSG CTL_SG_ILEVEL 2241 CLEVP CTLPRZR_ILEVEL 2242 MODERR MODELERROR 2243 CONT CTL_CONTROLLER 2244 ELLAST ELLAST 2245 GROUT GROUT 2246 MALCTL MAL_CTL 2247 CDELAY CTL_DELAYS 2248 CDTRIP CTLCORETRIPDELAYS 2249 . . . CDPOHI CTL_CORE_HIPOWERFRACTRIP_DL 2250 CDSRHI CTL_CORE_H1IPOWERSURTRIP_DL 2251 . . . CDPPLO CTLCORE-LOWPRZRPRES..TRI PDL 2252 . CDPPHI CTLCORE_H.I_PRZRPRES_TRIP_DL 2253 . . CDLPHI CTLCORE..HIYPRZR_.LEVELTRIP_DL 2254 . . CDTMAR CTLCOREOVER..TEMP_.MRGN-TRIP_DL 2255 . CDWMAR CTL.COREOVERPOWERMRGNTRIPDL 2256 CDGRCS CTL_CORERCSFLOW.FRACTRIPDL 2257 CDSIAS CTLCORESIASTRIP_DL 2258 CDPSGL CTLCORELOWSGPRESTRIPDL 2259 CDLSGL CTL_CORELOW_SGLEVELTRIPDL 2260 CDLSGH CTL_COREHISGLEVELTRIP DL 2261 . CDGSGM CTL_STEAKFEED.MISMATCH_TRI PDL 2262 . CDPCHI CTL_COREHI-CONTPRES_TRIPDL 2263 . CDUSER CTL_CORE_USERDEFINEDTRIP_DL 2264 CDMIST CTLMISC-TRIPDELAYS 2265 . CDGTRP CTLTURBTRIP..DELAY 2266 . CDITRP CTLMSIS_.TRI P_DELAY 2267 . CDFTRP CTL_FWS_TRIPDELAY 2268 . CDQTRP CTLRPCSTRIPDELAY 2269 . CDGSTR CTLTURB-SETBACKTRIP_DELAY 2270 . CDGRTR CTLTURBRUNBACKDELAY 2271 . CDMISC CTL_MISCDELAYS 2272 USR USER_COMMON 2273 SDELAY SCRAM_DELAY 2274 MOISTC MSLHNO.MOISTURECARRY 2275 SGTIOP SGTINITOPTION 2276 WARNOP INTERPOLATIONERROR_.OPTION 2277 DBGSGI SGSDEBUGSGSINI 2278 DBGSGH SGS-DEBUGSGHEAT 2279 COREQA CTLCOREPOWERA 2280 SAREA3 SGSAREADOWNCOMER 2281 ALPHA3 SGS_ALPHA_DOWNCOMER 2282 V3MULT SGS-VEL31-YMULT 2283 SVEL31 SGS-STEAMVEL31 2284 RBAL RCSBALANCE 2285 RNODFL RCS_NODAL.EXT.FLOWS 2286 RTOTFL RCS_NETEXT_FLOW 2287 RTOTHR RCSNET_HEAT.RATE 2288 RTOTM RCSTOTALMASS 2289 RTOTE RCS_TOTALENERGY 2290 ITOTP IODINETOTALSPARTITION 2291 RITOT RCSTOTALIODINE 2292 SITOT SGSTOTALIODINE 2293 RIRELT RCSIODRELTOT

Dimeon

To sions Definition

RE RE 60 RE 20 IN 20 LO 20 RE 4 RE LO RE 200 LO 10 LO LO 7 LO LO LO LO LO LO IN RE 15 RE 4,3 RE IN RE 3000 RE 1000 RE 1000 LO 1000 RE 50 RE 30 RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE 10 RE 20 RE RE RE RE RE RE RE 10 RE 1024 RE RE RE RE RE RE RE RE 4 RE 4 RE 4 RE 4 RE 54 RE 50 RE RE RE RE RE 10 RE RE RE

Value of time at which to pause Model queue information Model queue - fraction of timestep Model queue - model number called Model queue - on/off flag Flags for initial conditions Not used Flag for including control routines Spare space Model initialization flag Initialization of all routines Off flags for initialization models Initialization of RCS: off flag Initialization of CHT: off flag Initialization of POW: off flag Initialization of SGS: off flag Initialization of CONT: off flag Flag to initialize the 3-D core model Number of initialization passes Instrument level readings for controls SG level readings (SG, refleg) Pressurizer level reading User-accessible flag for model errors Control module variables Saved "last values, of control elements Control group output signals Control group malfunction cues Partition for control system delays Scram channel delays Hi power fraction scram delay High power SUR scram delay Low przr pressure scram delay High przr pressure scram delay High przr level scram delays Over-temp thermal margin scram delay Over-power thermal margin scram delay Low loop flow scram delay Scram due to SIAS delay Low SG pressure scram delay Low SG level scram delay High SC level scram delay Steam-feed flow mismatch scram delay Hi containment pressure scram delay Space for other scram delays Miscellaneous control system delays Turbine trip signal delay Main steamline isolation signal delay Main feedwater trip signal delay Reactor Power Cutback signal delay Turbine Setback signal delay Turbine Runback delay Space for other control system delays User global common variables Total scram delay time after trip 1 => No moisture carryover 0 => Adjust area. I => Find SO press 1 => Warning after each interp error 1 => Debug print on-subroutine SGSINI 1 => Debug print on-subroutine SGHEAT 0 Core power Area of downcomer for bubble rise calc Downcomer steam volume fraction Downcomer multiplier on Wilson velocity Steam velocity downcomer to steam dome RCS mass and energy balance Sum of the external flows to each node Sum of all RCS flows - includes PRZR Sum of all heat flows to RCS Sum of all RCS nodal masses - inc PRZR Sum of all RCS node total energy Variables to check iodine release model Total iodine in RCS nodes Total iodine in stm Generators & header Total of core release & external flows

Units

Seconds Partition Fraction Dimensionless Active Inactive Partition Unused True False Unused Partition True False True False True False True False True False True False True False True False Counts Fraction Fraction Fraction Pointer Partition Undefined Undefined Malfunc Normal Partition Partition Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Seconds Partition Seconds Seconds Seconds Seconds Seconds Seconds Seconds Segment Seconds Dimensionless Dimensionless Dimensionless Dimensionless Dimensionless Megawatts Ft^2 Dimensionless Dimensionless Ft/sec Partition Lbm/sec Lbmf/sec Btu/sec Lbm Btu Partition Curies Curies Curies



Index V a r i a b l e N a m ei No. Short Long

2294 . RIRELR RCS_IOD_RELRATE 2295 MINMAX CTL_SUMMARYDATA 2296 MXPOW CTLMAXPOWER_FRAC 2297 MXPOWT CTLJ4AXPOWER_TIME 2298 MJOTFR CTLJMAXH.EATFLUX)FRAC 2299 . MHTT CTL_.MAX_HEATFLUX_TIME 2300 MXPPR CTLJMAXPRZR_PRESS 2301 MXPPRT CTLMAXPRZRPRESSS_TIME 2302 MNPPR CTL_MIN_PRZRPRESS 2303 MNPPRT CTLMINPRZRPRESSTIME 2304 MXRCSP CTLMAXRCSPRESS 2305 MXRPT CTLMAXRCSS_PRESSSTIME 2306 MNRCSP CTLJIN_RCSPRESS 2307 MNRPT CTL_MINIRCSSPRESS_TIME 2308 MXSGP CTLMAXSGPRESS 2309 MXSGPT CTLJAXSG_PRESS_TIME 2310 MNSGP CTL__MIN_SG_PRESS 2311 MNSGPT CTLMINSGPRESS_TIME 2312 INWRCS CTL_INTEG_PFLOWNONMOM 2313 INSGV CTL_INTEG_SGS_VALVES 2314 INSLBO CTL_JINTEGMSLB_INSFLOW 2315 INSLBI CTLINTEGCMSLBOUTFLOW 2316 CORWO CTL_INITIALCORE_FLOW 2317 CORWFR CTL_.CORE_FLOW_FRAC 2318 CORHFR CTL_HEATFLUXFRAC 2319 CTPMIN CTLCETOPMINDNBR 2320 CTPMNT CTLCETOP_MINDNBR_.TIME 2321 CETOPC CETOP..LINK 2322 . CTPOUT CETOP_OUT 2323 . . . CTP01 CETOPOUTCASE 2324 . . CTPO2 CETOPOUTQDBL 2325 . . CTP03 CETOP_OUT_POLR 2326 . . . CTP04 CETOPSOUTTIN 2327 . . . CTP05 CETOP_OUTPIN 2328 . . . CTPO6 CETOPOUT.GAVG 2329 . . . CTPO7 CETOPOUT._ASI 2330 . . . CTPO8 CETOP_OUTNRAD 2331 . . . CTPO9 CETOPOUT1_PMAX 2332 . . . CTPO0O CETOP_OUT.DNB-N 2333 . CTPO11 CETOP._OUT_X-N 2334 . . . CTPO12 CETOPOUTDNB-1 2335 CTP013 CETOP_OUT_X-1 2336 CTPO14 CETOPOUT_QUIX 2337 . . . CTPO15 CETOPOUT_ITER 2338 . . . CTPO16 CETOPOUT_IEND 2339 . . . CTPO17 CETOPOUTATR 2340 . . CTPO18 CETOCPOUTHCH 2341 . . . CTP019 CETOP_OUTMNOD 2342 CTPINP CETOP_.IN 2343 CTPI1 CETOP_IN_TIME 2344 CTPI2 CETOP_IN_FLOW_FRAC 2345 . . CTPI3 CETOP_IN_INLETTEMP 2346 . . CTPI4 CETOPI NCORE.PRESSURE 2347 . . . CTPI5 CETOP_IN._HEAT_FLUfFRAC 2348 . . . CTPI6 CETOP_IN_FR_USERULT 2349 . . . CTPI7 CETOP_INFR.TEMPJULT 2350 . . CTPLNK CETOPLINKICONTROL 2351 . . CTPC1 CETOP_.PRESS_OPT 2352 . CTPC2 CETOPJFRDERIV 2353 . CTPC3 CETOP_FR_PATH1 2354 . . . CTPC4 CETOP_FR_PATH2 2355 . CTPC5 CETOPJFRJTEMP1 2356 . . . CTPC6 CETOP_FR_TEMP2 2357 . . . CTPC7 CETOP_FRDEL_TEMP 2358 VBMISC VATTENFALL-MISCELLANEOUS 2359 INIOUT INIT_DEBUG_OUTPUT 2360 JUNKi JUNK1PARTITION 2361 . SLFLC SLFLOWCOEFF 2362 . DRATIO RATIO_CONCSOLU 2363 . RAUSER RCSLINPROP_USER 2364 RLNUP RCSJUCMLINPROP 2365 . RSSCON RCSSSSCONTROL 2366 . RSSUSE RCSSSUSER 2367 CDCONT CDCONTSCOMMON

Dimensions

150

4 4 4 4 50 50 8

TME

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE LO RE IN IN RE RE RE RE RE RE RE RE LO IN LO LO RE

Definition

Net rate of core release and ext flows Case summary data Maximum power fraction during run Time of maxLmum power during run Maximum heat flux during run Time of maximum heat flux during run Maximum Pressurizer Pressure during run Time of maximu= Przr Press during run Minimum Pressurizer Pressure during run Time of minimum Przr Press during run Maximum RCS Pressure during run Time of maximum RCS Press during run Minimum RCS Pressure during run Time of Minimum RCS Press during run Maximum SG Pressure during run Time of maximum SG Press during run Minimumm SG Pressure during run Time of minimum SG Press during run Integrated flow though all leak paths Integrated flow though secondary paths Integrated flow MSLB inside containment Integrated flow MSLB outside containment Initial core flow Normalized core flow - frac of initial Core average heat flux fraction CETOP Minimum DNBR Time of CETOP Minimum DNBR Partion to store CETOP link data

19 CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP

7 CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP

7 CETOP CETOP CETOP CETOP CETOP CETOP CETOP CETOP

200 Space

112 8 5

50

standard output out: Case number out: Heat flux out: Power operating limit out: Inlet temperature out: Pressure out: Core average mass velocity out: Axial shape index out: Peripheral Axial shape index out: Max radial avg peaking factor out: Min DNBR at final iteration out: Quality at final iteration out: Min DNBR at first iteration out: Quality at first iteration out: QUIX file case number out: Number of iterations out: Iter code: 1 => DNBR conv-d out: Avg enthalpy transport coeff out: Min DNBR hot channel number Out: Min DNBR node location Inputs from CENTS in: CENTS simulation time in: Normalized core flow in: Core inlet temperature in: Core pressure in- Heat flux fraction in: User input Fr multiplier in: FR temperature multiplier link variables and options link Constant pressure option link. Fr vs temperature derivative link: Path # for Templ link: Path # for Temp2 link: Templ for DT calc link: Temp2 for DT calc link: Temp Diff for Fr correction for Vattenfall use

I => Debug print on-subroutine INITIAL These variables are unused but in decks Unused Conc ratio - unused for vdict revl5 nu Linearization of props. user control nu Max steps to update lin. props. nu Flag t=RCSs called f= RCS called nu Control of RCSs or RCS (user) Container array for Cooldown Controllers

units

Microcurie/sec Partition Fraction Seconds Fraction Seconds PsLa Seconds Psia Seconds PsLa Seconds Psia Seconds Psia Seconds Psia Seconds Lhm Lbm Lbm Lhm

Lbm/sec Fraction Fraction Fraction Seconds Partition Partition Fraction MegBtu/hr- ft-2 Fraction Degree F PsLa 10e6 lb/hr-ft2 Ratio Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Fraction Composite Units Pointer Pointer Partition Seconds Fraction Degree F Psia Fraction Fraction Fraction Partition True False 1/Del-DegF Pointer Pointer Degree F Degree F Degree F Partition Dimensionless Unused Unused Dimensionless True False Counts True False True False Partition


50

G-223


Xndex Va riable Name: NO. Short Long

2368 2369 2370 2371 2372 2373 2374 2375 2376 2377 2378 2379 2380 2381 2382 2383 2384 2385 2386 2387 2388 2389 2390 2391 2392 2393 2394 2395 2396 2397 2398 2399 2400 2401 2402 2403 2404 2405 2406 2407 2408 2409 2410 2411 2412 2413 2414 2415 2416 2417 2418 2419 2420 2421 2422 2423 2424 2425 2426 2427 2428 2429 2430 2431 2432 2433 2434 2435 2436 2437 2438 2439 2440 2441

Dimen

TU sion__

SGTDBP DBG_SGTRPARTITION SGTDBl DBGSGTRFLOW1 SGTDB2 DBGSGTRJFLOW2 SGTDB3 DBGSGTR&FLOW..SLOr SGTDB4 DBG SGTRPRESSPRI1 SGTDB5 DBGSGTR-PRESS-PRI2 SGTDB6 DBGCSGTRIPRESSSG SGTDB7 DBGCSGTR.PRESSITER SGTDB8 DBGSGTRSVOLkTUBEI SGTDB9 DBGCSGTR.SVOLSTUBE2

FWSCOM FWSCOMMON FDPATH FWSJFDPATH

FDPEL FWSSDPEL FCV FWSCV FRESL FWS-RESL FRHOFD FWSRHOFD FPEXT FWSPEXT FWMAS FWSMAS FWSWO FWSJWO FWSW FWSW FHPATH FWSJHPATH FQCURR FWSQCURR FRESV FWSRESV FRES FWSRES FHEXT FWSJHEXT FRHOEX FWSyRHOEXT FWSRP FWSRP FWSPS FWSPS FSUMP FWSSUMP FGPMCO FWSGPMCOR FNDIN FWSNDIN FNDOUT FWSJIDOUT FNDEXT FWSNDEXT FNCPMP FWSyNCPUMP FICPMP FWSICPUMP FWSICK FWSICK FWSIMF FWSIMF FPOISO FWSPOSISO FCVAFL FWSSCVAFLO FCVRES FWSCVRESMN FCVDPM FWSCVDPMIN FNFLO FWSNFLO FWSKEY FWSJCEY

FDNODE FWS-FDNODE FPEXTN FWSJPEXTN FHEXTN FWSJHEXTN FWSPO FWSPO FWSP FWSP FHNODE FWSJ1NODE FRHOND FWSRHONOD FWEXTF FWSWEXTF FHEXTF FWSJHEXTF FAEXTF FWS_AEXTF FPEXTF FWSPEXTF FWSUM FWS_WSUM FIMN FWS_IMN FNNOD FWSJNNOD FNEXTN FWSJNEXTN FNPSGM FWSJNPSGMFW FNPSGE FWS.NPSGECO FNPSGA FWSJJPSGAFW

* FNPFLB FWSSNPFWLB FWAFLB FWSAFWLB FNPPRV FWSSNPMFPRV

• FNSG FWSJNSG FDVALV FWSFDVALV

FSTROK FWSSTROKE FPOSIT FWSPOSIT FCVV FWSSCVV FTOPN FWSTOPN FTCLOS FWSJTCLOS FTLAG FWS.TLAG FCVP FWSCVP FSTP FWSSTP

RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE RE IN IN IN IN IN IN IN RE RE RE RE IN IN RE RE RE RE RE RE RE RE RE RE RE RE IN IN IN IN IN IN IN RE IN IN RE RE RE RE RE RE RE RE RE

36 4 4 4 4 4 4 4 4 4 20000 1600 50 50 50 50 50 50

50 50 50 50 50 50 50 50 50 50 so 50 50 50 50 50 50 50 50 50 50 50

400 20 20

30 30 30 30 30 30 30 30 30

4 4 4 4 4 4

1000 30 30 30 30 30 30 200 200

Definition

SGTR Debug Variables Debug Var SGTR Flow side 1 Debug Var SGTR Flow side 2 Debug Var SGTR Slot Flow Debug Var SGTR Primary press side 1 Debug Var SGTR Primary press side 2 Debug Var SGTR Secondary press Debug Var SGTR Slot pressure Debug Var SGTR Tube 1 Specific Volume Debug Var SGTR Tube 2 Specific Volume Feedwater System model segment FWS model flow path partition FWS model flow path elev gain ext path FWS model flow path flow coeff. FWS model flow path flow resistnce FWS model flow path density FWS model flow path external pressure FWS model flow path mass flow rate FWS model flow path volumetric flow FWS model flow path volumetric flow FWS model flow path flow enthaly FWS model flow path heat transfer FWS model flow path valve flow resist FWS model flow path total resistance FWS model flow path ext node enthalpy FWS model flow path ext node density FWS model flow path pump resistance FWS model flow path pump head FWS model flow path pressure error FWS model flow path density correction FWS model flow path input node ID FWS model flow path output node ID FWS model flow path external node ID FWS model flow path pump ID FWS model flow path pump status FWS model flow path check valve flag FWS model flow path calculation flag FWS model path isolation valve pos FWS model path check valve flow area FWS model path chk val flow resist. FWS model path chk val minimum DP FWS model network number of paths FWS model any fw pumps on flag FWS model node partition FWS model external node pressure FWS model external node enthalpy FWS model node pressure FWS model node pressure FWS model node enthalpy FWS model node density FWS model node external leak flow out FWS model node ext leak flow enthalpy FWS model node ext leak flow area FWS model node ext leak flow back press. FWS model node flow error FWS model node network masking flag FWS model network number of nodes FWS model network number of ext. nodes FWS model SC main fw path ID FWS model SG economizer fw path ID FWS model SG emergency/aux fw path ID FWS model MFWLB path ID FWS model MFWLB flow area (local) FWS model (not used) FWS model number of SG (local) FWS model valve partition FWS model valve demand (per cent) FWS model valve position FWS model valve flow coefficient FWS model valve stroke open time FWS model valve stroke close time FWS model valve actuator lag FWS model valve CV vs Position FWS model valve position vs. CV


Units

Partition Lbm/sec Lbm/sec Lbm/sec Psia Psia Psia Psia Ft^3/lbm Ft^3 /lbm Segment Partition Feet Composite Units Composite Units Lbm/Ft^3 Psia Lbs/sec Gal/min Gal/min Btu/lbm Btu/sec Composite Units Composite Units Btu/lbm Lbm/Ft^3 Composite Units Psid Psid Composite Units Pointer Pointer Pointer Pointer Pointer Pointer Pointer Fraction Fraction Composite Units Psid Counts Pointer Partition Psia Btu/lbm Psia Psia Btullbm Lbs/Ft^3 Lbm/sec Btu/ lbs Ft^2 Psia Lbm/sec Pointer Counts Counts Pointer Pointer Pointer Pointer Ft^2 Pointer Pointer Partition Percent Percent Composite Units Seconds Seconds Seconds Composite Units Fraction

G-224


Index V a r i a b I N a m e: No. Short Long

2442 FNPATH FWSNPATH 2443 FNTABL FWSJJTABLE 2444 FNPTV FWSNPTV 2445 FINDXF FWSINDEXF 2446 FNVMFV FWS_NVMFV 2447 FNVBFV FWSNVBFV 2448 FNVAL FWSVAL 2449 FNHDV FWSJNHDV 2450 FNVHDV FWSNVHDV

2451 FNAFVT FWStNAFWVT 2452 FNAFV1 FWSNVAFWl 2453 FNTAFV FWS_NTABFV 2454 FDPUMP FWSFDPUMP 2455 FSPDMD FWS_SPDMD 2456 FSPEED FWSSPEED 2457 FTAUON FWSTAUON 2458 FTAUOF FWSTAUOFF 2459 FWSHT FWS{HT 2460 FWSWT FWSWT 2461 FBTABL FWSBTABLE 2462 FATABL FWSATABLE 2463 FNPMTH FWSNPMPTH 2464 FNTABP FWS_NTABP 2465 FNPTP FWSNPTP 2466 FNPMPM FWSNPMPMFW 2467 FNPMPE FWSNPMPEFW 2468 FNPTMP FWSNPTHMFP 2469 FNPUM FWSNPUM 2470 FNTBFP FWS NTABFP 2471 FNMFWP FWS_NMFWP 2472 FNEFWP FWS-NEFWP 2473 FDHEAT FWS_FDHEAT 2474 . FTPWR FWSTPWR 2475 FTQLAG FWSTQLAG 2476 FHTRHV FWSHTRHOV 2477 FPWRTB FWSPWRTBL 2478 FQPTBL FWSQPTBL 2479 FHTHMX FWSHTRHMX 2480 FTPOWR FWS_TPOWR 2481 FTWHDP FWS_TWHDfP 2482 FTEMDP FWS_TENHDP 2483 FMAXTU FWS4MAXTAU 2484 FFDPSO FWSFDPOSO 2485 . FHFWBI FWSJHFWBIAS 2486 . FNPHET FWSNPHEAT 2487 . FNHTBL FWSNHTBL 2488 FWSNHT FWSJNHT 2489 . FNHDPT FWSNHDPTBL 2490 FDMODL FWSSFDMODL 2491 . FWSNRC FWSNRCIRC 2492 FWRCPB FWSFWRCPB 2493 . FWRCRE FWSJFWRCRE 2494 . FWRCSP FWS_FWRCSP 2495 FWRCIR FWSSFWRCIR 2496 FWRCOT FWSFWRCOUT 2497 FWRCIN FWSFWRCINT 2498 FNPTRC FWS_NPTHRC 2499 FNVLRC FWS_NVALRC 2500 FNPMRC FWSNPMPRC 2501 FIAURC FWS_IAUTORC 2502 FTIMET FWSSTIMET 2503 FITRIP FWSIFTRIP 2504 FITRPO FWSIFTRPO 2505 FDCLMS FWSDCLMASSES 2506 FECLMS FWSSECLJASSES 2507 SGAFWS AFWS_FLOW 2508 FWLMSS FWSLINEJASSES 2509 FDSYST FWSFDSYST 2510 NONC NONCOND_COMMON 2511 . NONC01 RCSSPECIESCONSTANTS 2512 . . NONC02 NUISOLUTES 2513 . . NONC03 HALF_LIFESOLUTES 2514 . . CRATIO CONCRATIOSTMLIQ 2515 . NONC05 CONCMAX


Dimen

Type sions Definition

30 FWS model valve path location ID 30 FWS model valve CV table ID 10 FWS model valve CV table no. of pts. 30 FWS model valve CV table index 4 FWS model Main Feed Valve ID 4 FWS model Bypass Feed Valve ID

FWS model number of valves FWS model number of Htr Drn valves

3 FWS model heater drain valve ID FWS model total number of AFW valves FWS model AFW valve 1 ID FWS model number of fw valve tables

1200 FWS model pump partition 20 FWS model pump speed demand (frac) 20 FWS model pump speed (frac) 20 FWS model pump speed lag (increasing) 20 FWS model pump speed lag (decreasing) 200 FWS model pump head vs flow tables 200 FWS model pump flow vs head tables 200 FWS model pump BTABLE vs flow 200 FWS model pump ATABLE vs flow 20 FWS model pump path ID 20 FWS model pump perf. table ID 10 FWS model pump table no. of pts. 4 FWS model pump MFP ID 4 FWS model pump AFW/EFW pump ID 4 FWS model pump MFP path ID

FWS model number of pumps FWS model number of fw pump tables FWS model number of mfw pumps FWS model number of efw pumps

500 FWS model fw heater partition FWS model turbine power

9 FWS model fw heater heat xfer tau 9 FWS model fw heater thermal mass 90 FWS model fw heater turb pwr vs Q 90 FWS model fw heater Q vs turb pwr 90 FWS model fw heater max enthalpy 10 FWS model fw Htr Drn turb pwr table 10 FWS model fw Htr Drn flow vs turb pwr 10 FWS model fw Htr Drn enth vs turb pwr 9 FWS model fw heater max tau 9 FWS model fw heater table index

FWS model fw enth bias to tune fw enth 9 FWS model fw heater path location ID 9 FWS model fw heater table no. of pts.

FWS model number of fw heaters FWS model fw htr drn table no. of pts.

288 FWS model fw model misc controls FWS model no. of recirc flow cntrls

20 FWS model pump recirc control PB 20 FWS model pump recirc control reset 20 FWS model pump recirc control setpt 20 FWS model pump recirc cntrl instr range 20 FWS model pump recirc control output 20 FWS model pump recirc control integral 20 FWS model pump recirc cntrl path ID 20 FWS model pump recirc cntrl valve ID 20 FWS model pump recirc cntrl pump ID 20 FWS model pump recirc cntrl auto flag 20 FWS model pump trip timer 20 FWS model pump current trip state 20 FWS model pump previous trip state 4 FWS model downcomer line mass 4 FWS model economizer line mass 4 Auxiliary feedwater flow rate 4,2 FWS steady state feed line mass 10000 FWS model fw system eqn partition 9000 Species and noncondensibles transport 61 Species Constants Partition

# dissolved solutes excl nc, SO+NC <= 20 20 Decay half lives of dissolved species 20 Conc ratio st,liq: Cs/(Cs+Cl) [0.0,1.0] 20 Maximum conc of species (LBM/LBPPM....)

Units

Pointer Pointer Counts Pointer Pointer Pointer Counts Counts Pointer Counts Pointer Counts Partition Fraction Fraction Seconds Seconds Feet Gal/mran Composite Units Composite Units Pointer Pointer Counts Pointer Pointer Pointer Counts Counts Counts Counts Partition Fraction Seconds Lbm Percent Btu/sec Btu/ibm Percent Lbm/sec Btu/lbm Seconds Pointer Btu/lbm Pointer Counts Counts Counts Partition Counts Percent Seconds Gal/min Gallons Fraction Fraction Pointer Pointer Pointer Pointer Seconds Pointer Pointer Lbm Lbm Lhin/sec Lbm Partition Segment Partition Counts Seconds Fraction Composite Units

G-225


index V a r i a b I a N a m e: No. Short

DimenM sions

2516 2517 2518 2519 2520 2521 2522 2523 2524 2525 2526 2527 2528 2529 2530 2531 2532 2533 2534 2535 2536 2537 2538 2539 2540 2541 2542 2543 2544 2545 2546 2547 2548 2549 2550 2551 2552 2553 2554 2555 2556 2557 2558 2559 2560 2561 2562 2563 2564 2565 2566 2567 2568 2569 2570 2571 2572 2573 2574 2575 2576 2577 2578 2579 2580 2581 2582 2583

NONC06 IDTYPESPECIES . NONC07 IDTYPESOLUTE

. NONC08 ID-TYPE-BORON

. NONC09 ID_TYPEN16

. * NONCIO ID-TYPE-IODINE

. NONCI1 IDTYPEXENON NONC12 IDTYPEPART

NONC13 IDTYPENONC . NONC14 IDTYPEHYD . NONCI5 ID-TYPE-NIT . NON15A IDTYPEAIR

NONC16 RCSNONCONDCONSTANTS NONC17 NUMNONC NONC18 NONCKDISSOLVE NONCI9 NONC.MW NONC20 COREN16_KULT NONC21 COND-NONC-FRAC NONC22 CONDNONCDEG_MULT DPGASP RCSPRZRSPRGASENTR

NONC31 RCSSPECIESNODES * NONC32 MASS-NONCDIS * NONC33 MASS.NONCDISTOT

* NONC35 RCS-CONCSOLUTE * NONC36 RCS..CULMSOLU

NONC37 RCSNONCOND-NODES NONC38 MASSNONCSEP NONC39 MASS.NONC.SEPTOT NONC41 QUALNONCSEP NONC42 QUAL.NONC.SEP-TOT NONC45 RCSCUM-NONC NONC46 CONDNONC NONC47 PPRES-NONC NONC48 PPRESNONC.TOT NONC49 PPRES-STM NONC51 PVOL.NONCTOT NONC52 TEMPNONC PPSLST PRESSSTM-LAST NONC54 PTEMPSTMSAT

NONC57 RCSSPECIESPATHS . NONC58 PCONC.SOLU NONC59 RCSNONCONDPATHS . NONC60 PFLOWNONC

. NONC61 PFLOWNONCMOM

. NONC62 P_FLOW_NONCNONM NONC65 PFRACNONC NONC66 PFRACNONCTOT NONC40 MASS-NONC-SEPRCS NONC50 FLOWDPMAXERR NONSOA FLOW_DP_NODEMAX.ERR NON50B FLOWDPPRINTNODE RLMGAS MASSNONCRCS PZQEFF RCSPRZRQEFF PZQCND RCSPRZR.QCOND NONC34 MASS-NONC-DIS-RCS NONC55 RCS.SPECIESCORE

. NONC56 CORE.RELESOLU NONC67 RCSNONCONDINTERF

NONC68 PFLOWAUXSPNONC NONCSI SISRCSNONC . NONC72 SISILRCSNONC

.. . NONC73 SIS2_RCS_NONC . . NONC74 SIS3_RCSNONC . NONC75 SIS4_RCSNONC . NONC76 SIS5_RCS_NONC . NONC77 SIS6_RCSNONC

NONC78 GSVESNONC NONC79 GSPRZRNONC NONC8O GS-SPECIES

IN 20 IN 15 IN IN IN IN IN IN 5 IN IN IN RE 65 IN RE 5 RE 5 RE RE 2 RE 5( RE RE 2: RE 51 RE 5) RE 5( RE 5( RE 1 RE 5{ RE 5S RE 5{ RE 5S RE 5S RE 5' RE 5S RE 5S RE 5S RE 5S RE 5 RE 5 RE 5 RE 3 RE 1 RE 1 RE 1 RE I RE 5 RE 1 RE 1 RE RE IN IN RE RE RE RE RE 2 RE 2 RE 3 RE 5 RE 6 RE 5 RE 5 RE 5 RE 5 RE 5 RE 5 RE RE IN

0 0 8

,5

0 5

Definition

Identifying pointers for the species Identifying pointers for the solutes Identifying pointer for boron Identifying pointer for N-16 Identifying pointer for iodine Identifying pointer for xenon Identifying pointer for particulates Identifying pointers for the nonconds Identifying pointer for hydrogen Identifying pointer for nitrogen Identifying pointer for air Noncondensibles constants Partition No. of noncondensible species, NC -= 5 NC dissolution const, lb/sec-ft2-delconc Molecular weights of non-condensibles Production constant for N-16 Noncond frac: l=full cond, 2=no condens Condens degrad at initl inflow of n/cs Const for gas entrainment in sprays Node species state Nodal mass of dissolved noncondensibles Nodal mass of dissolved noncondensibles Node concentrations of dissolved species Node solute accum rate prod+flow+disslv Node noncondensibles state Mass of separ-noncond in node Total mass of separ-noncond in node Quality of separ-noncond in nodal steam Quality of separ-noncond in nodal steam Node separ-nonc accum rates: flow+bubble Node rates of noncondensble dissolution Partial pressures of separ-nonconds Sum of partial pressures of sep-noncond Node steam partial pressures Total volume of separated non-cond gas Temperature of non-condensibles in node Last Nodal Pressure - does not inc gas Steam saturation temp at the partial pr Path species state Path concentrations of dissolved species Path noncondensibles state Path flows of all separ-nonconds Mom path flows of all separ-nonconds Non-mom path flows of all sep-nonconds Path concentrations of separ-noncond Path concentrations of separ-noncond Total mass of separ-nonconds in RCS Max error predicted - calculated press Node of max error FLOW_DPMAX Print DP data for this node (for debug) RCS noncond tot mass (separ & dissolved) Przr condens efficiency when n/c present Przr condens heat transfer Total mass of dissolved nonconds in RCS Core node species Solute release rate in core (production) Noncondensible interfaces partition Auxiliary spray noncondensibles flow Noncond inflow via SI lines Noncond inflow via SI line, CL 1 Noncond inflow via SI line, CL 2 Noncond inflow via SI line, CL 3 Noncond inflow via SI line, CL 4 Noncond inflow via SI line, HL 1 Noncond inflow via SI line, HL 2 Noncond inflow to vessel via Gas System Noncond inflow to przr via Gas System Species of Gas Sys gas (from IDTYPESP


0

300 0,5 0

0,20 0,20 450 015 0 0.5 0 0,5

0 005 0 0 0 0 0 0 000

50,20 080 so 00

0 50,5 50

Units

Partition Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Pointer Partition Counts Composite Units Composite Units Composite Units Fraction Dimensionless Dimensionless Partition Lbm Lbm Composite Units Composite Units Partition Lbm Lbm Fraction Fraction Lhnm/sec Lbm/sec Psia Psia Psia Ft^3 Degree F Psia Degree F Partition Composite Units Partition Lbm/sec Lbh/sec Lbsn/sec Fraction Fraction Lbm Psid Pointer Pointer LbM Fraction Btu/sec Lbm Partition Composite Units Partition Lbs/sec Lbm/sec Lbm/sec Lbm/sec Lbs/sec Lbm/sec Lbm/sec Lbm/sec Lbm/s ec Lbm/sec Pointer

G-226

Index

1056

1786

2507

1785

213

198

86

1191

1193

1192

1190

399

440

461

382

383

384

426

427

438

823

824

825

237

235

241

239

1043

1048

212

238

236

242

240

2367

203

2357

2352

2353

2354

2355

2356

2342

2346

2344

2349

2348

2347

Long Vari

ADMI_HEA

AFWS_ENTI

AFWS_FLO

AFWSNOZ

AREABLEE

AREACORI

AREA_INJ_

AREAVAL%

AREAVAL'

AREAVAL'

AREAVALU

ASEP._SG

ASL_MAX

ASIMIN

ASP_TBL

ASP.TBLDS

ASPTBL DS

ATUBES_M.

ATUBESM

ATUBES_MA

AXPDINPU

AXPDNUM

AXPDPRINI

BAD

BAN

BAR

BAT

BORONCOF

BOUYANCY_

BURNOUT_

BVD

BVN

BVR

BVT

CDCONTCO

CEASDIST

CETOP._FRD

CETOP._FRD

CETOP.FR_P

CETOP_FR_P

CETOP_FR_T

CETOP._FRT

CETOP_IN

CETOP..INC

CETOP_IN_Fl

CETOP_IN_Fl

CETOP_IN_F

CETOP._IN_H

Table G.3: Alphabetized Index of Lone Variable Names able Name Index Lone Variable I [ER 2345 CETOP_IN_INLET_ H 2343 CETOPIN_TIME W 2321 CETOP_LINK FLOW 2350 CETOPLINKCOI

ED_MIN 2322 CETOP._OUT E 2329 CETOP._OUTASI MULT 2339 CETOPOUTATR VE_PRZR 2323 CETOPOUTCASi VEQT 2334 CETOPOUTDNB VE_SPRAY 2332 CETOPOUTDNB VEUHEAD 2328 CETOPOUTIGAV

2340 CETOPOUTHCH

2338 CETOPJUTIEND

2337 CETOP_OUTJITER

2341 CETOPOUTMNO SGN 1 2330 CETOP_OUTNRA] SGN2 2331 CETOPOUTPIM, AXCS 2327 CETOP_OUTPIN AXHT 2325 CETOPOUTPOLI AXEC_HT 2324 CETOPOUT QDB] TOPT 2336 CETOPOULTQULD

POINTS 2326 CETOPOUT_TIN TNORMALIZATION 2335 CETOPOUT)_X-1

2333 CETOP..OUTX-N

2351 CETOP.PRESSOF

661 CFIiRCSAXIAL_

1423 CHGSASPRAY_F1 RE 1418 CHGSjRCSBOROI _CORE 1417 CHGSRCSENTH HEATER 1416 CHGS RCSFLOW

1419 CHGS RCSHYD

1420 CHGSRCSIOD

1421 CHGSRCSPART

1422 CHGSRCS-XEN 3MMON I CHR.COMMON

643 CHT_AVG_HEAT_ )EL_TEMP 664 CHT_AXIALDAT? )ERIV 652 CHTAXIALDATV 'ATHI 646 CHTAXIALDATA 'ATH2 645 CHTAXIALOUTF EMPI 634 CHTBOILING EMP2 600 CHTCHF_MULT

589 CHTCOMMON OREPRESSURE 597 CHTCONDFUEL LOWFRAC 669 CH-ITCONDROD

RTEMPMULT 627 CHTCONDLSAT_S RUSERMULT 626 CHT_CONDSTM EAT_FLUX_FRAC 625 CHTCONDWAT


Name

TEMP

ITROL

E

-_

-N

G

D D

AX

L

r

-w N

FLUX

•_ALL

_BO

_FC UT

_MULT

TM

I

G-227

Table G.3: Alphabetized Index of Lon Variable Names

Index

601

1249

1252

614

615

617

616

621

619

620

618

665

609

608

610

1250

641

653

635

650

603

1251

654

598

673

1243

1244

662

663

670

659

655

649

639

658

640

656

590

642

672

604

606

591

16

605

630

629

628

Lom! Variable Name

CHT-CONSTý-LEV

CHT-DELT

CHTý-DELTA-T

CHTý-DHFý-DP

CHTýDHGLDP

CHTI-DTSAT-DH

CHTI-DTSAT-DP

CH-1ý-DVSATG-DH

CHT-DVSATG-DP

CHTI-DVSATI-DH

CHT-DVSATL-DP

CHTENTH-COOL

CHT-ENTýLSAT-LIQ

CHT-ENTH-SAT-LIQ-MI

CHTý-ENTH-SAT-STM

Cfrfý-FDELT

CHT-FLASH-RATIý-LAST

CHTý-FLOW-STM-BO

CHT-FLUXSRIT

CHTý-FIX-DNB

CHT-ýFRAC-HT-GEN

CHIý-FTIME

CHIIGAP-COND

CHT-GAP-HCAP

CHTý-H-CORE-SECT

CHT-H-SUPER.MULT

CHTI-HEATI-FRAC

CHT-HEAT-LIQ

CHT-HEAT-STM

CHT-HTSAP-ROD

CHTý-HT-FLUX

CHTý-HT-GEN-ZR-WAT

Cfflý-HTCOFý-FB

Cfflý-HTCOFý-NB

CHT-HTCOFý-ST

CHT-HTCOFý-SUB

CHT-HiT

CHT-INPUTS

CH-Iý-LEVIMIX-LAST

Cffrý-M-COREýSECT

CHT-ýNNOQ-BO

Cffý-NNODLFC

CHT-NREGIONS-RAD

CKII-NUM-LINPROP

CHT-NUM-NODE

CFrrý_PRAN-SA7j-STM

CHT2RAN-STM

GIT-PRAN-WAT

Index

599

607

647

667

671

632

657

631

633

611

612

1398

1397

666

638

648

644

651

668

613

660

636

1267

637

1248

17

674

624

623

622

2227

2515

2514

1112

902

905

904

2546

2533

2532

903

901

1475

1847

1925

328

1148

196

Lone Variable Name

CHTý-PRESS-SUPERCRIT

CWIý-PROPERTIES

CHT-QUAL

CHTý.ROP-RADIAL

CHTI-SECTIONS-OUTPUT

CHT-SPECý-HTý-SAT-STM

Cfflý-SPEC-HT-STM

CHT-SPEQ-HTýWAT

CMý-STATE

CK-SVOI-SAT-LIQ

CFM-SVOLSA'Iý.STM

CK-SVOLCOOLýAV

CHT-TCOOL-AV

CHTJEMPý-COOL

CHTý-TEMP-CRIT

CHTJEMPý-CROSS

CfIT-TEMPffLJELAV

CHT-TEW-NB-ýM

CHTffEW-ROD

Cfffý-TEMPý-SAT

CK-TEW-SURF

Cfrfý-TERM

CHT-TERM-MAX

CHTý-TERM2

CHTý-TIMEýSCALE

CHT-TIME-STP-NUM

CHT-USILNEWý-ENTHALPY-OPnON

CffZ-VISCOS-SAT-STM

CHT-VISCOS-STM

CtrZ-VISCOS-WAT

CLCONT

CONC-MAX

CONC-RATICLSTM-LIQ

CONC-SOLU-QT

COND-BOIL

COND-BUB

CONDJNJ

COND-NONC

COND-NONC-DEG-MULT

CONP-NONQ-FRAC

COND-SURF

CONDLTDT

CONT-PRES

CONT-SGffEMP

CONTROL-COMMON

CONV-GPM-AREA

COREýBORON-ýREL

CORE.BOT


Table G.3: Alphabetized Index of Long Variable NamesIndex

596

594

1149

1150

2531

1151

592

15

2571

1187

197

1152

2168

2178

522

2174

2175

2177

2169

2171

2170

2173

2179

2172

2176

550

2117

2120

551

552

2118

2119

1993

1991

1978

523

1982

1985

1986

1987

1992

1988

1979

1989

1994

1990

1981

1980

Long Variable Name

CORE.Irrý-AREA CORE-HYD--DIA CORIý-HYDLREL

COREJODLREL COREýNMý-MULT CORE.PARTý-REL COREýRADý-OUT COREýRAD-OUT-DUMMY CORELRELEýSOLU COREýSURfý-AREA-LAST CORIý-TOP CORE-XEN-REL

MýAFWS-CONTROL Crl-AFWS-CONTROL-AUTO CrL.AFWS-CONTROLLERS CTL-AFWS-DELAY CTL-AFWSý-FLOW-MULT CTLýAFWS-MOTOR-PUMP CTIýAFWS-SETPOINTS CTI-AFWS-SQ-LEVEI-HIGH CrL-AFWS-SG-LEVEILOW CTIýAFWS-SGDPý-HIGH CTI-AFWS-SPEEDLSIG MýAFWS-TOTý-FLOW CrL.AMSý-TURB2UMP CR-AFWSý-VALVESONTROLLERS CrL-ATM-DUMFý-CONTROL CTI.ATM-DUMFý-CONTROL,-AUTU CTIýATM-DUMPý-NUM CTLý-ATM-DUMFý-PATH CTLýATM-DUMFý-SETPOINTS CrL-ATM-DUMFý-SPOINT

CM-CEA-ACCUM CrL,-CEA-AUTO CTIýCEA-COMMON CrL.CEA-CONTROLLER MýCEA-GAIN-EXP

CTLýCEA-LASIIJWE CTIýCEA-MAX CrL-CEA-MIN CTI.-CEA-PERFECr CTIýCEA-POS

CTL-CEA-SETPOINTS CTLýCEA-SPEED CM.CEA-SPEED-LAST CrL.CEA-STEP CTL-CEA-TREF-FULL

CT1ýCEA-TREfý-NO

Index

1983

1984

2319

2320

2029

2031

2017

2016

2018

2009

2030

2004

524

2021

2022

574

2243

521

1927

1974

2317

1943

2262

1966

1929

2249

1952

1946

1930

2250

1953

1933

2253

1956

1932

2252

1955

1940

2260

1963

1931

2251

1954

1939

2259

1962

1938

2258

Long Variable Name

CTIýCEA-TURBLQ-GAIN M.CEAPOSMON-FRAC

CTI,-CETOPý-MUq-DNBR CIICETOPý-MUq-DNBR-TIME CTI-CULFLOW CTIýCH-H CTIýCH-PUMFý-AUTO

C71ý07LPUW-FRAC CILSH-PUMFý-ON CTIýCH-PUW-W-RATED CTIýCH-T CTIýCHARGING-SETPOINTS CrLýCHGSSONTROLLERS CTI-CHV-FRAC CTL-CHV-RAREA CTIý.CONSTS CTI-CONTROLLER CTI-CONTROLLER-NUMBERS CTIýCORý-CONTROL CII-COREýCONTROL-AUTO CTICOREýFLOW-FRAC CTIý-CORE-HLCONT-PRES-TRIP Crl.-CORE.HLCONIý-PRES-TRTý-DL CTICORE-HLCONT - PRES-TRTý-OR CTLý-CORELHLPOWER-FRAC-TRIP C'rl.COREý-HLPOWER.FRACý-TRIPý-DL CTICOREýHL-POWER-FRAC-T-RIFý-OR Crl,-CORE.HLPOWER-SUR.BYPS CrlCORE.-HI-POWER-SUR-TRIP CrL.CORE.HLPOWER-SUR-TRUý-DL CrlýCORE-HL.POWER-SUR-TRTý-OR M1,CORIý-HURM-LEVE1ý7RIP CTIýCOREý-HLPRZR-LEVEI-TRIPý-DL CTL-CORIý-HLPRZR-LEVEITRIP-OR

CTL-CORE-HLPRZR-PRESffRIP CrI.CORE.HI-PRZR-PRES-7RWý-DL CTIýCORELHLPRZR-PRES-TRDý-OR CTIýCORELHLSG-LEVEIýTRIP Crl-COREýHLSQJEVELýTRIPý-DL CrL.CORE.HI-SO-LEVEI-TRIPý-OR CrIýCORE-LA)W-PRZRPRESý_TRjP MIýCOREJOW-MR-PRES-TRUý-DL CTL-CORE -LOW-PRZR-PRFS-TRIP-OR CTIýCORELLOW-SG-LEVEIýTRIP CrLCORE.LOW-SG-LEVEI.-TRIPý-DL CTL-CORE-LOW-SG-LEVEITRIFý-OR CrLýCOREJDWýSQ-PRES3RIP CIICOREýLOW.-SG-PRFS-TRff!-DL


Table G.3: Alphabetized Index of Long Variable Names

iable Name Index Long Variable

LOW.-SG-PRES-TRIP-OR 2152 CTIýFWS-CONTR

-OVER-POWER-MRGN-TRIP 525 GIIýFWSSONTR

-OVER-POWER-MRGN-TRIP.-DL 526 CTL-MS-ECONý-, VER-POWER.MRGNffRIR-OR 2162 CTL-MS-ýECO VER-TEMP-MRGN-TRIP 2159 CTI.FWS-ECON-. VER-TEMP-ýM11GN-TIZIR-DI, 2154 CTIFWS-ECON-ý VER-TEMR-MRGN-TRIP-OR 2147 CT1,FWS-H

POWER 2148 CTIFWS-jj-MA)

-POWER-FRAC-LAST 2149 CTL.ýFWS-H-TC POWER.FRACTION 2166 CTL-FWS-ISQ-P0 POWER-RATIO 549 CT1,FWS-ISO POWERA 2144 CTL-IFWSý-MA)ý

YTRIP 2161 CTI.-FWS-POS RCSFLOW-FRAC-TRIP 2155 CTL-MSPUMR_ RCSFLOW-FRAC-TRIR-DL 527 CTL-ýFWS-ýPUMPRCSFLO)&ý-FRAQ-TRIR-OR 2138 CTLýFWS-SETPO

ETPOINTS-FOR-TRIP 2141 CTLýFWS-SQ-LE IAS-TRIP 2139 CTL.FWS-SQLE IAS-TRIRDL 2140 CTLýFWS-SG-LE IAS-TRIR-OR 2158 CTLýFWS-SIG

:rRIP 2164 CTLýFWS-SPEE :MIR-CONTROLLER 2165 CTL-IFWSýSPEER :MIR-DELAYS 2145 CTI-FWS-SPEE

-TRIR-OR 2163 CTI-,FWS-SPEE

-TRIP-SIG 2150 CTI.ýFWS21RIP

-TURB-TRIP-BYPS 2156 CTL-FWS-TRIP-A

-TURB-TRIR-DELAY 528 CTI-FWS-TRIPý-C

-TURB-TRIP-DELAY-ý011 2267 CT1-FWS-TRIR-E USER-DEFINEDý-BYPS 2146 CTLýFWS-TRIP-S

SER-DEFINErLTRIP 2143 CTLýFWS-TURB USER-DEFINEDLTRIP-131, 2142 CTL-FWS-TURB USER.DEFINEDLTRIR-OR 2153 CTI.-FWS-VALV

-CHI-SPOINT 2160 CTLýFWS-VALV

-CH2-SPOINT 2157 CTI.ýFWS-:VALV ýCI-13-SPOINT 2209 CTLýGRAPH-17111

-CH4-SPOINT 2208 CTL-GRAPH-M.

.COMMON 2024 CTL-HA-ýREG-HE 2CONTROL 576 CTL-HALF LDN-W-GPM 2318 CTI-HEATý-FLU LDN-ZSPOINT 529 CT1,HEATER-C0 RCSYALVES 2032 CTI-HEATERS-C :rH-VARIABLES 2044 MI-HEATERS-C

2066 CT1ýHPSLFLO 2065 CTIýUPSLNPO

kuTo 2067 CTL-HPSI-PRES YPý-SIG 2068 Cr1.HPSIPUM YPS-CONTROLLERS 2069 CT1,HPSLSPLrr ONTROL 2239 CTI-ILEVEL

Long Var

CTLCORR

CTLCOR

CTLCOR

CTL-COR

CTL-COR

CTL.COR

CrtCOR

CTL.COREý

C7rL.COR

CTL-COREý

CTI-CORE

CTLCOREý

CTL-COR

CTLýCOREý

CTLýCORE.

CTL-CORE

CTLCORE,

CTL.CORE,

CTLýCORE

CTLýCORE,

CTLCOR

CTL-COR

CT1,COR

CT1,COR

CTLCOR

CTL.COR

CTLSOR

CTL-COR

CTL-CORE,

CTL-COR

CTI-COREý

CTL-CORE.

Cnýcvcs

CTL-CVCS

miýcvcs

crL-CVCS

cTLCVCS

CTLCVCS

CTLýCVCs

CTLýCvcs_

CTLýCVCs

CT1,CVCS

CTL-VBG

CTLýDELA'

CT1-FWS

CTL,_FWSE

CTI.FWS.ýB

CTLýFWSJ

.'4ame

OL.AUTO

OLLERS

ONTROLLERS

POS

IG

ALVEý-AUTO

S

'ONTOLLERS

low

UTO

ONTROLLERS

INTS

VELHIGH

VELLOAD

VELLOW

ýFRAC

MAX

ýMULT

3IG

LITO

NTROLLER.

ELAY

P

TRIR-DELAY

TRIR-FRAC

_AUTO

-POS

,-SIG

RVAL

ATý-X

'FRAC

NTROLLERS

ONTROL

ONTROLAUTO

JABLE

TS-TAB

TABLE

YUM

Index

1961

1935

2255

1958

1934

2254

1957

1969

1972

1971

1947

2279

1977

1936

2256

1959

1929

1937

2257

1960

1975

542

2248

1951

1976

1949

1942

1965

1950

1944

2263

1967

2005

2006

2007

2008

1995

2010

2003

2002

2020

2023

573

2247

2151

2167

548

2137



able Name Index Long Variable

532 CTL.MSISTRIPý_C I.-CONDITIONS 2266 MýMSISMPj 1.CORE.FLOW 531 CrLMSIVCONTI

_MSLBINFLOW 533 Crl.MSLJiCON-r _MSLBOUTý_FLOW 1973 Cr1,NUMRPS _PFLOW-NONMOM 577 CTIONE _SGS-VALVES 2203 CTIOUTPUT UTO 2212 CTIý_OUTPUIý_31)

LOW 2206 CrL.OUTPUIjCO

2204 CT1,OU-IUTjN 2210 CTLOLrrPLTIý_LO

WN-CONTROLLERS 2207 Cr1,_OLJTPU-1ý_NT WN-FRAC 2211 Cr1.OU-IU-Iý_Op( WN-SETPOINTS 2205 CT1,OUrPU7ý_OP' ýHEATEROFF 2056 CTL,_PORVAUT0

534 CTLý_PORVCONT LOW-TABLE 2052 CTI-PORV-PSET POINTS-TAB 543 CTI-POWER-CUT RES-TABLE 2038 MýPRES3HEA1 UMPý_NUM 2039 CrLPRES3HE PLIT 2036 CTLPRESPHEA1 E 2037 C171ý-PRES-PHEA1 HEAT-FLUX-FRAC 2050 CTLPRESSURIZE HEA-1ý-FLUX-TIME 2034 Crt-PRZR-BHLE POWER-FRAC 2033 CTLPRZR_ýHEATI POWEKTIME 2043 CTL.PRZRHEAT1 PRZR-PRESS 2241 CTIPRZRILEVE PRZR-PRESS-TIME 2012 CTLPRZR-LEVE ICSý_PRESS 2013 CT1,PRZRLEVE CSý_PRESSTtME 1996 CTIý_PRZRLEVE G-PRESS 1999 CTIý_PRZRLIQS G-PRESS-TIME 546 CTLýPRZRLVL.E RZRPRFSS 1998 CrlPRZR-PLEVE RZRPRESSTIME 1997 CTIPRZRPLEVE CS-PRESS 2011 CT1ýPRZRPROQ CS-PRESS-TIME 547 CTIý_PRZRPROQ QPRESS 2040 Cr1.PRZRREIý_P G-PRESS-TIME 2051 CTI-PRZR-RELIE DELAYS 2045 CT1,PRZRSPRA SETPOINTS 2049 Crl,-PRZR-SPRA

11?ý_DELAYS 2048 CTLPRZRSPRA ONTý_PRESTRIP 2047 CT1,PRZRSPRA) ONTROL 2046 MýMR.SPRA. ONTRO1_Atrr0 2000 CTI-PRZR-STM-S ETPOINTS 535 MýPSVCONTR G-PRES-TRIP 2055 CnPSVPSETý_B G-SLFLOW.-TRIP 2054 CTL.PSVPSE-Iý_C

IP 2053 CTIPSVPSETý_O

Index

569

2225

2316

2314

2315

2312

2313

2019

2025

2027

2026

530

2028

2001

2035

579

2071

2070

2072

2073

2074

578

2298

2299

2296

2297

2300

2301

2304

2305

2308

2309

2302

2303

2306

2307

2310

2311

2271

2192

2264

2113

2110

2115

2111

2112

2114

2116

Long Vari

CTL.INrr

CTLINrrIA

CTI-INITIA

CT1,INTE

CTLINTEG

CTL-INTEG

CTI-INTEG

CTL-LDN-A

CTLLDN

CTILDK-H

CrL.LDNT

CTLLETDC

CTL.LETD0

CTLý_LETDO

CTILEVE

CTLLUAM

CTIýLPSI_

CTLLPSIN

CT1_LPSLP

CTLLPSIP

CT1_LPSLS

CT1,MON

CTI-MAX

CTL-MA)(

CT1_MAX_

CTL-MAX

CTI.-MAX

CTL.MAX

CTIý_MAX_

C'rLMAXI

CTL-MAX-S

CrL._MA.XS

CTLýMuqp

CTI-MIN-P

CTL-MIN-R

CT1.MINR

CTI1MINS

CTLýMuqs crl,_MIS(ý_

CTI.MISC

CTI.MISC-7,

CTLýMSISJ

cr1,_MSIS_(

CTLMSIS_(

CTLýMSISS

criýMSISS

CT1_MSISS

CTLýMSIS

lame,

ONTROLLER

ELAY

OLLERS

OLLERS

AAP

UNT

7ERVAL

OP

ITLE

L

ION

OLLERS

ACK-CONTROLLER

R-OFF

R-ON

R-OFF

R-ON

R RELIEF

IELýSPOINT

R-SETPOINTS

RS_ýVOLT

L

-ERROR

JNST

-SETPOINTS

PVOLý_REF

RR-CONTROLLER

L

L.TEMP

EVEL

VLýCONTROLLER

RES

F-SETPOINTS

r-CONTROL

r-CONTROI-AUTO

r-PRES-OFF

-PRES-ON

r-SETPOINTS

PVOL-REF

OLLERS

LDN

LOSE

PEN




EffRIP 2084 CTL-SIS-SI[j-H

LOW-STPOINT 2086 CTL-Srfý-ELEV-Pf

CONTROL 2087 CTI.Srlý-FLOW-C

CONTROL.AUTO 2088 CTL.Srlý-GAS-CO

PTRIP 2089 CTIýSIT-GAS-PR

ETPOINTS 2090 CTL-SIT-GAS-ýVO

IP 2091 CTL-Sný-ISQ-VA

TRIPý-DELAY 2092 CTL-SrIý-LIQ-SPV

TRIP-TIME 2093 CTL.SM-LIQ-VO

ONTROLLERS 2085 CTL-SrLNUM

ONTROL 2229 CTI-SPARE

H 2213 CTLýSPARE2

-MIN 538 CTLýSPRAY-CO

PLIT 1948 CTI.STEAM-ME

ELTEMP 1941 CT'L-STEAM-ME

ELTEMPD 2261 CTIýSTEAMJEE

LOW 1964 CTL.STEAM-ýFEE

LOWD 2295 CTLýSUMMARY

ODIM 2014 CTLýZýAVG

ERTIME 539 CTL.TýAVG-CO

RES 2015 CTLýT--REF

RESD 540 CTL:LREYý-CON'

EMP 553 CTL-TAV-NUM

VEL 554 CTLffAV-PATH

FETIES 2214 CTL-TIMEýBLOC

'-SETPOINTS 2202 CTL-TIME.CON

ASET-OPEN 1968 CrL.TIME-COR

PSETý.CLOSE 1926 CTL-TIMEýSTEP

PSET-FULL 12 CTL.TITLE

-PSET-OPEN 2101 CTIýTURB-AO

ONTROI.-AUTO 2121 CTI.,TURB-BYPA

HLCONT-PRES 2130 CTIýTURB-BYPA

LOVVý-SLýPRES 555 CTI.,TURB-BY

LOV%ý-TAVG 556 CTI.-TURB-BY

PRZR-PRES-LOW 2122 CTL-TURB-BY

PTRIP 2098 CTL-TURB--CO

ETPOINTS 2105 CTLZIURB-CO

SLSH-DP 2106 CTI-TURBSO

IME 2103 CTL-TURB-DEM

rRIP 2124 CTIýTURB-DUM

TRIPSONTROLLER 2129 CTL-TURB-ýDUM

MMON 2128 CTL-TURB.ýDUM

NTROL 2126 CTLýTURB-ýDUM

ELAY 2123 CTL-TURB-ýDUM

w 2127 CTL-TURB-ýDUM

LPSI-BC 2125 CTI.TURB-DUM

LPSI-H 2109 CTLýTURB-PTR

T-BC 2191 CTL-TURB-RUN

Index

1970

1945

2180

2182

2184

2181

2183

2268

2185

536

2094

2095

2096

2097

2194

2195

2199

2200

2198

2201

2196

2197

2193

2240

2131

2132

2136

2135

2134

2133

2077

2061

2063

2062

2059

2079

2058

2060

2075

2078

537

2057

2064

2076

2080

2081

2082

2083

LDng Vari

C7LQCOR

CTLýRCP

CTI.-RPCS

CTL-RPCS

CTL-RPCS

CTL-RPCS

CTLRPCS

CTL-RPC

CTL-RPCS

CTL-RPS-jC

CTLSDC-C

CTL-SDC-E

CTLSDC-H

CTLSDC-S

CTLSET ý13

CTLSETý-D

CTI-SETý

CTL-SETý

CTL.SET-N

CTL.SET-P

CTL-SET-P

CTI.-SET-P

CTL.SET-T

CTISG-IL1

CTLýSG-SA

CTI.,SGS

CTL.SGSV

CTL-SGSV

CTLSGSV_

CT1,SGSV

CTLýSIASJ

CTL-SIAS

CTL-SIAS

CTL-SIAS

CTL-SIAS

CTL-SIAS

CTL-SIASý'

CTI-SIAS

CTI-SIAS-'

CTL-SIAS

CTL-SIAS

CTLýSIS-0

CTL-SIS-0

CTLýSIS-D

CTL-SIS-m

CTLSISH

CTLýSIS-H

CTLýSIS-S

14ame

ES

OEFF

NST

ES

LUME

,VE

OL

LUME

TROLLERS

DLMISMATCH-BYPS

ELMISMATCH-TRIP

D-MISMATCH-TRIPý-DL

DLMISMATCH-TRM-OR

ATA

[TROLLER

OLLER

K

TANTS

-TRIP

r-TC SS-CONTROL

SS-CONTROL.AUTO

SS-NUM SS-PATH

SS.SETPOINTS

rROL

rROL-AUTO

rROI.-LjDAD

AND

Fý-DELP

P-MODE

Pý-NCLOSE

P-NOPEN

PLOPEN

P-QCLOSE

P-QOPEN

P

BACK


Index

2189

545

2270

2188

2186

544

2187

2190

2269

2099

2104

2107

2108

541

2265

2102

2100

2226

2042

2041

587

575

584

274

1523

1531

1535

1538

1534

1533

1532

1537

1536

557

558

2371

2369

2370

2368

2375

2372

2373

2374

2376

2377

2215

223

224

Long Vari

CTLTURB..

CTL_TURB

CTL TURB_

CTLTURB

CTL_TURB

CTITURB_

CTL_TURB_

CTL1TURB_

CTL_TURB

CTITURB_

CTL_TURB_

CTL_TURB..

CTLJTURB.

CTL_TURB "

CTLTURB

CTLTURB_"

CTL_TURB_.

CTLUNUSE

CTuVOLT_

CTLVOLT_

CTLWARN

CTLZERO

CTLMAX

CURRENTT

CVCS-DATA

CVCSRHX_

CVCS_RHX_.

CVCSRHX

CVCS RHX_

CVCS_RHX '

CVCS_RHX."

CVCSRHX_

CVCSRHX_

DBADD

DBCOM

DBGSGTR_

DBGSGTR_

DBG.SGTR_

DBGSGTR

DBG SGTR_

DBGSGTR_

DBGSGTR_

DBG_SGTR_.

DBG_SGTR_

DBGSGTR_

DELT

DESIGNFLC

DESIGN_FLC

Table G.3: Alphabetized Index of Long Variable Names able Name Index Long Variable r RUNBACKAUTO 225 DESIGNFLOW_SA RUNBACK CONTROLLER 890 DHDM RUNBACK DELAY 889 DHDU .SETBACKAUTO 893 DHF._DP _SETBACKCONTROL 894 DHGDP SETBACK-CONTROLLER 1478 DMWQT ENTH SETBACKSETPOINTS 1477 DMWQTFLOW SETBACK_TRIP 1022 DPACTUAL SETBACK.TRIPDELAY 1023 DPCHECK SETPOINTS 1017 DPELEV STEAMRATED 1020 DP_EXT

TRIP 1016 DPFRIC TRIPAUTO 1127 DP_GLOB TRIPCONTROLLERS 1019 DPHEAD TRIPDELAY 1018 DP_LOSS TRIP_TIME 1049 DP.WLOSSUPLEN

TRIP_VALVE_TIME 1015 DPMOM ED 1095 DP_NON_UHEAD BACK 1039 DPPUMP PROP 1021 DP_TOT

885 DPDMLIQ

886 DPDMSTM

884 DPDMTOT

*AB 888 DPDUSTM

887 DPDUOTOT DATA 899 DRFTBUB HCH 273 DTDW_TAB HEAT 1456 DUM001 HLDN 892 DVDHTOT J'CH 891 DVDPTOT "TLDN 895 DVF_DP WCH 896 DVG_DP WLDN 559 ELEMS

423 ELEVTUBESHEE

560 ELIN FLOWSLOT 2244 ELLAST FLOW1 580 ELMAX FLOW2 561 ELTYPE PARTITION 1118 ENGYGLOB

PRESS_ITER 1058 ENGY_HEATER PRESSPRII 1105 ENGY QT PRESSPRI2 841 ENGYSTM PRESS_SG 1166 ENGYSTM LAST SVOL_TUBEI 840 ENGYTOT SVOLTUBE2 1167 ENGYTOT_LAST

1117 ENTH-GLOB 1W_PORV 849 ENTIHLIQ 1W_SAFETY 1 1173 ENTHLIQLAST


4ame

•FETY2

.T

I

G-233

Index

852

1122

1175

851

1104

1051

850

1174

853

1123

848

1091

1025

400

204

800

802

799

801

798

803

205

1179

1180

586

2216

1886

1196

1195

2224

1042

2563

2564

2565

259

234

1026

595

464

467

1772

1766

1769

1778

1781

1775

1784

1771

Table G.3:

Long Variable Name

ENTHLIQSAT

ENTH LIQ.SATGLOB

ENTH_-LIQ..SATLAST

ENTHMIX

ENTHQT

ENTHQUADLCORE

ENTHSTM

ENT•-STM-LAST

ENTHSTMSAT

ENTH-STM-SAT-GLOB

ENTH-TOT

ENTH_UHEADTOP

ESUBK

EVAPSSALPHA

EXCOREBOT

EXCOREOFFSET

EXCOREOFFSETAV

EXCOREPOWER

EXCORE-POWER-AV

EXCOREPOWERD

EXCORETAU

EXCORETOP

FATALJNPUTERROR

FATAL-OUTPUTERROR

FCTMAX

FDELT

FHINIT

FLAG-LOCA

FLAG-RODEJ

FLGQUE

FLOWCOREIN

FLOWDP_MAXERR

FLOW_DPNODEMAXER

FLOW DP._PRINTNODE

FRAC_HDTABL

FRACTABL

FSUBK

FUEL-DENSITY

FW COEFF

FWLB.AREA

FWLB ECONENTH

FWLB_ECON_F

FWLB..ECONFLOW

FWLB-ECON_10

FWLB.ECON_PT

FWLB_ECON QUAL

FWLBECONXE

FWLB_ENTH

Alphabetized Index of Long Variable Names

Index Long Variable?

1765 FWLB_F

1768 FWLBFLOW

1770 FWLBH

1758 FWLB_IN

1777 FWLB_10

1776 FWLBIODINE

1764 FWLB_LOCATION

1761 FWLBOUT

1779 FWLB_PART

1780 FWLB_Pr

1774 FWLBQUAL

1773 FWLBQUALITY

1767 FWLB_W

1783 FWLBXE

1782 FWLBXENON

2420 FWSAEXTF

2430 FWSAFWLB

2462 FWSATABLE

2461 FWSBTABLE

2378 FWSCOMMON

1743 FWSCON_10

1744 FWSCON_PT

1745 FWSCONXE

2381 FWSCV

2406 FWSCVAFLO

2408 FWS_CV_DPMIN

2407 FWSCV_RESMN

2440 FWS_CVP

2436 FWS_CVV 2505 FWSDCLMASS

494 FWSDIAM

2380 FWSDPEL

R 2506 FWSECL_MASS

495 FWSECONDIA!•

1737 FWSECONFLO

477 FWSECONJUN(

489 FWSECONLINE

1742 FWSECONLINE

1751 FWSECON-NOZ

1748 FWSECONNOZ

1754 FWSECONNOZ

1757 FWSECONNOZ

486 FWS-ECON.VAL

1731 FWSECONVAL

492 FWS_ECONVOL

1739 FWSENTH

1892 FWSENTH_TAB

2473 FWSFDHEAT


Name

4

MTION

,.COEFF

.H

.._ENTH .,_FLOW

_QUAL -,T YE_COEFF

YE_P

LE

G-234


Index

2490

2411

2379

2484

2454

2509 2433

1736

1738

465

2497

2495

2496

2492

2493

2494

2397

2392

2419

2413

2485 2416

2388

2459

1893

1894

1895

2479

2476

2501

2403

2402

2503

2504

2404

2423

2445

476

1728

2410

488

487

493

1740

1735

1741

475

2508

Lon! Variable Name

FWSFDMODL

FWSFDNODE

FWSFDPATH

FWSFDPOSO

FWSFDPUMP

FWS_FDSYST

FWSFDVALV

FWSFLOW EWSFLOW-TQT FWSFLOWIOO

FWSFWRCINT

FWS_FWRCIR

FWSFWRCOUT

FWS_FWRCPB

FWS_FWRCRE

FWSFWRCSP

FWS-GPMCOR

FWSHEXT

FWS-HEXTF FWSHEXTN FWSHFWB lAS FWSHNODE FWSHPATH

FWS_HT

FWSHTABLEENTH

FWSHTABLE..LOAD

FWSHTABLEýNUM

FWS_HTHMX

FWS...TRHOV

FWS_1AUTORC FWSICK

FWSICPUMP

FWSIFrllIP

FWSJlFTRPO

FWS_M4F

FWSIMN

FWS_INDEXF

FWSJUNCTION

FWSJUNCTION_P

FWS_KEY

FWS_LINE.COEFF

FWSLINEýCOEFFS

FWS_LINE.DIAMS

FWSLINE..ENTHALPIES

FWS-L[NE-FLOWS

FWSLINE-H

FWSLINE-JUNCrION

FWSLTNE-MASSES

Index

490

2483

2451

2401

2400

2398

2399

2472

2425

2409

2489

2449

2488

2487

2471

2424

1750

1747

468

1753

1756

1749

1746

1752

1755

2442

2429

2486

2431

2467

2466

2500

2463

2428

2427

2426

2468

2498

2465

2444

2469

2491

2432

2470

2453

2443

2464

2452

WCAP-15996-NP, Revision 0G-3

Lon! Variable Name

FWS_-LINEVOLUMES

FWSMAXTAU

FWS_ýNAFWVT

FWS-NCPUMP

FWSNDEXT

FWS_NDIN

FWS-NDOUT

FWSNEFWP

FWS_NEXTN

FWS-NFLQ

FWSNHDPTBL

FWSNHDV

FWS.J4HT

FWS-NHTBL

FWS_NMFWP

FWS_ýNNOD

FWSNOZENTH

FWS_NOZ_FLOW

FWSNOZ_HEIGHT

FWSNOZQUAL

FW_ýNOZ_T

FWSNOZZLE_-ENTHALPY

FWS-NOZZLEFLOW

MSNOZZLEQUALITY FWS.NOZZLE_TEMP

FWSNPATH

FWSNPFWLB

FWSý_NPHEAT

FWSJJPMFPRV

FWSNPMPEFW

FWS_ýNPMPMFW

FWS..NPMPRC

FWS-NPMPTH

FWS-NPSGAFW

FWS-NPSGECO

FWSNPSGMFW

FWS-NPTHiMFP

FWS_ýNPTHRC

FWS-NMr

FWS_NPTV

FWSNPUM

FWSJ'4RCIRC

FWS_NSG

FWSNTABFP FWSNTABFV

FWSNTABLE FWS_NTABP FWS..NVAFWI

G-235

Index

2448

2499

2447

2450

2446

2415

2414

2384

2421

2412

2405

2435

2395

483

1734

481

478

1733

479

474

1727

1726

1732

482

480

2477

2389

2478

2391

2382

2390

2393

2383

2417

2394

2455

2456

2441

2434

2396

2458

2457

2438

2482

2502

2439

2437

2480

Long Vari

FWSNVAL

FWSNVALI

FWS NVBF'

FWS.NVHD

FWSNVMF

FWSP

FWS-P0

FWSPEXT

FWSPEXTF

FWSPEXTT

FWSPOSIS4

FWSPOSIT

FWSPS

FWS_PUMP_

FWS.PUMP.

FWSPUMPR

FWSPUMP

FWS_PUMP_

FWS.PUMP.

FWSPUMP_

FWSPUMP_

FWSJUMP_

FWSPUMP

FWSPUMP_

FWSPUMP.

FWSPWRT

FWSQCUR

FWS-QPTBL

FWSRES

FWSRESL

FWSRESV

FWSRHOE.

FWSRHOFI

FWSRHON

FWSRP

FWSSPDM]

FWSSPEED

FWSSTP

FWS-STROI

FWSSUMP

FWSTAUO

FWSTAUO:

FWS-TCLOS

FWS-TENHr

FWSTIMET

FWST1LAG

FWS.TOPN

FWS_TPOW




2474 FWSTPWR

RC 2475 FWSTQLAG

2481 FWSTWHDP

V 485 FWS_VALVECOE

V 484 FWSVALVECOE

1730 FWSVALVEP

1729 FWSVALVEPRE

491 FWS_VOL

2387 FWS_W

2386 FWS_WO

0 2418 FWSWEXTF

2385 FWSWMAS

2422 FWS.WSUM

'-COEFF 2460 FWSWT

FLOW 562 GROUPS

*-FLOWJNPOINTS 2245 GROUT

_FLOWTABLE 583 GRPMAX

.HEAD 2582 GS-PRZRNONC

YEAD-TABLE 2583 GSSPECIES

JUNCTION 2581 GSYES-NONC

UP 1481 GWSQTFLOW

"PIN 1480 GWSQTPRES

-SPEED 199 HACEACORE

SPEEDNPOINTS 209 HAUHEADCORI

-SPEEDTABLE 441 HAWALLIMSLI

BL 499 HAWALLISGBD

R 442 HAWALLOMSL

L 500 HAWALLOSGBI

245 HAD

253 HADC

2513 HALF_LIFESOU

XT 243 HAN

251 HANC

OD 249 HAR

257 HARC

D 247 HAT

255 HATC

214 HCAP-HEATER

KE 260 HDDEGTABL

1038 HEADPUMP

FF 875 HEATCOND

N 870 HEAT.CONT

S 1041 HEATCORE

DP 1057 HEATELEC

871 HEATEXT

1060 HEATHEATER

874 HEATLIQ

R 1061 H EAT_PRZR

Name

FE

FFS

SSURES

E

,H

D

JTES

G-236

Index

1036

1033

873

872

869

229

385

386

387

392

393

394

469

470

471

246

254

244

252

250

258

248

256

2526

2518

2524

2520

2519

2525

2523

2522

2517

2516

2521

2230

2237

2359

2229

2238

2233

2236

2231

2234

2232

2235

582

570

588

Lone Vari

HEAT_PUM]

HEATSG

HEATSTM

HEATTOT

HEATWAL

HEIGHTQT

HSP_TBL

HSPJBL.D)

HSPTBL_D.D

HTI3TBL

HT3_TBL_D.

HT3_TBL_D

HTNOZ

HTNOZ_ECC

HTNOZ_EFV

HVD

HVDC

HVN

HVNC

HVR

HVRC

HVT

HVTC

IDJTYPE_Al

IDTYPE_BC

ID_TYPE_HY

IDTYPE_10]

IDTYPE_NI

ID_TYPE_NI

IDTYPE_NC

IDTYPEPA

IDTYPESO

IDTYPE SP

IDLTYPEXE

INITALL

INIT_CORE

INITDEBUG

INITFLAG

INITITER

INIT..OFFC

INIT_OFF CC

INITLOFF_MC

INILýOFFYPO

INITOFFRC

INITOFF_SG

INMAX

INPED

INPEDFILE

Table G.3: Alphabetized Index of Long Variable Names able Name Index Long Variable 1 P 572 INPEDPAGE

571 INPEDSEQNCE

2276 INTERPOLATION_

2290 IODINE._OTALS_ L 2360 JUNKPARTITION

766 KFRAIN

195 KLOSS_UPLEN_NI SGN I 194 KLOSSUPLENPC SGN2 821 KSHAPIN

1525 LDNPIPE AREA SGNI 1524 LDNPIPEDATA SGN2 1529 LDN_PIPE.DELTA

1528 LDNPIPEKENT )N 1527 LDN_PIPE._KGEON

1526 LDNPIPELOD

1539 LDNRCSENTH

1540 LDNRCSPRES

1424 LDNS RCS FLOW

878 LEVLLIQ

1044 LEVLLIQVESSEl

877 LEVL_MIX

1046 LEVLMIXCORE

1045 LEVL_MIXVESSE R 1062 LEVLPRZR_DP )RON 219 LEV LPRZRRTD YD 1106 LEVLQT

DINE 220 LEVL_REFBOT 6 221 LEVLREFTOP T 222 LEVLRELIEF )NC 1197 LOCABLOWDOW RT 581 LSTMAX LUTE 2246 MAL_CTL ECIES 1760 MAL FWLBECOI NON 1763 MALFWLBECOI

1759 MALFWLBIN

1762 MALFWLBOUT -OUTPUT 1454 MAL_LBLOCA

1530 MALLDNBREAK

1672 MALMSLBIN IT 1649 MALMSLB_OUT ON 1472 MAL_RCP_HIVIB

ODELS 1471 MAL_RCPLOCKE] 1W 1470 MAL_RCP_SHAFTI ZS 1458 MALRCSVALVE S 1473 MAL_RODCORE

1457 MALRODEJECT 1453 MAISBLOCA

1455 MALSGTR


N4ame

ERROROPTION

PARTITION

EG

3S

_ELEV

L

L

IN

UN

LOUT

D

BREAK

I

G-237

Index

1464

1463

1466

1461

1465

1462

1468

1467

1469

1459

1460

206

846

1170

1183

918

1108

1116

844

1168

1093

2536

2569

2537

2566

2541

2562

2542

230

845

1169

843

1171

1107

593

443

501

28

29

830

833

832

828

829

831

1845

2242

827

Table G.3:

Long Variable Name

MALYLVPRZR_CONT

MALVLVPRZRMOV

MALVLVPRZRMSPRAY

MALVLVPRZRPORV

MALYLVPRZR QT

MALVLV-PRZRSAFETY

MALLVQTCONT

MAL3VLV.QTGWS

MALVLVQTNSUPPLY

MAL VLVUHEADCONT MALVLV UHEADQT

MAP-EXCORE

MASS-BUB

MASSBUBLAST

MASSBUB.PRED

MASSBUBSECT

MASSGASQT

MASSGLOB

MASS-LIQ

MASSLIQJLAST

MASS-NONUHEAD

MASS-NONCDIS

MASSNONC_DISRCS

MASS NONCDIS_TOT

MASSNONC-RCS

MASSNONC-SEP

MASSNONC_SEP_RCS

MASSNONCSEP_TOT

MASS.QTMAX

MASSSTM

MASSSTMLAST

MASSTOT

MASSTOT_LAST

MASS.WATQT

MATTYP

MCP_-WALL_MSLH

MCPWALLSGBD

MODINIT

MODINITV

MODOFFCHT

MODOFF-POWER

MODOFFQT

MODOFFRCP

MOD OFFRCPOIL

MODOFF_.RCS

MODOFFSGBD

MODELERROR

MODELOFF



Index Long Variable Name

2221 MODELQUEUE

2223 MODQUE

449 MSLBAREA

1673 MSLBINFLOW

1650 MSLBOUT_FLOW

516 MSLHACROSS

517 MSLHACROSST

514 MSLHAFRSL

1686 MSLH_AOUT

1687 MSLHAOUTATM

1688 MSLHAOUTCOND

1689 MSLHAOUTCONT

1690 MSLH_AOUTTURB

1651 MSLH_CON-10

1652 MSLHCONPT

1653 MSLH_CONXE

1678 MSLH_CSL

1875 MSLHDPMIN_MULT

1654 MSLHDVDH

1655 MSLHDVDP

1698 MSLH_-ENTHATM

1703 MSLHENTHCOND

1708 MSLHENTHCONT

1713 MSLHENTHTURB

515 MSLHFKBRK

518 MSLH_FKCROSS

519 MSLHFKCROSST

1697 MSLH_FLOWATM

1724 MSLH_FLOWCHOKED

1702 MSLH_FLOWCOND

1707 MSLH_FLOWCONT

1712 MSLH_FLOWTURB

1848 MSLH_FUIMEMAX

1656 MSLH_H

1657 MSLHHF

1658 MSLHHG

1674 MSLHHSL

1699 MSLH_10_ATM

1704 MSLH_10_COND

1709 MSLH_1OCONT

1723 MSLHIOCONTTNT_LEAK

1722 MSLH_10_CONTLEAK

1718 MSLH _IO _INT _ATM

1719 MSLH_10_INTCOND

1720 MSLHIOTNT_CONT

1717 MSLHI 0 NTFLOW

1721 MSLHJO _INT _TURB

1714 MSLH_10_TURB

G-238

Index

1677

1659

1660

450

451

1682

1680

1681

2274

1696

1661

1675

1700

1705

1710

1715

1662

1663

1648

1664

1665

1666

1667

457

1676

1668

452

454

453

455

1683

1684

1669

1691

1692

1693

1694

1695

1670

1701

1706

1711

1716

1679

1906

1907

1908

1909

Long Vari

MSLHISL

MSLH_M

MSLHML

MSLHMSIN

MSLHMSIV

MSLHMSIV

MSLHMSIN

MSLHMSIV

MSLHNO_,

MSLHOUT]

MSLH-_P

MSLHPSL

MSLH_PT1_A

MSLH_PT_C

MSLH_PT_C

MSLHPT_T

MSLHQ

MSLHQAT

MSLHSTAI

MSLHSV

MSLH_SVF

MSLH-_SVG

MSLH_T

MSLH_TAT1n

MSLH-TSL

MSLH_TWA

MSLHVALI

MSLHVALI

MSLHVALI

MSLHVAL•

MSLHVAL•

MSLHVALI

MSLHWIN

MSLH WOU

MSLHWOU

MSLHWOU

MSLH_WOU

MSLHWOU

MSLH_X

MSLHXE_A

MSLH_XE_C

MSLHXEC

MSLHXE_T

MSLHXSL

MSLH2_CON

MSLH2_CON

MSLH2_CON

MSLH2_DVD


Table G.3: Alphabetized Index of Lon2 Variable Names able Name Index Long Variable I

1910 MSLH2_DVDP

1911 MSLH2_H

1912 MSLH2_HF _AMAX 1913 MSLH2_HG _BYPASSAMAX 1914 MSLH2_M

'BYPASSPOS 1915 MSLH2_ML _POS 1916 MSLH2_P

FSIG 1917 MSLH2_Q AOISTURECARRY 1918 MSLH2JQATM FLOW 1905 MSLH2_STATE

1919 MSLH2_SV

1920 MSLH2_SVF 1TM 1921 MSLH2_SVG

OND 1922 MSLH2_T

ONT 1923 MSLH2JTWALL "URB 1924 MSLH2_X

94 N.AREASECT

73 NBOT

193 NBOTUPLEN

74 NGEOM

81 NHEAT_CAP

80 NHEAT_XFER_B(

79 NHEATXFERC(

4 77 NHEATXFER_LI

78 N_HEAT_XFER_Si LL 95 NHEIGHTSECT

VEAMAX 909 NHETERO VEEXIT 75 NSECTIONS VE_INLET 192 NTOPUPLEN IE.NUM 82 NXFERBOIL IEPOS 83 NXFERINJ ESIG 907 NECANDIDATE

68 NODEANNUL T 71 NODEAREA T_ATM 69 NODECEASH

T_COND 54 NODECL T_CONT 55 NODECLI TTURB 56 NODE CL2

57 NODECL3 TM 58 NODE.CL4

OND 65 NODECORE ONT 72 NODEHEIGHT

URB 41 NODE_HLI

42 NODE HL2 LO 43 NODEHL3

rPT 44 NODEHL4 _XE 66 NODEPRZR

'H 45 NODESG

Name

OT

ONT

Q rM

Index

47

46

60

49

48

61

51

50

62

53

52

63

67

908

1096

2529

2530

2510

563

270

496

23

202

24

38

473

472

211

36

513

33

34

2528

103

106

100

105

102

101

99

107

267

22

233

20

35

1497

462

Long Vari

NODESGI(

NODESG! I

NODESGI i

NODESG2(

NODE.SG2

NODESG2I

NODESG3(

NODESG3I

NODESG31

NODESG4(

NODE_SG41

NODESG4I

NODEUHE

NONEQ_S

NONC.DILl

NONCJK(D

NONCMW

NONCOND_

NOTAB

NPTSTAB

NUMAFW.

NUMBACI

NUMCEAS

NUMCHGS

NUMCLN

NUM_FWS

NUMFWS

NUMHEA'

NUM_HLN

NUMMSLI

NUMNOD

NUM-NOD

NUMNON

NUM-PATI

NUM PATI

NUMPATI

NUMPATI

NUMPATI

NUMPAT)

NUM-PATI

NUMPATI

NUMPOLl

NUMPROI

NUMPUM

NUMSG

NUM_SGi_

NUM_SGS

NUMSL



able Name Index Long Variable l•

C 37 NUM_SL_NODES

H 104 NUM_SMLBRK

P 2512 NUMSOLUTES

C 183 PAREA

H 190 PAREA_ATWS_M

P 188 PAREA_ATWS_M

C 1198 PAREA_LEAK

H 191 P._AREA_RODEJ

P 456 PATMOSPHERE

C 1071 PBORON_AUX_S

H 1068 PBORON_SPRAY

P 2555 PCONCSOLU

AD 1849 PCONDENSER

TATE 185 PDIAM_1HYD

-RATE 1031 P..ELEV_DOWN

'ISSOLVE 177 P ELEV_EXIT

155 P_ELEV_INLET

-COMMON 1030 PELEVUP

945 P_.ENTH

1070 P-ENTHAUXSPi

PUMPS 1083 P.ENTH_BLEED

KHEATERS 966 PENTHLIQ

1374 PENTH_LIQ_LB

SPUMPS 1074 PENTH_RELIEF

JODES 1067 PENTH_SPRAY

JUNCTIONS 967 PENTH_STM

-PUMPS 1375 P.ENTHSTMLB

rERS 1090 P..ENTH_UHEAD_

NODES 1088 PENTHUHEAD

Fl 922 P.FLOW

ES 1069 PFLOWAUX_SP

ESSEC 2573 PFLOWAUXSP_

C 1072 PFLOWBLEED

HS 943 P_FLOWCRIT

HSCL 1176 PFLOW_LAST

HS_EXT 2557 PFLOWNONC

IS_HL 2558 PFLOW_NONCJ

S-INT 2559 P._FLOW_NONCI

S_LEAK 1202 P_FLOWPRZRC

SMOM 1080 PFLOWPRZR_(

HS_NONM 1073 P_FLOWRELIEF

3S 1066 P_FLOWSPRAY

PHEATERS 1089 PFLOWUHEAD

PS 1087 P_FLOW_UHEAD

2560 P_FRACNONC

NODES 2561 P_FRAC_NONC_1

SECT 178 P_GEOM

1029 PNODEDOWN

4ame

AX

IN

PRAY

RAY

CONT

_QT

RAY

NONC

MOM

NONM

"ONT IT

_CONT _QT

IOT

G-240

I

Table G.3: Index Long Variable Name

154 Pý-NODE-EXIT 132 Pý-NODEJNLET

1028 Pý-NODE.UP 1078 Pý-NONC-PRZR-CONT 1079 P-NONC-PRZR-QT 1113 Pý-NON(ý-QTý-CONT 1097 Pý-NONC-UHEADý-CONT 1098 Pý-NONCý-UHEAD-QT 970 P-QUAL 179 P-RADIUS

1013 Pý-STM-DOWN 992 P-STM-UP 968 Pý-SVOL 1377 P-SVOI-LB 1075 Pý-SVOIRELIEF 991 P-VOID 1376 Pý-VOIDý-LB 122 PATN-ANNUIý-CORE 200 PATH-CEA-LOW 201 PATH-CEA-UP

128 PATH-CL

123 PATHSOREýUHEAD 127 PATH-HL 182 PATN-KLOSS-NEG 181 PATHI-KLOSS-POS

125 PATH-LB-LOCA 194 PATli-LEN-DIAM 126 PATH-PUMP 129 PATH-SG

124 PAT14-SPRAY 121 PATH-SURGE 180 PATH-TLOA 130 PAT'H-UCEA 402 PERIM

6 PLANTý-DATADATE

3 PLANT-DATA-FILEýNAME 2 PLANT-DATA-LABEL 5 PLAYIý-DATA-TIME 4 PLANIý-DATA-TITLE 520 PLT-CTL 13 PLTDATA 18 PLTI-RCS 19 PLT-RCS-DESIGN 31 PLT-RCSýNODALIZATION 30 PLT - RCS-NODE 96 PLT-RCS-PATH 210 PUTý-RCS-PRZR 226 PLIý-RCS-QT



Index Long Variable Name

232 PLT-RCSý-RCP 21 PLT-RCSffYPE

186 PLTý-RCS-VES 329 PLTý-RCS-VLVAREA 379 PLTý-SGS 463 PLTý-SGSý-FWS 425 PLTý-SGS-HEAT 380 PLT-SGS-INTERNAL 439 PLTý-SGS-MSW 512 PLT-SGS-MSLH2 497 PLTý-SGS.SGBD 335 PLTý-VLVAREAPRZR-CONT 334 PLTI-VLVAREA-PRZR-MOV 337 PLIý-VLVAREA-PRZRMSPRAY 332 PLT-VLVAREA-PRZR-PORV 336 PLT-VLVAREA-PRZR-QT 333 PLIý-VLVAREA-PRZK-SAFETY 339 PLT-VLVAREA-QTý-CONT 338 PLT-VLVAREAýQ-Fý_GWS 340 PLT-VLVAREA-QTý_NSUPPLY 330 PLTý-VLVAREA-UHEAD-CONT 331 PL7ý-VLVAREA-UHEAIý-QT 815 POMý-AXIAIýDATA 747 POW-CORE-TRIF-FRACTION 751 POW-DKHT-ANSDHC 748 POW-DKHIý-COMMON 753 POW-DKHTý-DHCBEG 754 POW-DKH7ý-DHCFCT 756 POW-DKHTý-IFDHC 749 POIK-DKHTý-INP 752 POW-DKHTý-NDHC 755 POW-DKIJTý_STATE 757 POW-DKHIý-TIMDHC 750 POW-DKHT-TIMDHT 811 POW-EXCORECALIB 804 POW-EXCORE-DATA 797 POW-EXCORELDISP 813 POW-EXCORELGAIN 807 POW.-EXCOREýOFFSET 809 POW.-EXCORa-OFFSELAV 796 POW-EXCOREý-OUT 806 POW-EXCOREýPOWER 808 POW-EXCORE.POWER-AV 805 POW-EXCORELPOWERD 814 POW-EXCOREýSVR 810 POW-EXCORE-TAU 812 POW-EXCOREýTUNE 724 POW-IFUPOWTIM

G-241

Table G.3: Alphabetized Index of Loniz Variable Names

Long Variable Name

POW-INITIAL-CONDITIONS POWKIN-ALPHA POW-KIN-BBAR POW-KIN-BBARR POWK[N-BETA POWýKrN-BORONFBOFrrION POW-KINSH12 POW-KIN-COMMON POW-KIN-CORIý-W-FRACMB POW-KIN-CUT-ROD-OFTION POW-KIN-CUTBACK POWKIN-ýDENCOR POW-KIN.ýDH-FACTOR PW-KIN-DK POWý_KIN-DKjNrr POWKIN-ýDKBOR POW-KIN-DKCON POW-KIN-PKCONZ POAý-KIN-DKCTM POW-KIN-DKCTMZ POWKIN-DKCUT POWLKIN-DKDEN POW.-KIN-DKDENZ POW-KIN-DKDOP POWKIN-DKHERMC POW-KIN-DKINS POW-KIN-ýDKINSZ POW-KIN-DKMOD POW-K[N-DKROD POW-K[N-DKSCRAM POW-KIN-DKT POWLKIN-DKTMD POW-KIN-PKTMP POW-K[N-DKTMPZ POW-KIN-DLAM POMý-KIN-DOPPLER-FB-01710N POWLKIN-EDGEýWEIGHT POW-KIN-EN2 POW-KIN-EX2 POW-KIN-FEEDBACK-OPTIONS POW-KlNffWWFRAC.MIN POW-KIN-HERM-CREDR-OPTION POW-KIN-HERM-CREDnTAB POWýKIN-MERM-FLOW-REF POW.-KIN-HERM-MULT

POW-KIN-HERM.Y-FLOWR POWýKIN-HERM-POW-REF POW-KIN-HERM-TD

Index

767 768 688 782 783 781 793 794 792 700 727 701 702 703 723 704 705 730 692 775 772 744 717 745 788 787 706 728 707 741 719 726 710 712 714 722 716 774 771 719 708 676 679 677 681 682 680 816

Lom Variable Name

POW-KrNHERMrrE.INPLJT POW-KIKHERMrrE2ARAM POW.-K[NINP POVVý-KIN-MV(-CONSOLD POW-K[NMDCCONHOT POW.-K[NMDCING-INPUT POW-MMODý_DENSMYý-FB.OPTION POW-KrKMOD-DENSnYOPTION POW.-K[NMODLTEMP-FBQlynON POW.-KINMODDK POW-KIN_ýNCUTBACK POW-KINNDKCON POW-KINNDKCTM POW.-K[NNDKDEN POWý_KIN - NDKINS POW-K[NNDKTMP PO)K-K[NNQDK POWKINOUT POW-KIN-PLAM POW.-KIN-POWMFLOW-MAX POAý_KIN-POWrOFLOWMIN

POAý-KINQD2 POW-KIN-QDK POWKDLQF2 POWKINREG-ROD-OFYrION POWý-KIN-SCRAM-ýROD-OPTION

POIK-KIN-SIGD2 POIKK[N_$OURCE POINý-KINSTARL POW-KIN-STATE POWý-KrNff POW.-K[NWLFrBACK POW-KINTDKCON POW-K[NTDKC'rM POW-KrN-TDKDEN POW-KINTDKINS POW-KINTDKTMP POW.-M-TEMPffILIý-MAX POW.-KINTEMFý-TJLT-MIN POW-KINTQDK POW-KIN-TSS POW-USER-COMMON POWUSERIFUPOW POWUSERJNP POW-USER-NPOWr

POWUSERPOWr POWUSERPOWZ POW-USER-QAXL

Index

765 689 693 694 691 791 742 687 779 789 725 720 785 732 729 733 709 695 711 696 739 713 697 735 740 721 699 734 737 738 731 736 715 698 690 790 784 746 743 786 773 795 780 777 770 778 776 769



685

686

758

684

683

759

762

764

760

817

761

818

820

763

819

675

2547

2548

2549

189

187

1115

1172

227

837

1103

838

275

2552

1448

281

282

286

285

283

280

284

2553

564

2550

429

428

317

315

1352

1476

314

231

Long Variable Name

POWUSERQC

POWUSERQCD

POWUSERQCDLOOKUP

POWUSERSTATE

POWUSER.TPOWT

POWZRH2OCOMMON

POWZRH2OFZBJ

POWZRH20OH2M

POWZRH2O_INP

POW ZRH20_IZX

POWZRH20NYZIR

POWZRH2OPCZR

POWZRH20_QZRH2O

POWZRH20_STATE

POWZRH20_ZX

POWER-COMMON

PPRESNONC

PPRES-NONC TOT

PPRESSTM

PRESATWSMAX

PRESATWSMIN

PRESGLOB

PRESLAST

PRESN2

PRESPRED

PRES.QT

PRESS

PRESSLDN

PRESSSTMLAST

PRSIHEATERVOLT FRAC

PRZRHEATERMULT

PRZRPORV-MULT

PRZRQTMULT

PRZRRELIEFRTDTAU

PRZRSAFETYMULT

PRZRSPRAY MULT

PRZRVENT_ MULT

PTEMPSTM-SAT

MITAB

PVOLNONCTOT

QSGTBL

QSG100

QTFLOWFRAC

QTGWSM ULT

QTJ4_P

QTMODNPUTS

QTN2_MULT

QTRUPTURESPOINT

Index

316

1121

881

917

2543

2544

880

269

263

264

261

266

265

262

2362

1493

1345

368

1210

1301

1209

1346

1224

372

1331

358

357

371

1204

369

1302

1334

1206

367

362

1208

277

1303

1217

304

1225

1205

1226

1223

1213

303

305

1212


Lone Variable Name

QTVENTMULT

QUALGLOB

QUAL MIX

QUALMIX SECT

QUALNONCSEP

QUALNONCSEPTOT

QUALTOT

RATEDBUSVOLT

RATED_PUMPDENS

RATEDPUMP HD

RATEDPUMPSPEED

RATEDPUMP.SYNCH

RATEDPUMP.TORQ

RATEDVOL FLOW

RATIOCONCSOLU

RBINIT

RCPADMIFLOWCORR

RCPADMI-FLOWCORR_MULT

RCPADMIIM

RCPADMIMULT

RCPADMIRE

RCPAMPS

RCPBREAK

RCPCAVITLOADMULT

RCP CAVITSGDPFRAC

RCPCAVITSGDPFRAC-MIN

RCPCAVITSGDPMULT

RCPCAVITVIBRMULT

RCP.COMMON

RCPDELAMPS

RCPDELSPEED LOCKED

RCPDTLASTTRIP

RCPELECTRIC

RCP_-FLOW REF

RCPFRSP..RUBRATCH

RCPFREQ

RCPFREQRATED

RCPFRICCOEFF

RCPHEAT

RCPHEAT MULT

RCPHIVIB

RCPINTERNAL

RCPLOCKED

RCPMALFUNCTION

RCP_.MECHANICAL

RCPMOMINERTIA

RCPMOMINERTIA_SPLIT

RCPPF

G-243

Index

1312

1227

1228

1211

1222

309

1220

1219

1335

1353

1215

1216

1214

363

1336

1218

1221

307

306

308

1207

276

1451

1449

92

93

91

1378

2284

376

1399

1101

1100

301

950

927

160

137

975

997

1406

1402

1403

1405

1408

1409

1413

1412

Long Vari

RCP_.RCPS'

RCP_RCS_U

RCPSEALS_

RCP_.SLIP

RCPSPEED

RCP._SPEED.

RCPSPEED

RCPSPEED

RCP._STOPP]

RCPTBEAR

RCPTORQ_

RCPTORQ_

RCPTORQ_

RCP TORQ.

RCPfTRIPPE

RCP VIBR

RCPVIBR-t

RCPVIBR_

RCP.YVIBR j

RCP_VIBR'

RCPVOLT

RCPYOLT_

RCPiFREQ.

RCPLVOLT

RCSANNU]

RCS.ANNU]

RCSANNU

RCSAREA_

RCSBALA!

RCS_BHTR

RCSBORO)

RCSCEAJ

RCSCEAJ

RCSCEAIN

RCSCHGS_

RCSCHGS_

RCSCHGS

RCS-CHGS

RCSCHGS.

RCSCHGS_

RCS-CHTE

RCSCHT_E

RCSCHT_E

RCSCHT_F

RCSCHTL

RCSCHTL

RCSCHTj

RCS_CHTI


able Name Index Long Variable ?

TART 1401 RCS_CHTPRESS

EAK 1404 RCS-CHTQUAL

_LEAK 1407 RCSCHTQUALIN

1410 RCSCHTQWALL

DERWV 1411 RCSCHTTWALL

_DERIV_SHAKE 826 RCSCOMMON

MOTOR 1141 RCSCONC_BORO

PUMP 1142 RCSCONCHYD

ED 1143 RCSCONC_IOD

INGHIGH 1144 RCSCONCPART

ELEC 1140 RCSCONC_SOLU

FRIC 2538 RCSCONGSOLU

HYD 1145 RCS-CONC.XEN

_RUBRATCH 324 RCSCONDSURF

278 RCS_CONST

318 RCS_CONSTGEN

AMP 325 RCSCONSTLEA]

MAX 310 RCSCONSTLOO

NORM 279 RCSCONSTPRZI

.TPME 302 RCSCONSTPUM

313 RCSCONSTQT

RATED 293 RCSCONSTUHE

FRAC 311 RCS.CONT-HEAT

.FRAC 1040 RCSCORE

L_ASECT 1177 RCSCOREFLASI

L_HSECT 1294 RCS_COREHYD

L_NSECT 356 RCSCRIT_FLOW.

LBLAST 1256 RCSCRITMODE

NCE 2545 RCSCUMNONC

_RLD_MULT 2539 RCSCUMSOLU

NCORE 1052 RCSDELHHLTII

V 1360 RCSDELT

4ULT 1247 RCSDELT_-HEAT

_KTERM 1363 RCSDELTWALL

ENTH 1362 RCSDELTA_T

FLOW 1383 RCSDELTEM_SG

_PELEVIN 290 RCSDFLASH_MI

PNODEIN 1370 RCS_DHEATFAS

_QUAL 370 RCSDHEATFAS

_STM_UP 1371 RCSDHEATMA

NTHIN 1372 RCS_DHEATSTE

NTHLIQ 1305 RCSDHFMIN

NTHSTM 288 RCSDMFLASH

'LOWIN 1163 RCSDOSE_2HR

ýEVMIX 1164 RCSDOSE_8HR

LEVSAT 1156 RCSDOSEBF

AASSBUB 1157 RCSDOSECF

MASSLIQ 1161 RCS_DOSECON!


lame

N

TE

MULT

ERAL

KS

P

PS

"AD -MULT

H-LAST

RELMAX

,CHECK

L

ER

-_LB

ýX_PRZR

TT TI'UHEADFRAC

KFASTT

P._FAS'T

PRZR

D -DF

G-244

Index

1160

1155

1154

1162

1153

1158

1159

1306

1380

1325

322

1263

1310

1350

346

1311

373

1182

1354

1361

1387

1382

1264

1276

1368

1365

1246

1366

1292

1269

1369

1253

1364

165

142

1114

1266

1268

1384

1367

1381

1450

1286

1181

1236

1231

1319

1318

Table G.3:

Lone Variable Name

RCSDOSECONTLEAK

RCSDOSEFLASH

RCS_DOSE_INIT_IOD

RCSDOSEfTOTCURIE

RCSDOSE._VARIABLES

RCSDOSEXOQ2

RCSDOSEXOQ8

RCSDP_ELEVSURGE

RCS_DP_LEAK_LASTLLB

RCSDRAINSSDC

RCSDROPCONDMULT

RCSDTFOPENLB

RCSDWSDC

RCSDW SIT

RCSDWSOLIDSDC

RCSDWSTPSDC

RCSDWSTPSIT

RCSEQUILIBRIUM

RCS_FAILURESTATUS

RCS_FDELT

RCS_FLAG_COARSE_NODES

RCSFLAG DPLEAKLB

RCSFRAC_SIT_12B

RCS_FrIME-BUB

RCS-FTIMECVCS

RCSFTIMEHEAT

RCS_FTIME_HEATER

RCS_FTIMEPATHS

RCSFTIMEPRZR

RCSFTIMESDC

RCSJFTIME.SIT

RCS _FTIMESPRAYS

RCS-FTIMEWALL

RCSGASPELEV[N

RCSGASPNODEIN

RCS GLOBAL_AVERAGE

RCS_HSITCONT

RCS_H_SURGE_TAU

RCS-HAPRIM

RCSHEATJFAS1T

RCSHEAT_SGMAXLB

RCSHEATER.VOLT_BUS

RCS_HIGHPCOARSENODE

RCSHOMOGENEOUS

RCSICOUNT-FLOWLIM_P

RCSICOUNTMUKPR_P

RCSINITAIRPRZR

RCS_INIT_LEVEL_PRZR


Index Long Variable I 1317 RCS_INIT_P

1324 RCS_INIT_TLOOI

1323 RCS_[NIT_T_PRZS

1488 RCSJNrTIALCO1D

1482 RCSINPUTS_PRZ

834 RCSINTERNAL

2294 RCS_IOD_REL_RA

2293 RCS_IOD_RELJTO

321 RCS_ITERDH_NE

319 RCS_ITER_DP

320 RCS_ITER_DP_NE

1307 RCSITER_DPL

378 RCSK_TEMPCLI

323 RCS_KLOSSMUL

208 RCS-KWEIGHT_H

1260 RCS LEFFSPR

1373 RCSLARGEBRE.

1388 RCSLBLOCA_FI

1379 RCS_LB_SGDRAIV

960 RCSLBLOCA_EN

937 RCSLBLOCA_FL(

171 RCSLBLOCA_PE]

148 RCS_LBLOCA_PN'

985 RCS_LBLOCAQU

1007 RCSLBLOCA_STI

951 RCSLDNSENTH

928 RCSLDNSFLOW

161 RCSLDNSPELE\

138 RCS-LDNSPNOD

976 RCSLDNSQUAL

998 RCSLDNS_STM_I

289 RCSLEVLSAT_F

2363 RCS_LINPROP_US

1184 RCS_LOCAMAPP

1262 RCS-MAL038

1194 RCSMALFUNCTI

1275 RCS_MAX_BC_E¾

1270 RCSMAXCHGS

1326 RCSMAXDRAIN

1241 RCS_MAX_EXT_E

1272 RCSMAXLDNS

1271 RCSMAX_SIT

1273 RCS_MAX_WDRA

1274 RCSMAXWSDC

912 RCSMBUBSS

1240 RCS_MIN_EXT_Er 1414 RCS_MODINPUT

1415 RCSMODINPUT


Name

NDITIONS

-RRELIEF

TE

T

LOCA

T

TILT

AK

RST

rTh

)W

LEVIN

ODEIN

AL

-_UP

IN

EIN

UP

?RZR

ER

ING

ON

LSDC :NTH

IN

NTH

"S "SBOP

I

G-245

Index

1474

1452

1431

1447

1390

1400

1396

1391

341

1330

1238

1239

1257

1285

1290

1295

1298

1309

1315

2286

2287

1355

2285

897

900

883

839

847

70

868

40

876

842

39

64

836

87

59

854

906

879

860

76

32

835

2527

2572

2540

Lone Var

RCSMOD_

RCS.MODI

RCSMOD_

RCSMODL

RCSMOD_

RCSMOD_

RCSMOD_

RCSMOD_

RCSMORE

RCSMORE

RCSMORE

RCSMORE

RCSMORE

RCSMORE

RCSMORE

RCS-MORE

RCSMORE

RCSMORE

RCSMORE

RCSNETI

RCSNETI

RCSNEVE

RCSNODA

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCS-.NODE

RCSNODE

RCS-NODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNODE

RCSNONC

RCSNONC

RCSNONC



iable Name Index Lone Variable 1•

INPUTS_CONT 2556 RCSNONCOND_P

INPUTS-MALFUNCTIONS 1230 RCS NSTEPCALC

INPUTSVLVCONTR 1237 RCSNUM_FLOW.

INPUTS3VOLTCONTR 2364 RCSNUMLINPR(

OUTPUTS 25 RCSNUMMSPRA

OUTPUTSCHT 1232 RCSNUMMUKPT

OUTPUTSCORE 26 RCSNUMPORVS

OUTPUTSINSTRUM 27 RCSNUMSAFET

YVARIABLES_504_RO 108 RCSNUM1NCHG

_VARIABLES_504_SR 112 RCSNUMINSIS

_VARIABLESA 114 RCSNUMMAX_C]

.VARIABLES_I 116 RCSNUMMAX_D

_VARIABLES_II 115 RCSNUMMAX_LI

.VARIABLES-11 119 RCSNUMMAX_M

_VARIABLESJIIA 113 RCS_NUMMAX_Ri

*_VARIABLESIIIB 117 RCSNUMMAX_SI

*_VARIABLES-IV 118 RCSNUMMAX_SI

YVARIABLESV 109 RCSNUMOUTL1

..YARIABLES_VI 110 RCSJNUMOUTR(

EXTFLOW 11 RCSNUMOUTSE

HEAT-RATE 1229 RCS_OPTIMIZATI

RSTOPAUTO 959 RCSORINGENTI

LEXTFLOWS 1344 RCS-ORINGFAIL

",-BUBBLES 936 RCSORINGFLO•

"-CONDENSATION 170 RCSORINGPELT

.DERIVATIVES 147 RCSORINGPNO]

,_ENERGIES 984 RCSORINGQUA

-ENTHALPIES 1006 RCSORINGSTM

.GEOMETRY 1130 RCSP_BORON

*_HEATRATES 1234 RCS_P_CONDUCT

*-HL 156 RCSPELEVJNL

LLEVELS 157 RCSP_ELEVINL

-MASSES 1304 RCS_P_ELEVMO

,NUMBERS 946 RCS_PENTH_MO

.-OTHERS 947 RCS_PENTHNO

'_PRESSURES 923 RCSP_FLOW_M(

..SECTIONALIZED 924 RCS_PFLOW_NC

-_SL 1200 RCS_P_FLOW_PO

-SPECVOLUME 1203 RCS_P_FLOW_PR

'.STATES 1081 RCS-PFLOWPI

-_STEAMFRAC 1201 RCS_P_FLOW_SA

-_TEMPERATURE 1131 RCSPHYD

.-TH_VARS 1135 RCSPHYDAU

,-TOTALS 1132 RCS_P_IOD

-.-VARIABLES 1136 RCS_P_IODAUX.

ONDCONSTANTS 133 RCS_P_NODEIN

.OND_[NTERF 134 RCS_P_NODE_INI

ONDNODES 1343 RCSP_ORING

game

ATHS

ULATIONS

IMP

VP

YVLVS L P

•VLVS

S

HGSIN

RAINSOUT

DNSOUT

OM

CP

DCOUT

[SIN

)NS

-WDRAINS

)C

ON

VIN

DEIN

L

_UP

ETMOM

ET_NONM

D_SURGE

NM )M NM DM

WNM

RV

ZRQT1

ZRQT2

FETY

ý_SPRAY

-SPRAY

LETMOM

LET_NONM

G-246

I


366

1133

1137

1235

971

972

1129

1245

993

994

1233

1134

1138

1165

1024

944

921

1014

969

1027

920

948

925

158

135

973

995

961

938

172

149

986

1008

955

932

166

143

980

1002

131

97

120

98

375

360

1054

89

1337

,Long Variable Name

RCS-Pý-ORING-FAIL RCS-Pý-PART RCS-R-PARTý-AUX-SPRAY RCS-Pý-PRANDTL RCS-Pý-QUMMOM RCSJý-QUAINONM RCSJý-SOLU RCS-Pý-SPIKELOUTPUT RCS-Pý-STM-UP-MOM RCS-Pý-STM-UPLNONM RCS-Pý-VISCOS RCS-PLXEN RCS-PLXEN-AUX-SPRAY RCS-PAST-VALUES RCS-PATH-DERIVATIVES RCS-PATH-ENTHALPIES RCS-PATH-FLOW-RATES RCS-PATH-PRESS-DROPS RCS-PATH-QUALMES RCS-PATH-UPDOWN RCS-PATH-VARIABLES RCS-PATHEXTý-ENTH RCSý-PATHEXTý-FLOW RCS-PATHEXT-PELEWN RCS-PATHEXT-PNODEIN RCS-PATHEXIý-QUAL RCS-PATHEX7ý-STM-UP RCS-PATHINT-ENTH RCS-PATHINTý-FLOW RCS-PATHINTý-PELEVIN RCS-PATHIN7ý-PNODEIN RCS-PATHWIý-QUAL RCS-PATHINTý-STM-UP RCS-PATHLEAK-ENTH RCS-PATHLEAK-FLOW RCS-PATHLEAK-PELEVIN RCSLPATHLEAK-PNODEtN RCS-PATHLEAK-QUAL RCS-PATHLEAK-STM-UP RCS-PATHS-GEOMErRY RCS-PATHS-NODALIZATION RCS-PATHSLNUMBERS RCS-PATHS-TX)TALS RCS-PM-RLDý-MULT RCS-PRES-COARSEý-MAL034 RCSLPRESSURIZER RCSý-PRZR-ASECT RCSLPRZR-CONDLSURF

Index

1289

1242

342

1299

1332

1300

344

1342

287

1254

1199

1327

364

1291

90

1288

1328

1329

351

1283

1297

1338

1281

365

1314

1313

359

88

1082

2568

1340

2567

1341

1322

964

941

175

152

989

1011

2534

343

1339

345

1293

347

350

377

Long Variable Name

RCS-PRZR.CONDý-WALL

RCS-PRZR.CONTý-HEATý-MULT

RCS3RZILDHSPRAY-EQ

RCS-MR-D7ý-BOIL

RCS-MR.DrIý-SUB-BOIL

RCS-MR-DTý_SUBC

RCS-PRZR.DTý_SUBH

RCS-PRM-DTý-SUBSS

RCS-PRZR.FLASKMULT

RCS-PRZR-FLASH-TAU

RCS-PRZR-FLOW-VALVES

RCSý-PRZR.FRAQ-AIR

RCS2RZR-HAX-WALL

RCS-PRZRýHLIQ-MULT

RCS-PRZR-HSECr

RCSýPRZR-HWALLIý-MULT

RCS-PRZR-KHSTM

RCS-PRM-KPý-SIM

RCS-PRZR-IýBOIL

RCS-PRZRJýCONDLOFF

RCSýPRZR-LEVEL

RCS-PRZR-LEVL-LAST

RCS-PRZR-LOWPý-COND-LOG

RCSýMR.LVLDTý-SUBC

RCSýPRZR-MASS-AIR

RCS-PRZR-MASS-STM

RCS-PRZR-MSPRAYTAU

RCS-PRZR-NSEC'r

RCS-PRZR-PRES

RCS2RZR-Q-COND

RCS-PRZR-Q-CONT

RCS-PRZRQEFF

RCS-PRZP.-QAX-WALL

RCS-PRZR-QUAL-RELIEF

RCS-PRZR - RELIEFENni

RCS-PRZR - RELIEFý-FLOW

RCS-MR-RELIEF-PELEVIN

RCSý-PRZR.RELIEFý-PNODEIN

RCSý-PRZR-RELIEFý-QUAL

RCS-PRZR-RELIEFý-STM-UP

RCS-PRZR-SPR-GAS - ENTR RCS-PRZR-SPRAY-EQ

RCS-PRZR.C-WALL

RCS-PRZR-TALLDTSUB

RCSjRZR.TREFý-TAU

RCSý-PRZR-VEN'LRIG

RCS-PRZR.VENT-RIG-FRAC

RCSý-PRZR-VLV-LVIB-MULT


Table G.3: Alphabetized Index of L

LDng Variable Name

RCSJRZR-VLV-REVH-:rAU RCS-PRZR-VLVH-MAX-TAU RCS-PUMPS RCS-Q-CEA-CORE RCS-Q-CEA-COREýMULT RCS-Q-ýUHEAD-CORE RCS-QUALMIN-ýNE RCS-QUENCFLTANK RCS-ýRCPý-CAVITAT RCS-RCP-SVOL RCS-RCPYOIDF RCS-RCPLEAK-ENTH RCS-RCPLEAK-FLOW RCSRCPLEAK-PELEVIN RCS-ýRCPLEAK-PNODEIN RCS-RCPLEAK-QUAL RCS-RCPLEAK-STM-ýUP RCS-RCSLBfflRST RCS-RCW-ENTH RCS-RCW-ýýOW RCS-ýRCWJELEVIN RCS-ýRCW-PNODEIN RCS-ROVý-QUAL RCS-ROVý-STM-UP RCS-REINMALIZE RCSý-RELE-NONC RCS-ýRELIý-PRIME RCS-RELEýSOLU RCS-RELEýSOLUSORE RCS-RODEJ3NTH RCS-RODEJ-FLOW RCS-RODEJ-PELEVIN RCS-RODEJ-PNODEIN RCS-RODEI-QUAL RCS-RODEJ-STM-UP RCS-SBLOCA3NTH RCS-SBLOCA-FLOW RCSýSBLOCA-PELEVIN RCS-SBLOCA-PNODEIN RCS-SBLOCA-QUAL RCS-SBLOCA-STM-UP RCS.SDCý-ENTH RCS-SDCý-FLOW RCS-$DQ-PELEVIN RCS-SDC-PNODEIN RCS-SDQ-QUAL RCS-SDQ-STM-UP RCS-SDCSrr-CONSIS*r-TEST

riable Names

Long Variable Name

RCS-SEARCH-n-ER

RCS-SEARCILTYPE

RCS-SECTý-NODE.VARIABLES

RCS-SG-W-ADD

RCS-SGLDFý-MULT

RCS-SG-DPý-W-MULT

RCS-SG-NSECT

RCS-SCL-SEC71ý-DH

RCS.SG-SEC7r-DW

RCS-SG-SECr-ENTH

RCS-SG-SECT-ýý

RCS-SG-SECT-LW

RCS-SGLSECTYRESS

RCS-SQ-SECr-QP

RCS-SG-SECT-QS

RCS-$G-SEC7r-:rEMP

RCS-SG-SECr-TOP'r

RCS-SG-SECLTrUBE

RCS-SGI112-DPý-ADD

RCS-SG1112-DP-ýýMULT

RCS-SGTR3N-rH

RCS-SGTR-FLOW

RCS-SGTR-FLOWMULT

RCS-SGTR-PELEVIN

RCSýSGTR-PNODEIN

RCS-SGTR-QUAL

RCS-SGTR-STM-UP

RCS-SIS-ýENni

RCS-SIS-ýýOW

RCS-SIS-PELEVIN

RCS-SIS-YNODEIN

RCS-SIS-QUAL

RCS-SIS-STM-UP

RCS-SOLUTE

RCS-SPECtES-CONSTANTS

RCS-SPECIES-CORE

RCS-SPECIES-NODES

RCS-SPEC[ES3ATHS

RCS-SPRAY-DELH-ýDEG

RCS-SPRAYý-EFF

RCS-SPRAY-EFF-MULT

RCS-SPRAY-EFFI

RCS-SPRAY-EFF2

RCS-SPRAYý-ENTH

RCS-SPRAY-FLOW

RCS-SPRAY-PDEQ-TERM

RCS-SPRAY-PELEVIN

RCS-SPRAYý-PNODEIN

ong Va

Index

1185

1186

911

352

1287

354

1498

1499

1500

1510

1501

1502

1507

1504

1505

1503

1509

1506

353

355

956

933

312

167

144

981

1003

954

931

164

141

979

1001

1128

2511

2570

2535

2554

1277

1258

1259

1278

1280

962

939

1284

173

150

Index

374

361

1034

1050

297

1053

1282

1102

1348

1347

1333

949

926

159

136

974

996

1389

952

929

162

139

977

999

1316

1139

913

1146

1147

958

935

169

146

983

1005

957

934

168

145

982

1004

953

930

163

140

978

1000

1308


Index

1279

987

1009

963

940

174

151

988

1010

2365

2366

1178

1032

1356

1357

327

326

1261

1351

1386

1385

1358

1359

2289

2291

2288

916

1255

1099

965

942

176

153

990

1012

298

348

349

1086

1188

1189

914

915

1296

1320

1321

1349

1265

Long Vari

RCS_SPRAY

RCSSPRAY

RCS-SPRAY

RCSSPRAY

RCS._SPRAY

RCS_SPRAY

RCS-SPRAY

RCSSPRAY

RCSSPRAY

RCSSSCO

RCS_SSUSF

RCS_STATU

RCSSTEAM

RCSSTEPJ_

RCS_STEPR

RCS-SUBCR

RCSSUPERI

RCSSUR(

RCS._TEMNP..

RCSTEMP_.

RCSTEMP_

RCSTIME_C

RCSTIME_S

RCS_TOTAL

RCS_TOTAL_

RCSTOTAL_

RCS_TRANS

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUHEAD

RCSUPPER_

RCSVALVES

RCSVLV AR

RCSVOID_T(

RCSVOID Tj

RCSVOLT_H

RCS_WPRZR

RCS_WPRZR

RCS_WSIT

RCSW-SrITc

Table G.3: Alphabetized Index of Long Variable Names able Name Index Long Variable I '_PRESDEG 1392 RCSL_PMPI-DP '_QUAL 1393 RCSL_PMP2_DP ._STMUP 1394 RCSLPMP3_DP 'BLEEDENTH 1395 RCSLPMP4_DP BLEEDFLOW 1479 RCWQTFLOW BLEEDPELEVIN 1425 RCWRCSFLOW BLEED PNODEIN 898 RELEBUB BLEEDQUAL 216 RESILHEATER BLEEDSTMUP 1494 RKPUMP NTROL 1490 RLINIT ER 1489 RPINIT S 1495 RSINIT [LGENERATOR 1492 RTCLIN FAILURE 207 RTRV_BYPASS RECOVERY 296 RTRVHEADSEAI IT_FLOW MULT 294 RTRVJKLOSSCOF CRITFLOWMULT 299 RTRVMIXINLET GE_TAU 300 RTRVMIXOUTLI

L12B 295 RTRV.VENTMUL .GLAST 431 RTUBES SG-PRE IIII RUPTUREQT •ONTROL 1491 RWINIT CALE 1522 SBDELTA-ELEV ENERGY 1517 SBLOCAPIPE_DA

.IODINE 1518 SBPIPEAREA ,_MASS 1521 SBPIPE KENT _CORR 1520 SB_PIPE_KGEOM _CONTHEATMULT 1519 SBPIPELOD _PRES 2273 SCRAMDELAY _RELIEFENTH 1426 SDCRCSFLOW -RELIEFFLOW 1119 SENGGLOB .RELIEFPELEVIN 565 SEQNCE _RELIEFPNODEIN 403 SFCONC_10 .RELIEFQUAL 381 SGDESIGN RELIEFSTMUP 424 SGECONOMIZER RINGSEALMULT 434 SGHCONV VENTRIG 414 SGHT4_MAX VENTRIGFRAC 418 SGREFBOT

HEAD 416 SG REF LEGS

417 SG_REF._NUM •EA 419 SGREFTOP

P 435 SGRWALL RAN 422 SG_TUBEAREA TRBUS 1496 SG_TUBESECTION CONT 404 SG-U12

,-QT 405 SGLU23

406 SGV2_ACTIVE ONT 407 SG'V4_MAX


Name

LMULT RE

IT

TA

4S

I

G-249


Index Lone Variable Name Index Long Variable Name

408 SG.V5_.MAX 1827 SGBD_SINKFLOW

498 SGBDACROSS 1833 SGBDSINKIO

505 SGBD BOT-COEFF 1842 SGBDSINKP

1814 SGBDBOT.,ENTH 1824 SGBDSINKPOS

1811 SGBDBOTFLOW 1836 SGBD_SINKPT

508 SGBD BOT HTNOZ 1839 SGBD_SINKXE

1817 SGBD-BOT_1O 504 SGBDSURFCOEFF

1808 SGBDBOTPOS 1813 SGBDSURF_ENTH

1820 SGBDBOT_'T 1810 SGBD_SURFFLOW

1823 SGBDBOTXE 507 SGBDSURFHTNOZ

1788 SGBDCON-1O 1816 SGBDSURF_.10

1789 SGBDCONT 1807 SGBD_SURFPOS

1790 SGBDCON)XE 1819 SGBDUSURFPTf

1791 SGBDDVDH 1822 SGBD_SURF._XE

1792 SGBD DVDP 1800 SGBDSV

1793 SGBDJH 1801 SGBD_SVF

1794 SGBDHF 1802 SGBDSVG

1795 SGBDHG 1803 SGBD_T

1796 SGBDL 1804 SGBDTWALL

1797 SGBDM 502 SGBDYOL

1798 SGBD_-ML 1805 SGBDX

510 SGBDOUTCOEFF 432 SGMTCP

1831 SGBDOUTENTH 2281 SGSALPHADOWNCOMER

1828 SGBD.OUTFLOW 2280 SGSAREADOWNCOMER

509 SGBDOUTHTNOZ 1850 SGS_ASEPTUNE

1834 SGBDOUT.I0 1543 SGS_BOT_P

1843 SGBDOUTP 1541 SGSCOMMON

1825 SGBDOULTPOS 1550 SGS_CON_BORONI

1837 SGBDOUTPT 1551 SGSCONBORON2

1840 SGBQDOUTXE 1544 SGS_CON_101

1799 SGBDP 1545 SGSCON_102

511 SGBDRELIEFAMAX 1546 SGS_CONPTi

1832 SGBDRELIEF ENTH 1547 SGS_CONPI2

1829 SGBDRELIEFFLOW 1548 SGSCONXE1

1835 SGBDRELIEF_10 1549 SGSCONXE2

1844 SGBDRELIEF._P 1881 SGSCRIT_MODEL

1826 SGBDLRELIEFPOS 2278 SGS_DEBUG_SGHEAT

1838 SGBD RELIEF_-PT 2277 SGSDEBUG_SGSINI

1841 SGBDRELIEF._XE 1552 SGS DELTV

503 SGBDLSGCOEFF 1851 SGSDELTVMAX

1812 SGBDSGCENTH 1553 SGSDP

1809 SGBDSGFLOW 1554 SGS_DVDP

506 SGBDSGHTNOZ 1560 SGS_El

1815 SGBD_SG_10 1561 SGS_E2

1806 SGBDLSG yOS 1562 SGS.E3

1818 SGBDSGPT 1563 SGS_E4

1821 SGBDSGXE 1564 SGS_ES

1830 SGBD-SINKENTH 1901 SGS_ECONASUB


Index

1903

1904

1902

1899

1900

1897

1898

1896

1555

1556

1557

1558

1559

1852

1632

1853

1854

1725

1855

1633

1643

1565

1566

1567

1568

1569

1570

1883

1542

1571

1572

1573

1574

1575

1890

1891

1882

1508

1576

1856

1857

1644

1645

1646

1577

1858

1859

1578

Lone Vari

SGS_ECON_

SGS-ECON

SGS_ECON{

SGS_ECON

SGSECON

SGSECON

SGS_ECON

SGS_.ECON_'

SGS_ENTHI

SGS_ENTH2

SGS-ENTH3

SGSENTH4

SGSENTH5

SGS_FK3TJ1

SGS_FLOW_

SGS_FTIME

SGS_FTIME_

SGSFWS

SGSHASUB

SGSHEAT

SGSHEAT_

SGSHF

SGSHG

SGSHLEVE

SGS_HT2

SGS_HT3

SGS_HTI

SGS_INITIAl

SGSINTER!

SGS_Ml

SGS_M2

SGS_M3

SGSM4

SGSM5

SGS_MASS_

SGS_MASS_

SGS-MORE

SGS_NSECT

SGSP

SGS_PCNVR

SGS_PMIN

SGSQCON

SGS_QWAL

SGSQWAL

SGS_RECIRC

SGS_RECIRC

SGSRECIRC

SGS_RHOI

Table G.3: Alphabetized Index of Long Variable Names able Name Index Long Variable CNVRG 1579 SGS-RHO2 FLIM 1580 SGS-RHO3 TCAV 1581 SGS-RHO4

.TFIN 1582 SGSRHO5 *TFOUT 1860 SGS_SEP_PMIN :MIN 1787 SGS_SGBD TPOUT 2283 SGSSTEAM VEL3 YARS 1647 SGS-STEAMLINE

1583 SGSSVI

1584 SGSSV2

1585 SGS_SV3

1586 SGS_SV4

1587 SGS_SV5 UNE 1590 SGS_TI CHOKED 1591 SGST2

1592 SGST3 PMAX 1593 SGST4

1594 SGST5 -OPTION 1879 SGS_TAUFLOW

1863 SGS_TAU_WOUTS' LOAD 1861 SGS-TAURCITUIN

1862 SGS_TAURC2.MA2

2292 SGS_TOTAL1_IODl? L 1588 SGS_TREFLG

1888 SGS-TUBEAREA_

1889 SGS-TUBEAREA

1846 SGSTUNE LCONDITIONS 1589 SGS-TWALL NAL 1864 SGS_UADROP_PEIR

1865 SGS_UADROP..WF

1595 SGSUSTM

1866 SGSUSTMMIN

1602 SGS.V1

1603 SGSV2 FULLTUBEAREA 1604 SGS_V3 ZEROTUBEAREA 1605 SGS_V4

VARIABLES 1606 SGSV5

1867 SGSVCNVRG

2282 SGSVEL31-MULT G 1596 SGS_VF

1876 SGS_VYREF T 1597 SGS3VF2 LLI 1598 SGSVF3 U13 1599 SGS_VF4

1600 SGSVF5 DELVOL 1601 SGSVG

-MIN 1877 SGS_VGREF

1878 SGSVLEGREF


4ame

G

lE

NE

DEGRAD

.OPTION

•IM

DMIN

I

G-251

Index

1617

1618

1619

1623

1620

1621

1625

1622

1624

1607

1608

1609

1610

1611

1868

1612

1613

1614

1615

1616

1626

1627

1628

1869

1629

1630

1631

1880

1870

1871

1872

1873

433

2275

1874

1636

1638

1634

1637

1639

1635

1641

1642

1640

1514

1511

1516

1515

Long Vari

SGS-W13

SGSW21

SGS_.W23

SGSW25

SGSW31

SGSW32

SGS.W42

SGS-W51

SGS_.W53

SGSWFI

SGS.WF2

SGSWF3

SGS_WF4

SGSWF5

SGSWFMI?

SGSWGI

SGS_.WG2

SGSWG3

SGSWG4

SGS_)WG5

SGSW)OU¶

SGSXI

SGSX2

SGSX2_I

SGSX3

SGSX4

SGSX5

SGSXTAU

SGT_HTCR

SGT_..HTCR

SGT_.HTCS(

SGTHTCS'

SGTHYD_

SGTjNITJ_

SGTQMU

SGTRCS_

SGTRCS_

SGTRCSj

SGTSGQ

SGTSGQ

SGTSG=Q

SGT_.TEMP

SGTTEM.

SGT_,TEM.

SGTRBRE

SGTRDAT

SGTR.SLO

SGTRSLO


able Name Index Long Variable N

1513 SGTRTUBE_ENTR

1512 SGTRTUBELENG

1430 SLTANKFLOW

1429 SISRCSBORON

1428 SISRCSENTH

1427 SISRCSFLOW

2574 SISRCSNONC

2575 SIS IRCSNONC

2576 SIS2_RCSNONC

2577 SIS3_RCSNONC

2578 S1S4_RCSNONC

2579 SIS5_RCSNONC

2580 SIS6_RCSNONC

1887 SKAMUL

2361 SLFLOWCOEFF

1685 SLP_FLOW

458 SLICHECKVALV

459 SLIDP100

444 SLI_FLOW_COEFF

1885 SLINIT

SG 919 SLIPSECT

271 SLIP_TAB

460 SLODPI00

445 SLOFLOWCOEFI

11 SNAPSHOT_-DATE

8 SNAPSHOTFILE_]

7 SNAPSHOT-LABE'

FLOW 10 SNAPSHOTIME

TC 9 SNAPSHOTTITLE

TH 401 SPACE

CW 1035 SPEEDPUMP

TM 1884 SPINIT

DIAM 1671 STEAMLINESTA

)PTION 866 SUBCLIQ

.LT 1047 SVOLDOWNCON

.COLD 1120 SVOLGLOB

?ECON 856 SVOLLIQ

QHOT 858 SVOLLIQSAT

COLD 1124 SVOLLIQ. SATC3

ECON 857 SVOLSTM

HOT 859 SVOLSTMSAT

'-COLD 1125 SVOLSTMSAT_

-_ECON 855 SVOLTOT

?_HOT 1092 SVOLUHEAD_TC

AKELEV 585 TABMAX

*A 410 TAU_10

)T_BREAKAREA 411 TAUPT

TBREAKOPT 420 TAUREFLGDN


ame ANCE.K

TH

E

F

NAME ,L

rE

IER

3LOB

GLOB

DP

G-252

Table G.3: Alphabetized Index of Long Variable NamesIndex Long Variable Name

421 TAUREFLG_UP

412 TAUXE

409 TAURCI

2217 TBASE

391 TBL2_NUM

398 TBL3_NUM

867 TEMP._CONT

1059 TEMPHEATER

862 TEMPLIQ

2551 TEMP.NONC

1063 TEMPPRZRREF

1065 TEMP_PRZRRTD

1064 TEMPPRZR.SURGE

1109 TEMP_.QT

1110 TEMPQTSURGE

864 TEMPSAT

1126 TEMPSAT GLOB 863 TEMP_-STM

861 TEMPTOT

1077 TEMPVALVERELIEF

865 TEMPWALL

602 TGAPIN

2218 TIME

2219 TIME SCALE

2222 TIMQUE

430 TMP_TBL

217 TOPHEATERS

1037 TORQPUMP

272 TORQTAB

2220 TSTOP

568 UNUSED

446 UNUSEDFLOWCOEFF

14 UNUSEDyVARPLT01

678 UNUSEDVARPOWO1

2272 USERCOMMON

395 V3_TBL

396 V3_TBLDSGNI

397 V3JTBLDSGN2

2358 VATTENFALL_MISCELLANEOUS

447 VELIOO

1076 VIBRVALVERELIEF

1438 VLV_PRZRCONT

1484 VLV_PRZRFLOW_OPTION

1486 VLVPRZRFLOWTABLE

292 VLVPRZRKLOSSDOWN

291 VLVPRZRKLOSS_UP

1437 VLVPRZRMOV

1440 VLVPRZR-MSPRAY

Index

1445

1485

1435

1446

1085

1084

1487

1439

1483

1436

1442

1441

1443

1432

1444

1433

1434

882

910

448

413

1055

218

1094

228

388

389

390

415

436

437

466

268

215

84

85

566

567

822

Lone Variable Name

VLVPRZRMSPRAYSIG

VLVPRZRNPOINTS_TAB

VLV_.PRZRPORV

VLVPRZRPORV_SIG

VLVPRZRPRESDOWN

VLVPRZRPRES_UP

VLVPRZRPROPTABLE

VLVPRZRQT

VLVPRZRQUALDF

VLV PRZRSAFETY

VLVQTCONT

VLVQTGWS

VLVQTNSUPPLY

VLVRCS_POS

VLVRCSSIG

VLVJUHEADCONT

VLVUHEADQT

VOIDFRAC

VOL MIX

VOL MSLH

VOLSGS

VOLT HEATER

VOLTHEATERMAX

VOLUNONUHEAD

VOLUQT

VSTTBL

VST_TBLDSGNI

VST_TBL_DSGN2

W32-FLOWCOEFF

WALLAREA

WALL MCP

WFWIOO

WINDTORQMULT

XFERHEATER

XFERSURFPOFF

XFERSURF._PON

XTAB

YTAB

ZSHAPIN


Table G.4: Alphabetized Index of Short Variable Names

Index Short Variable Name

92 AANN

2281 ALPHA3

89 APZR

94 ASECVA

399 ASEPSG

440 ASLMAX

461 ASLMIN

383 ASPTBI

384 ASPTB2

382 ASPTBL

237 BAD

235 BAN

241 BAR

239 BAT

238 BVD

236 BVN

242 BVR

240 BVT

2178 CAAUTO

2174 CADELA

2173 CADPHI

2175 CAFMUL

2168 CAFWS

2172 CAGMAX

2171 CALMI

2170 CALLO

2177 CAMOTR

2169 CASET

2179 CASSIG

2176 CATURB

1991 CAUTO

2130 CBAUTO

2124 CBDELP

2214 CBLOCK

2129 CBMODE

2128 CBNCLS

2126 CBNOPN

2123 CBPOPN

2127 CBQCLS

2125 CBQOPN

2122 CBSET

2121 CBYPAS

2017 CCAUTO

2022 CCAVAL

1978 CCEA

2031 CCENTH

2029 CCFLOW

2016 CCFPMP


2021 CCFVAL

2009 CCGRAT

2005 CCLSP1

2006 CCLSP2

2007 CCLSP3

2008 CCLSP4

2018 CCPMPO

2004 CCSET

2030 CCTEMP

2020 CCVALV

1995 CCVCS

2120 CDAUTO

2367 CDCONT

2247 CDELAY

2267 CDFrRP

2256 CDGRCS

2270 CDGRTR

2261 CDGSGM

2269 CDGSTR

2265 CDGTRP

2266 CDITRP

2253 CDLPHI

2260 CDLSGH

2259 CDLSGL

2271 CDMISC

2264 CDMIST

2262 CDPCHI

2249 CDPOHI

2252 CDPPHI

2251 CDPPLO

2258 CDPSGL

2268 CDQTRP

2118 CDSET

2257 CDSIAS

2250 CDSRHI

2254 CDTMAR

2248 CDTR[P

2119 CDTSP

2117 CDUMP

2263 CDUSER

2255 CDWMAR

2077 CEAUTO

2081 CEBHLP

2083 CEBSIT

2057 CECCS

2088 CECGAS

2076 CEDEL

2060 CEDPSL


2086 CEELEV

2087 CEFLCO

2066 CEGHPS

2071 CEGLPS

2082 CEHHLP

2068 CEHNUM

2084 CEHSIT

2230 CEINIT

2091 CEIVAL

2073 CELNUM

2080 CEMISC

2065 CENHPS

2070 CENLPS

2085 CENSIT

2061 CEPCHI

2067 CEPHPS

2059 CEPLO

2072 CEPLPS

2089 CEPSIT

2063 CEPSLL

2058 CESET

2069 CESHPS

2064 CESIS

2092 CESLIQ

2074 CESLPS

2062 CETAVL

2321 CETOPC

2078 CETRP

2079 CETRPP

2075 CETRPT

2090 CEVGAS

2093 CEVLIQ

2151 CFAUT

2152 CFAUTO

2143 CFDELA

2154 CFEAUT

2148 CFEMAX

2147 CFENTH

2149 CFETC

2144 CFGMAX

2141 CFLHI

2140 CFLLO

2139 CFLPRG

2155 CFPAUT

2142 CFRAMP

2138 CFSET

2164 CFSFRC

2165 CFSMAX


2145 CFSMUL

2163 CFSSIG

2156 CFrAUT

2146 CFrLO

2150 CFTRP

2153 CFVAUT

2167 CFVBYP

2162 CFVEPO

2159 CFVESI

2166 CFVISO

2161 CFVPO

2160 CFVPOS

2158 CFVSI

2157 CFVSIG

2137 CFWS

2105 CGCAUT

2103 CGFDEM

2104 CGGRAT

2106 CGLOAD

2189 CGRAUT

2191 CGRTRP

2188 CGSAUT

2186 CGSCON

2099 CGSET

2187 CGSSET

2190 CGSTRP

2108 CGTAUT

2100 CGTCLS

2107 CGTRP

2109 CGTRPP

2102 CGTRPT

2101 CGVTC

2044 CHAUTO

2032 CHEATR

2034 CHLBSP

2035 CHLOFF

2038 CHPBOF

2039 CHPBON

2036 CHPPOF

2037 CHPPON

2040 CHPREF

I CHR

2033 CHSET

589 CHT

664 CHTAXA

652 CHTAXB

671 CHTSEO

646 CHTAXF


Table G.4: Alphabetized Index of Short Variable NamesIndex Short Variable

Name

645 CHTAXL

590 CHTINP

605 CHTNUM

2233 CHTOFF

607 CHTPRP

633 CHTSTr

2042 CHVBAK

2041 CHVPRP

2043 CHVRAT

2115 CIAUTO

2114 CIGSLO

2225 CINCON

2113 CIPCHI

2112 CIPSLO

2111 CISET

2116 CITRP

1974 CKAUTO

1975 CKTRP

1977 CKTRPP

1976 CKTRPS

1968 CKTRPT

2019 CLAUTO

2227 CLCONT

2027 CLENTH

2239 CLEVEL

2241 CLEVP

2240 CLEVSG

2025 CLFLOW

2028 CLFRAC

2003 CLGSP

2002 CLLSP

2001 CLSET

2026 CLTEMP

2110 CMSIS

1973 CNRPS

1965 CODTUR

1959 COGRCS

1964 COGSGM

1956 COLPHI

1963 COLSGH

1962 COLSGL

2236 CONOFF

2243 CONT

1966 COPCHI

1952 COPOHI

1955 COPPHI

1954 COPPLO

1961 COPSGL


196 CORBOT

796 CORE3D

1969 COREQ

2279 COREQA

1970 COREQT

2318 CORHFR

2237 CORINI

197 CORTOP

2316 CORWO

2317 CORWFR

1960 COSIAS

1953 COSRHI

1957 COTMAR

1967 COUSER

2203 COUT

2212 COUT3D

2211 COUTCL

2206 COUTCT

2209 COUTFI

2208 COUTGR

2204 COUTIN

2210 COUTLO

2205 COUTOP

2207 COUrT1

1951 COVER

1958 COWMAR

2012 CPLERR

1998 CPLEV

2013 CPLINS

2011 CPLPRG

1972 CPOWFL

1971 CPOWFR

2010 CPPROG

1996 CPSET

1999 CPSLIQ

2000 CPSSTM

1997 CPTEM

2182 CQAUTO

2181 CQSET

2183 CQTRP

2184 CQTRPP

2185 CQTRPT

1993 CRACCM

2514 CRATIO

1982 CREXP

1984 CRFPOS

1983 CRGAIN

1986 CRMAX


1987 CRMIN

1985 CRMOTL

2180 CRPCS

1992 CRPERF

1988 CRPOS

1979 CRSET

1989 CRSPD

1994 CRSPDL

1990 CRSTEP

1981 CRTFUL

1980 CRTNO

2131 CSAFE

2136 CSAOPN

2135 CSCLOS

2094 CSDCCN

2095 CSDCDH

2096 CSDCHM

2097 CSDCSP

2192 CSETPT

2134 CSFULL

2133 CSOPEN

2213 CSPAR2

2228 CSPARE

2045 CSPRAY

2132 CSSET

2014 CTAVG

1927 CTCONT

1942 CTDTUR

1945 CTGKSP

1936 CTGRCS

1948 CTGSBY

1941 CTGSGM

674 CTHHOP

2202 CTIMCN

1926 CTIME

1925 CTL

573 CTLDBG

584 CTLMAX

1933 CTLPHI

1940 CTLSGH

1939 CTLSGL

12 CTLT

2226 CTLUN

2351 CTPCI

2352 CTPC2

2353 CTPC3

2354 CTPC4

2355 CTPC5


2356 CTPC6

2357 CTPC7

1943 CTPCHI

2343 CTPI1

2344 CTPI2

2345 CTPI3

2346 CTPI4

2347 CTPI5

2348 CTrP16

2349 CTPI7

2342 CTPINP

2350 CTPLNK

2319 CTPMIN

2320 CTPMNT

2323 CTPOI

2332 CTPO10

2333 CTPOI I

2334 CTPOI2

2335 CTP13

2336 CTP014

2337 CTPO15

2338 CTr•O6

2339 CT?!O7

2340 CTPO18

2341 CTP019

2324 CTP02

2325 CTI03

2326 CTP04

2327 CTPO5

2328 CTTr06 2329 CTrP7

2330 CTrP8

2331 CTPO9

1929 CTOHI

1947 CTPORA

2322 CTPOUT

1932 C1PPHI

1931 CTPPLO

1938 CTPSGL

2015 CTREF

1928 CTSET

1937 CTSIAS

1946 CTSRBY

1930 CTSRHI

1934 CTrMAR

1949 CITUBY

2098 CTURB

1950 CTUSBY


I

G-255



1944 CTUSER

1935 CTWMAR

2056 CVAUTO

2055 CVBLDN

2054 CVCLOS

1523 CVDAT

2053 CVOPEN

2052 CVPSET

2050 CVRELF

1535 CVRHHC

1534 CVRHHL

1538 CVRHQ

1533 CVRHTC

1532 CVRHTL

1537 CVRHWC

1536 CVRHWL

1531 CVRHX

2051 CVSET

2049 CWAUTO

2048 CWPOFF

2047 CWPON

2046 CWSET

2024 CXHA

2023 CXREG

496 DANPMP

557 DBADD

511 DBAMAX

498 DBATNK

505 DBCBOT

503 DBCOEF

558 DBCOM

510 DBCOUT

2278 DBGSGH

2277 DBGSGI

499 DBHAWI

500 DBHAWO

508 DBHBOT

506 DBHNOZ

509 DBHOUT

507 DBHSUR

501 DBMCPW

1844 DBPRRL

504 DBSCUR

502 DBVTNK

522 DCACON

550 DCAVCN

555 DCBNUM

556 DCBPAT


524 DCCCON

574 DCCONS

551 DCDNUM

552 DCDPAT

537 DCECOT

548 DCFBCN

525 DCFCON

528 DCFCOT

526 DCFECN

549 DCFICN

527 DCFPMP

541 DCGCOT

545 DCGRUN

544 DCGSET

576 DCHALF

529 DCHCON

531 DCICON

532 DCICOT

569 DC1NIT

543 DCKCUT

,530 DCLCON

579 DCLIMS

533 DCMCON

578 DCMONE

521 DCNCON

577 DCONE

311 DCONMU

278 DCONST

546 DCPCOE

547 DCPCOP

523 DCRCON

539 DCTACO

553 DCTANU

554 DCTAPA

536 DCTCON

542 DCTCOT

520 DCTL

540 DCTRCO

534 DCVPOR

535 DCVPSV

587 DCWARN

538 DCWCON

575 DCZERO

373 DEDGDT

2215 DELT

467 DFAFWB

489 DFCELN

486 DFCEVL


487 DFCLIN

488 DFCLN

483 DFCPMP

484 DFCVAL

485 DFCVL

495 DFDELN

493 DFDLIN

494 DFDLN

477 DFEJUN

465 DFG100

481 DFGNUM

478 DFGTAB

479 DFHTAB

476 DFJUN

475 DFLJUN

473 DFNJUN

472 DFNPMP

474 DFPJUN

482 DFSNUM

480 DFSTAB

492 DFVELN

490 DFVLIN

491 DFVLN

463 DFWS

318 DGENC

328 DGPMA

212 DHBURN

215 DHHA

214 DHHCAP

217 DHLTOP

211 DHNUM

216 DHOHMS

218 DHVMAX

450 DIAMAX

204 DIEXBO

206 DIEXMP

205 DIEXTO

207 DIFBY

208 DIFrLT

199 DIHACE

209 DIHAUI

203 DIHCEA

299 DIIMIX

202 DINCEA

186 DINVES

300 DIOMIX

378 DLBCLC

325 DLCONS


310 DLOOPC

327 DLSBMU

326 DLSPMU

516 DM2ACI

517 DM2AC2

514 DM2AFR

515 DM2FKB

518 DM2KCI

519 DM2KC2

512 DM2SLH

513 DM2SLO

341 DM504

451 DMABY

449 DMAREA

458 DMCHKV

29 DMDINV

459 DMDPI1

460 DMDPOI

441 DMHAWI

442 DMHAWO

443 DMMCPW

28 DMODIN

456 DMPATM

446 DMSLC

439 DMSLH

444 DMSLIC

"445 DMSLOC

457 DMTATM

452 DMVAMX

454 DMVEX

453 DMVIN

455 DMVNUM

448 DMVOL

23 DNBACK

24 DNCHGS

322 DNDMUL

321 DNIDHN

319 DNIDPE

320 DNIDPN

30 DNODE

26 DNPORV

22 DNPROP

27 DNPRSV

324 DNSMUL

25 DNSPRA

96 DPATH

376 DPBHMU

279 DPCONS



Name

356 DPCRFL

346 DPDGMX

290 DPDMAX

288 DPFLSH

287 DPFMUL

350 DPFRIG

2534 DPGASP

364 DPHAXW

344 DPHDT

281 DPHMUL

323 DPKMUL

351 DPLBOL

220 DPLRBO

347 DPLRIG

219 DPLRTD

221 DPLRTO

289 DPLSAT

365 DPLSBO

360 DPM034

375 DPPHMU

282 DPPMUL

286 DPQMUL

285 DPRTAU

210 DPRZR

342 DPSDE

343 DPSEQ

283 DPSMUL

345 DMrDT

359 DPTMSP

374 DPTREV

284 DPVMUL

377 DPVVMU

280 DPWMUL

313 DQCONS

315 DQGMUL

229 DQHT

230 DQMASS

314 DQNMUL

227 DQPN2

231 DQPRUP

317 DQSFRC

226 DQTANK

316 DQVMUL

228 DQVOL

368 DRAREF

2362 DRATIO

358 DRCMIN

357 DRCMUL


IndexIndex Short Variable Name

302 DRCONS

232 DRCP

18 DRCS

274 DRCURR

369 DRDAMP

19 DRDESN

273 DRDTDW

234 DRFRAC

277 DRFRAT

367 DRFREF

362 DRFRUB

305 DRISPL

372 DRLMUL

267 DRNPOL

233 DRNUM

275 DRPLEK

304 DRQMUL

271 DRSLIP

270 DRTNUM

272 DRTORQ

363 DRTRUB

21 DRTYPE

269 DRVBUS

307 DRVMAX

371 DRVMUL

306 DRVNOR

276 DRVRAT

309 DRVSPD

308 DRVTIM

438 DSAEHT

426 DSAFLO

427 DSAHT

422 DSATUB

436 DSAWAL

418 DSBREF

433 DSDHYD

352 DSDP

353 DSDPI2

354 DSDPW

355 DSDPW1

424 DSECON

423 DSETUS

497 DSGDB

381 DSGDES

379 DSGS

380 DSGSIN

312 DSGTRM

425 DSHEAT


434 DSHWAL

437 DSMCPW

417 DSNREF

416 DSREFL

435 DSRWAL

420 DSTDN

419 DSTREF

421 DSTUP

596 DTAHT

595 DTDENS

594 DTH2

606 DTNFC

591 DTNRAD

604 DTNZ

592 DTROUT

190 DUAMAX

188 DUAMIN

298 DUAMUL

191 DUAROD

293 DUCONS

370 DUFAST

349 DUFRIG

301 DUKCEA

294 DUKCOR

348 DULRIG

1456 DUMOOl

15 DUMMYI

366 DUORFL

189 DUPMAX

187 DUPMIN

296 DUPMUL

297 DURMUL

295 DUVMUL

334 DVAMOV

337 DVAMSP

340 DVANC

335 DVAPCO

332 DVAPOR

336 DVAPQT

333 DVAPSV

339 DVAQTC

338 DVAQTG

329 DVAREA

331 DVAUHQ

330 DVAVNT

223 DVGPOR

224 DVGPSI

225 DVGPS2

292

291

222

361

213

559

560

2244

580

561

400

2420

2462

2461

586

2381

2406

2408

2440

2407

2436

2505

2216

2473

2490

2411

2379

2380

2454

2509

2433

2506

1742

1751

1741

1740

1750

1749

2484

1737

1748

1736

1735

1747

1746

2397

1734

1738

Short Variable Name

DVKDWN

DVKUP

DVLREL

DVTMAX

DWABLD

ELEMS

ELIN

ELLAST

ELMAX

ELTYPE

EVAPSS

FAEXTF

FATABL

FBTABL

FCTMAX

FCV

FCVAFL

FCVDPM

FCVP

FCVRES

FCVV

FDCLMS

FDELT

FDHEAT

FDMODL

FDNODE

FDPATH

FDPEL

FDPUMP

FDSYST

FDVALV

FECLMS

FEELIN

FEENOZ

FELIN

FELINE

FENOZ

FENOZZ

FFDPSO

FGELIN

FGENOZ

FGLIN

FGLINE

FGNOZ

FGNOZZ

FGPMCO

FGPMP

FGTOT

G-257



1893 FHENTH

2392 FHEXT

2419 FHEXTF

2413 FHEXTN

2485 FHFWBI

1886 FHINIT

1894 FHLOAD

2416 FHNODE

1895 FHNUM

2388 FHPATH

1733 FHPMP

1892 FHTBL

2479 FHTHMX

2476 FHTRHV

2501 FIAURC

2402 FICPMP

2423 FIMN

2445 FINDXF

1743 FIOCON

2503 FITRIP

2504 FITRPO

198 FLA

1772 FLBEH

1760 FLBEIN

1778 FLBEIO

1763 FLBEOU

1781 FLBEPT

1769 FLBEW

1775 FLBEX

1784 FLBEXE

1771 FLBH

1759 FLBIN

1777 FLBIO

1762 FLBOU

1780 FLBPT

1768 FLBW

1774 FLBX

1783 FLBXE

2224 FLGQUE

2483 FMAXTU

2452 FNAFVI

2451 FNAFVT

2401 FNCPMP

2400 FNDEXT

2398 FNDIN

2399 FNDOUT

2472 FNEFWP

2425 FNEXTN


2409 FNFLO

2489 FNHDPT

2449 FNHDV

2487 FNHTBL

2471 FNMFWP

2424 FNNOD

2442 FNPATH

2429 FNPFLB

2486 FNPHET

2467 FNPMPE

2466 FNPMPM

2500 FNPMRC

2463 FNPMTH

2431 FNPPRV

2428 FNPSGA

2427 FNPSGE

2426 FNPSGM

2468 FNPTMP

2465 FNPTP

2498 FNPTRC

2444 FNPTV

2469 FNPUM

2432 FNSG

2443 FNTABL

2464 FNTABP

2453 FNTAFV

2470 FNTBFP

2448 FNVAL

2447 FNVBFV

2450 FNVHDV

2499 FNVLRC

2446 FNVMFV

1731 FPEVAL

2384 FPEXT

2421 FPEXTF

2412 FPEXTN

1728 FPJUN

2405 FPOISO

2435 FPOSIT

1726 FPPIN

1727 FPPMP

1744 FPTCON

1730 FPVAL

1729 FPVALV

2477 FPWRTB

2389 FQCURR

2478 FQPTBL

2391 FRES


2382 FRESL

2390 FRESV

2393 FRHOEX

2383 FRHOFD

2417 FRHOND

2455 FSPDMD

2456 FSPEED

1732 FSPMP

2441 FSTP

2434 FSTROK

2396 FSUMP

2458 FTAUOF

2457 FTAUON

2438 FTCLOS

2482 FTEHDP

1757 FrENOZ

2502 FTIMET

2439 FTLAG

1756 FTNOZ

1755 FrNOZZ

2437 FTOPN

2480 FTPOWR

2474 FTPWR

2475 FTQLAG

2481 FTWHDP

2430 FWAFLB

464 FWCOEF

2418 FWEXTF

1766 FWLBEF

1765 FWLBF

1770 FWLBH

1758 FWLBIN

1776 FWLBJIO

1764 FWLBLO

1761 FWLBOU

1779 FWLBPT

1767 FWLBW

1773 FWLBX

1782 FWLBXE

2508 FWLMSS

2385 FWMAS

2497 FWRCIN

2495 FWRCIR

2496 FWRCOT

2492 FWRCPB

2493 FWRCRE

2494 FWRCSP

2378 FWSCOM


1739 FWSENT

2459 FWSHT

2403 FWSICK

2404 FWSIMF

2410 FWSKEY

2488 FWSNHT

2491 FWSNRC

2415 FWSP

2414 FWSPO

2395 FWSPS

2394 FWSRP

2422 FWSUM

2387 FWSW

2386 FWSWO

2460 FWSWT

1745 FXECON

1754 FXENOZ

1753 FXNOZ

1752 FXNOZZ

562 GROUPS

2245 GROUT

583 GRPMAX

245 HAD

253 HADC

243 HAN

251 HANC

249 HAR

257 HARC

247 HAT

255 HATC

673 HCORE

1033 HEATSG

260 HMUL

90 HPZR

1657 HSLHHF

386 HSPTB1

387 HSPTB2

385 HSPTBL

393 HT3TB1

394 HT3TB2

392 HT3TBL

414 HT4MAX

469 HTNOZ

471 HTNOZA

470 HTNOZE

468 HTNOZF

246 HVD

254 HVDC



Name

244 HVN

252 HVNC

259 HVOID

250 HVR

258 HVRC

248 HVT

256 HVTC

588 INEDFL

572 INEDPG

571 INEDSQ

2229 INIFLG

2359 INIOUT

582 INMAX

570 INPED

2313 INSGV

2315 INSLBI

2314 INSLBO

2312 INWRCS

1723 IOCTL

1722 IOCTLK

1718 ITOTAT

1719 ITOTCD

1720 ITOTCT

2290 rrOTP 1721 ITOTTU

2360 JUNKI

689 KALPHA

693 KBBAR

694 KBBARR

691 KBETA

742 KCH12

782 KCONSC

783 KCONSH

720 KDCORE

709 KDKBO

733 KDKBOR

695 KDKBOZ

725 KDKCT

739 KDKCUT

735 KDKDOP

715 KDKFT

698 KDKFrZ

740 KDKHER

748 KDKHT

749 KDKHTI

755 KDKHTS

721 KDKIN

699 KDKINZ


713 KDKMD

697 KDKMDZ

734 KDKMOD

711 KDKMT

696 KDKMTZ

737 KDKROD

738 KDKSCR

729 KDKSUB

736 KDKTMD

731 KDKTOT

732 KDKUSR

690 KDLAM

728 KDSRC

746 KEN2

743 KEX2

816 KFAXIL

785 KFDH

751 KFDHC

753 KFDHCO

754 KFDHCM

794 KFLDEN

756 KFLGDH

682 KFPOWT

685 KFQC

686 KFQCD

758 KFQCDT

766 KFRAIN

747 KFTRIP

762 KFZBJ

764 KH2M

767 KHER3D

765 KINCON

817 KIZX

687 KKIN

688 KKINI

730 KKINO

741 KKINS

700 KLMOD

679 KLUPOW

781 KMHER

770 KMLHER

701 KNBO

727 KNCT

752 KNDHC

723 KNDKIN

704 KNFT

703 KNMD

702 KNMT


681 KNPOWT

705 KNQDK

778 KNWFR

761 KNYZIR

791 KOPBOR

789 KOPCUT

793 KOPDEN

790 KOPDOP

786 KOPFB

795 KOPHER

792 KOPMOD

788 KOPREG

787 KOPROD

818 KPCZR

776 KPHER

692 KPLAM

768 KPRHER

772 KPTWMN

775 KPTWMX

744 KQD2

717 KQDK

745 KQF2

820 KQZRH2

780 KRHER

821 KSHPIN

706 KSIGD2

707 KSTARL

710 KTBO

726 KTCT

750 KTDHC

769 KTDHER

722 KTDKIN

716 KTFT

719 KTFUEL

757 KTIMDH

771 KTLTMN

774 KTLTMX

714 KTMD

712 KTMT

683 KTPOWT

718 KTQDK

708 KTSS

724 KTUPOW

676 KUSER

677 KUSERI

684 KUSERS

784 KWEDGE

779 KWFHET


773 KWFRMN

777 KWHER

680 KWPOWZ

811 KXCALB

804 KXDISP

813 KXGAIN

809 KXOFFA

807 KXOFFS

805 KXPOWD

806 KXPOWR

808 KXPWAV

814 KXSVR

810 KXTAU

812 KXTUNE

759 KZRH2

760 KZRH2I

763 KZRH2S

819 KZX

1525 LDPAR

1524 LDPDAT

1529 LDPDZ

1528 LDPKE

1527 LDPKG

1526 LDPLOD

1539 LDRCH

1540 LDRCP

581 LSTMAX

1906 M2CIO

1907 M2CPT

1908 M2CXE

1909 M2DVDH

1910 M2DVDP

1918 M2QARM

1912 M2SLHF

1913 M2SLHG

1911 M2SLHH

1914 M2SLM

1915 M2SLML

1916 M2SLP

1917 M2SLQ

1919 M2SLSV

1922 M2SLT

1924 M2SLX

1920 M2SVF

1921 M2SVG

1923 M2TWAL

1687 MAATM

1688 MACOND




1689 MACONT

2246 MALCTL

1686 MAOUT

593 MATrYP

1690 MATURB

1651 MCIO

672 MCORES

1652 MCV1

1678 MCSL

1653 MCXE

1875 MDPMIN

1654 MDVDH

1655 MDVDP

1698 MEATM

1703 MECOND

1708 MECONT

1713 METUR

1848 MFTMAX

1697 MGATM

1702 MGCOND

1707 MGCONT

1696 MGOUT

1673 MGSLBI

1650 MGSLBO

1712 MGTUR

1674 MHSL

1699 MIATM

1682 MIBYPO

1704 MICOND

1709 MICONT

2295 MINMAX

1680 MIPOS

1681 MISIG

1677 MISL

1714 MITUR

1648 MNODE

1905 MNODE2

2302 MNPPR

2303 MNPPRT

2306 MNRCSP

2307 MNRPT

2310 MNSGP

2311 MNSGPT

2221 MODELQ

2242 MODERR

2231 MODOFF

2223 MODQUE

2274 MOISTC


1700 MPATM

1705 MPCOND

1710 MPCONT

1849 MPRESC

1675 MPSL

1715 MPTUR

1663 MQARM

1724 MSCHOK

1672 MSLBI

1649 MSLBO

1647 MSLH

1656 MSLHH

1658 MSLHHG

1659 MSLHM

1660 MSLHML

1661 MSLHP

1662 MSLHQ

1664 MSLHSV

1667 MSLHT

1670 MSLHX

1671 MSLIN

1665 MSVF

1666 MSVG

1676 MTSL

1668 MTWALL

1683 MVPOS

1684 MVSIG

1692 MWATM

1693 MWCOND

1694 MWCONT

1669 MWIN

1691 MWOUT

1695 MWTURB

1701 MXATM

1706 MXCOND

1711 MXCONT

2298 MXHTFR

2299 MXHTr

2296 MXPOW

2297 MXPOWT

2300 MXPPR

2301 MXPPRT

2304 MXRCSP

2305 MXRPT

2308 MXSGP

2309 MXSGPT

1679 MXSL

1716 MXTUR


86 NAMULT

68 NANNUL

69 NCEASH

55 NCL1

56 NCL2

57 NCL3

58 NCLA

65 NCORE

73 NELBOT

1717 NETIOU

74 NGEOM

41 NHLI

42 NHL2

43 NHL3

44 NHL4

2238 NINIT

38 NNODCL

36 NNODHL

34 NNODSE

35 NNODSG

37 NNODSL

71 NODEA

54 NODECL

40 NODEHL

31 NODENO

39 NODENU

64 NODEOT

45 NODESG

59 NODESL

76 NODETH

32 NODETO

70 NODGEO

2526 NONI5A

2564 NON50A

2565 NONSOB

2510 NONC

2511 NONCOI

2512 NONC02

2513 NONC03

2515 NONC05

2516 NONC06

2517 NONC07

2518 NONC08

2519 NONC09

2520 NONCIO

2521 NONCII

2522 NONCI2

2523 NONC13


2524 NONCI4

2525 NONCI5

2527 NONCI6

2528 NONCI7

2529 NONC18

2530 NONC19

2531 NONC20

2532 NONC21

2533 NONC22

2535 NONC31

2536 NONC32

2537 NONC33

2569 NONC34

2538 NONC35

2539 NONC36

2540 NONC37

2541 NONC38

2542 NONC39

2562 NONC40

2543 NONC41

2544 NONC42

2545 NONC45

2546 NONC46

2547 NONC47

2548 NONC48

2549 NONC49

2563 NONCSO

2550 NONC5 1

2551 NONC52

2553 NONC54

2570 NONC55

2571 NONC56

2554 NONC57

2555 NONC58

2556 NONC59

2557 NONC60

2558 NONC61

2559 NONC62

2560 NONC65

2561 NONC66

2572 NONC67

2573 NONC68

2575 NONC72

2576 NONC73

2577 NONC74

2578 NONC75

2579 NONC76

2580 NONC77



Name

2581 NONC78

2582 NONC79

2583 NONC80

2574 NONCSI

75 NOSECT

563 NOTAB

66 NPRZR

87 NSECT

47 NSGIC

46 NSGIH

60 NSGIP

49 NSG2C

48 NSG2H

61 NSG2P

51 NSG3C

50 NSG3H

62 NSG3P

53 NSG4C

52 NSG4H

63 NSG4P

67 NUHEAD

91 NUMANN

33 NUMNOD

88 NUMSEG

20 NUMSG

824 NUMSHP

462 NUMSL

81 NWLMXC

82 NXBOIL

80 NXBOT

79 NXCON

83 NXINJ

77 NXLIQ

84 NXSPOF

85 NXSPON

78 NXSTM

72 NZTOT

122 PANCOR

183 PAREA

128 PATHCL

1029 PATHDN

131 PATHG

127 PATHHL

97 PATHNO

120 PATHNU

129 PATHSG

98 PATHTO

1028 PATHUP


201 PCEAUH

123 PCORUH

6 PDATE

185 PDIA

174 PEBLED

160 PECHGS

162 PEDRN

177 PEEXIT

158 PEEXT

165 PEGAS

155 PEINIT

172 PEINT

171 PELB

166 PELEAK

161 PELET

156 PEMOM

157 PENONM

170 PEORIN

175 PEPZRR

159 PERCP

402 PER1M

169 PERODE

168 PESB

163 PESDC

167 PESGTR

164 PESIS

173 PESPRA

176 PEUHR

154 PEXIT

3 PFILE

943 PFLOWC

178 PGEOM

151 PIBLED

137 PICHGS

139 PIDRN

135 PIEXT

142 PIGAS

148 PILB

143 PILEAK

138 PILET

133 PIMOM

132 PINLET

134 PINMOM

149 PINT

147 PIORIN

152 PIPZRR

136 PIRCP

146 PIRODE


145 PISB

140 PISDC

144 PISGTR

141 PISIS

150 PISPRA

153 PIUHR

182 PKXNEG

181 PKXPOS

2 PLABEL

125 PLBLOC

184 PLDIAM

13 PLT

14 PLTO1

114 PNCHGM

108 PNCHGS

106 PNCL

110 PNDRN

116 PNDRNM

100 PNEXT

105 PNHL

102 PNINT

101 PNLEAK

109 PNLET

115 PNLETM

99 PNMOM

119 PNMOMM

107 PNNONM

103 PNPATH

113 PNRCP

104 PNSB

11 PNSDC

117 PNSDCM

112 PNSIS

118 PNSISM

675 POW

678 POW01

815 POWAX

2234 POWOFF

303 PPINER

2552 PPSLST

126 PPUMP

179 PRADII

825 PRISHP

124 PSPRAY

992 PSTMUP

121 PSURGE

5 PTIME

4 PTITLE


180 PTLOA

564 I'1TAB

130 PUCEA

200 PUPCEA

2568 PZQCND

2567 PZQEFF

428 QSGIOO

429 QSGTBL

1198 RALEAK

2363 RAUSER

2284 RBAL

899 RBDRFT

1493 RBINIT

897 RBNODE

898 RBRELE

902 RCBOIL

1418 RCBORN

905 RCBUB

1417 RCENTH

1416 RCFLOW

1270 RCHGMX

1419 RCHYD

904 RCINJ

1420 RCIOD

1100 RCKMUL

1101 RCLCEA

900 RCNODE

1421 RCPART

1204 RCPCOM

1206 RCPELE

1205 RCPINT

1227 RCPLEK

1223 RCPMAL

1213 RCPMEC

1256 RCRMOD

826 RCS

1040 RCSCOR

1114 RCSGLO

1373 RCSLB

1389 RCSLBL

1194 RCSMAL

2232 RCSOFF

1229 RCSOPT

1054 RCSPZR

1102 RCSQT

1034 RCSRCP

1032 RCSSG

1128 RCSSOL




1178 RCSSTA

1086 RCSUH

903 RCSURF

1188 RCSVLV

901 RCTOT

1422 RCXEN

1360 RDEL

1362 RDELTA

1363 RDELWL

890 RDHDM

889 RDHDU

893 RDHFDP

1305 RDHFMN

894 RDHGDP

1163 RDM2HR

1164 RDM8HR

1156 RDMBF

1161 RDMCDF

1157 RDMCF

1160 RDMCLR

1155 RDMFSH

1154 RDMIIO

1162 RDMTCU

1158 RDMXQ2

1159 RDMXQ8

883 RDNODE

1023 RDOCHK

1022 RDPACT

885 RDPDML

886 RDPDMS

884 RDPDMT

888 RDPDUS

887 RDPDUT

1017 RDPELE

1020 RDPEXT

1016 RDPFRC

1019 RDPHED

1018 RDPLOS

1015 RDPMOM

1014 RDPPAT

1021 RDPTOT

1425 RDRNG

1273 RDRNMX

1153 RDSPAR

892 RDVDHT

891 RDVDPT

896 RDVGDP

895 RDVHDP


1310 RDWSDC

1311 RDWSTP

963 REBLED

950 RECHGS

1350 REDGST

952 REDRN

1263 REDTLB

1266 REELB

948 REEXT

1264 REFLB

1265 REGLB

1349 REGSIT

1316 REINIT

961 REINT

960 RELB

1031 RELDN

955 RELEAK

951 RELET

849 RELIQ

852 RELIQS

1308 RELTST

1030 RELUP

1262 RELVLB

851 REMIX

946 REMOM

839 RENNOD

847 RENODE

947 RENONM

841 RENSTM

840 RENTOT

959 REORNG

944 REPATH

964 REPZRR

949 RERCP

958 RERODE

957 RESB

953 RESDC

956 RESGTR

954 RESIS

962 RESPRA

853 RESRMS

850 RESTM

1025 RESUBK

848 RETOT

965 REUHR

1275 REXBMX

1354 RFAIL

1010 RFBLED


997 RFCHGS

1361 RFDELT

1370 RFDQHT

1371 RFDQMX

999 RFDRN

995 RFEXT

1008 RFINT

1007 RFLB

1276 RFLBUB

1251 RFLCHT

1365 RFLCOL

1368 RFLCVC

1002 RFLEAK

998 RFLET

1246 RFLHET

1366 RFLNON

1292 RFLPZR

1269 RFLSDC

1369 RFLSIT

1253 RFLSPR

1364 RFLWAL

993 RFMOM

994 RFNONM

1006 RFORNG

1011 RFPZRR

1367 RFQHT

996 RFRCP

1005 RFRODE

1004 RFSB

1000 RFSDC

1372 RFSDQS

1003 RFSGTR

1001 RFSIS

1009 RFSPRA

1026 RFSUBK

1012 RFUHR

1423 RGASPR

940 RGBLED

927 RGCHGS

1127 RGDP

929 RGDRN

1122 RGELQS

1118 RGENGY

1117 RGENTH

1123 RGESTS

925 RGEXT

938 RGINT

937 RGLB


932 RGLEAK

928 RGLET

1116 RGMASS

923 RGMOM

924 RGNONM

936 RGORNG

921 RGPATH

1115 RGPRES

941 RGPZRR

1121 RGQUAL

926 RGRCP

935 RGRODE

934 RGSB

930 RGSDC

1119 RGSENG

933 RGSGTR

931 RGSIS

1124 RGSLQS

939 RGSPRA

1125 RGSSTS

1120 RGSVOL

1126 RGTSAT

942 RGUHR

1056 RHADMI

1058 RHENGY

909 RHETRO

1448 RHFVLT

1057 RHQELE

1060 RHQHTR

1061 RHQPZR

1059 RHTEMP

1247 RHTvIE

1296 RHVBSP

1450 RHVBUS

1055 RHVOLT

916 RIBCOR

912 RIBUBM

1474 RICONT

913 RIDBUB

1044 RILLIQ

1045 RILMIX

1452 RIMAL

918 RIMBUB

1415 RINBOP

1488 RINCON

1414 RINPUT

834 RINTER

1482 RIPZRR



Name

1476 RIQT

2294 RIRELR

2293 RIRELT

919 RISLIP

1307 RITDPL

2291 RITOT

1431 RIVLVC

1447 RIVOLT

914 RIVTOP

915 RIVTRN

917 RIXMIX

1187 RKASUR

1043 RKBORN

1048 RKBOUY

1148 RKBREL

1049 RKDPUH

1051 RKEDIS

1052 RKETLT

1042 RKGIN

1149 RKHREL

1294 RKHRMX

1328 RKHSTM

1150 RKIREL

1046 RKLMIX

1151 RKPREL

1329 RKPSTM

1494 RKPUMP

1041 RKQ

1050 RKQCEA

1053 RKQUH

1047 RKSANN

1398 RKSAV

1147 RKSREL

1397 RKTAV

1152 RKXREL

1378 RLBALS

1387 RLBCOS

1380 RLBDPL

1383 RLBDTS

1374 RLBEL

1375 RLBES

1382 RLBLDP

1379 RLBLDR

1197 RLBLOW

1381 RLBQMX

1388 RLBRCS

1377 RLBS

1376 RLBVFR


1173 RLELIQ

1175 RLELQS

1166 RLENST

1167 RLENTO

1182 RLEQUI

1174 RLESTM

1424 RLETG

1272 RLETMX

1176 RLFLOW

1181 RLHOMO

1179 RLIERR

1490 RL1NIT

1177 RLKFLS

1196 RLLB

1184 RLLBMP

878 RLLIQ

1170 RLMBUB

2566 RLMGAS

877 RLMIX

1168 RLMLIQ

1169 RLMSTM

1171 RLMTOT

876 RLNODE

2364 RLNUP

1180 RLOERR

1172 RLPRES

1195 RLRODE

1245 RLSPIK

1324 RLTINT

1330 RM504

846 RMBUB

1183 RMBUBP

1454 RMLB

1530 RMLDNB

844 RMLIQ

842 RMNODE

830 RMOCHT

827 RMODEL

829 RMOOIL

833 RMOPOW

832 RMOQT

1239 RMORI

1257 RMOR2

1285 RMOR3

1290 RMOR3A

1295 RMOR3B

1298 RMOR4

1309 RMOR5


1315 RMOR6

1238 RMORA

828 RMORCP

831 RMORCS

1471 RMRLOC

1473 RMROD

1457 RMRODE

1470 RMRSHB

1472 RMRVIB

1453 RMSB

1455 RMSGTR

845 RMSTM

843 RMTOT

1458 RMVALV

1463 RMVMOV

1464 RMVPCR

1461 RMVPOR

1465 RMVPQT

1468 RMVQTC

1467 RMVQTG

1469 RMVQTN

1462 RMVSAF

1466 RMVSPR

1459 RMVUHC

1460 RMVUHQ

1141 RNBOR

907 RNECAN

906 RNENOD

908 RNESTA

1355 RNEVER

1282 RNEXMN

1142 RNHYD

1143 RNIOD

835 RNODEV

2285 RNODFL

1144 RNPART

1139 RNREL

1140 RNSOL

1145 RNXEN

1400 ROCHT

1396 ROCORE

1391 ROPUMP

1390 ROUTPT

1165 RPASTV

920 RPATHV

1191 RPAVLV

1130 RPBOR

1234 RPCOND


1475 RPCONT

1286 RPCORS

1337 RPCSUR

1289 RPCWAL

1024 RPDER

1062 RPDPLV

1306 RPDPMD

1299 RPDTBL

1300 RPDTSB

1342 RPDTSS

1241 RPEMAX

1240 RPEMIN

945 RPENTH

1327 RPFAIR

922 RPFLOW

1202 RPGCON

1200 RPGPOR

1203 RPGQTI

1081 RPGQT2

1201 RPGSAF

1080 RPGSQT

1320 RPGVCN

1321 RPGVQT

1291 RPHLMU

1288 RPHWMU

1131 RPHYD

1236 RPICRT

1489 RPINIT

1132 RPIOD

1185 RPITER

1231 RPITRP

1319 RPLAIR

1283 RPLCOF

1318 RPLINT

966 RPLIQ

1338 RPLLAS

1281 RPLLOP

1297 RPLREF

1314 RPMAIR

1313 RPMSTM

1230 RPNCAL

1078 RPNCON

1237 RPNCRT

836 RPNODE

1079 RPNQT

1232 RPNTRP

1133 RPPART

1317 RPPINT


I

G-263

Table GA: Alphabetized Index of Short Variable Names


1082 RPPLOC

1304 RPPMOD

1235 RPPRAN

1341 RPQAXW

1242 RPQCMU

1340 RPQCON

970 RPQUAL

837 RPRESP

838 RPRESS

1129 RPSOL

967 RPSTM

968 RPSVOL

1293 RPTAUR

1254 RPTFLS

1323 RPTINT

1063 RPTREF

1065 RPTRTD

1332 RPTSB

1064 RPTSRG

1339 RPTWAL

1186 RPTYPE

1027 RPUPDN

1233 RPVISC

1199 RPVLV

991 RPVOID

1134 RPXEN

1322 RPXREL

1193 RQAVLV

875 RQCOND

870 RQCONT

1478 RQEDMW

1105 RQENGY

1104 RQENTH

871 • RQEXT

1477 RQGDMW

1481 RQGGWS

1479 RQGRCW

1106 RQLEVL

874 RQLIQ

1111 RQLRUP

1108 RQMGAS

1107 RQMWAT

1113 RQNCON

868 RQNODE

1480 RQPGWS

1352 RQPJ4

1103 RQPRES

1112 RQSOLU


873 RQSTM

1109 RQTEMP

872 RQTOT

1110 RQTSUR

869 RQWALL

1392 RRIDP

1393 RR2DP

1394 RR3DP

1395 RR4DP

1345 RRADFC

1210 RRADIM

1301 RRADMU

1209 RRADRE

1346 RRAMPS

1221 RRAVIB

1399 RRBORL

1224 RRBREK

1303 RRCFRC

263 RRDD

1039 RRDP

1302 RRDSLO

1222 RRDSPD

1334 RRDTrP

1331 RRFCAV

1451 RRFFRQ

1208 RRFREQ

1449 RRFVLT

1038 RRHEAD

1036 RRHEAT

1225 RRHIVI

1348 RRLCAV

1228 RRLEAK

1226 RRLOCK

1353 RRLTHI

1212 RRPF

264 RRPHD

265 RRPHT

1217 RRQRCP

1211 RRSLIP

1220 RRSMOT

261 RRSPDR

1035 RRSPED

1219 RRSPMP

1312 RRSTAR

1335 RRSTOP

1347 RRSVOL

266 RRSYNC

1215 RRTELE


1216 RRTFRI

1214 RRTHYD

1037 RRTORQ

1336 RRTRIP

262 RRVFLO

1218 RRVIBR

1333 RRVOID

1207 RRVOLT

1426 RSDCG

1325 RSDCGF

1326 RSDCGM

1274 RSDCMX

1287 RSDPMU

911 RSECT

1356 RSFAIL

1384 RSHAOV

1495 RSINIT

1429 RSISB

1428 RSISE

1427 RSISG

1430 RSITG

1271 RS1TMX

856 RSLIQ

858 RSLIQS

854 RSNODE

1357 RSRECV

1146 RSREL

2365 RSSCON

857 RSSTM

859 RSSTMS

2366 RSSUSE

1013 RSTDN

855 RSTOT

1385 RSTPRE

1351 RTC12B

1492 RTCLIN

867 RTCONT

1249 RTDEL

1252 RTDELT

1406 RTEIN

1402 RTELIQ

1268 RTESRG

1403 RTESTM

1250 RTFDEL

1244 RTFRAC

1405 RTGIN

1243 RTHSMU

1358 RTIMEC


1359 RTIMSC

862 RTLIQ

1408 RTLMIX

1409 RTLSAT

1413 RTMBUB

1412 RTMLIQ

860 RTNODE

2289 RTOTE

2286 RTOTFL

2287 RTOTHR

2288 RTOTM

1401 RTPRES

1404 RTQUAL

1410 RTQWAL

864 RTSAT

863 RTSTM

866 RTSUBC

1267 RTrMAX

1248 RTTMSC

1261 RTISRG

1411 R"TWAL

431 RTUBES

865 RTWALL

1407 RTXIN

1190 RUAVLV

1090 RUECON

1088 RUEQT

1091 RUETOP

1089 RUGCON

1087 RUGQT

1344 RULORG

1093 RUMNON

1097 RUNCON

1096 RUNDIL

1098 RUNQT

1099 RUPLOC

1095 RUPNON

1343 RUPORG

1255 RUQCMU

1092 RUSTOP

1094 RUVNON

1189 RVAREA

1074 RVEREL

1437 RVFMOV

1438 RVFPC

1435 RVFPOR

1439 RVFPQT

1442 RVFQTC



Name

1441 RVFQTG

1443 RVFQTN

1436 RVFSAF

1444 RVFSIG

1440 RVFSPR

1433 RVFUHC

1434 RVFUHQ

1486 RVGPZR

1073 RVGREL

1485 RVNPZR

882 RVOIDF

1484 RVOPZR

1085 RVPDN

1432 RVPOS

1487 RVPPZR

1084 RVPUP

1446 RVSPOR

1075 RVSREL

1445 RVSSPR

1077 RVTREL

1076 RVVRLE

1483 RVXPZR

1135 RWAHYD

1136 RWAIO

1137 RWAPT

1192 RWAVLV

1138 RWAXE

1071 RWBAUX

1068 RWBPAT

1277 RWDELH

1070 RWEAUX

1083 RWEBLD

1258 RWEFF

1278 RWEFFI

1280 RWEFF2

1259 RWEFFM

1067 RWEPAT

1069 RWGAUX

1072 RWGBLD

1066 RWGPAT

1491 RWlNIT

1260 RWLEFF

1279 RWLPRS

1284 RWPDEG

988 RXBLED

975 RXCHGS

977 RXDRN

973 RXEXT


986 RXINT

985 RXLB

980 RXLEAK

976 RXLET

881 RXMIX

971 RXMOM

972 RXNMOM

879 RXNODE

984 RXORNG

969 RXPATH

989 RXPZRR

974 RXRCP

983 RXRODE

982 RXSB

978 RXSDC

981 RXSGTR

979 RXSIS

987 RXSPRA

880 RXTOT

990 RXUHR

1888 SADEG

1890 SADFUL

1889 SADGOP

1891 SADZER

2280 SAREA3

1850 SASEPT

1901 SASUBE

1797 SBBDM

1791 SBDVDH

1792 SBDVDP

1814 SBEBOT

1812 SBENTH

1831 SBEOUT

1832 SBEREL

1830 SBESNK

1813 SBESUR

1809 SBG

1811 SBGBOT

1828 SBGOUT

1829 SBGREL

1827 SBGSNK

1810 SBGSUR

1817 SBIBOT

1815 SBIO

1834 SBIOUT

1835 SBIREL

1833 SBISNK

1816 SBISUR


1788 SBITNK

1845 SBMODF

1543 SBOTP

1518 SBPAR

1820 SBPBOT

1517 SBPDAT

1522 SBPDZ

1521 SBPKE

1520 SBPKG

1519 SBPLOD

1837 SBPOUT

1838 SBPREL

1843 SBPROT

1842 SBPRSN

1836 SBPSNK

1819 SBPSUR

1818 SBPT

1789 SBPTNK

1802 SBSVG

1804 SBTWAL

1808 SBVBOT

1825 SBVOUT

1806 SBVPOS

1826 SBVREL

1824 SBVSNK

1807 SBVSUR

1823 SBXBOT

1821 SBXE

1840 SBXOUT

1841 SBXREL

1839 SBXSNK

1822 SBXSUR

1790 SBXTNK

1550 SCBORI

1551 SCBOR2

1549 SCEX2

1544 SCIOI

1545 SCIO2

1903 SCNVRG

1870 SCOLDT

1546 SCPTI

1547 SCPT2

1881 SCRMOD

1548 SCXEI

11 SDATE

2273 SDELAY

1552 SDELTV

1553 SDP


1554 SDVDP

1858 SDVREC

1786 SEAFWS

1896 SECON

1555 SENTHI

1556 SENTH2

1557 SENTH3

1558 SENTH4

1559 SENTHS

565 SEQNCE

2195 SETDDT

2198 SETDM

2197 SETDP

2194 SETDT

2196 SETP

2201 SETRT

2193 SEMT

2199 SETW

2200 SETWD

403 SFCONI

1865 SFDMIN

8 SFILE

1852 SFK3T

1904 SFLUIE

1854 SFPMAX

1853 SFr1ME

2507 SGAFWS

1787 SGBD

1793 SGBDH

1794 SGBDHF

1795 SGBDHG

1796 SGBDL

1798 SGBDML

1799 SGBDP

1800 SGBDSV

1803 SGBDT

1805 SGBDX

1632 SGCHOK

432 SGMTCP

1785 SGNAFW

1499 SGQDH

1500 SGQDW

1501 SGQLH

1502 SGQLW

1498 SGQNNS

1497 SGQNSE

1508 SGQNSS

1509 SGQOPT


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1496 SGQPAR

1507 SGQPR

1504 SGQQP

1505 SGQQS

1510 SGQSEH

1503 SGQSET

1506 SGQTrB

1541 SGS

1560 SGSEI

1561 SGSE2

1562 SGSE3

1563 SGSE4

1564 SGSE5

1725 SGSFWS

1565 SGSHF

1566 SGSHG

1570 SGSHTI

1568 SGSHT2

1569 SGSHT3

1542 SGSINT

1851 SGSM

1571 SGSMI

1572 SGSM2

1573 SGSM3

1574 SGSM4

1575 SGSM5

2235 SGSOFF

1576 SGSP

1583 SGSSVI

1584 SGSSV2

1585 SGSSV3

1586 SGSSV4

1587 SGSSV5

1590 SGSTI

1591 SGST2

1592 SGST3

1593 SGST4

1594 SGST5

1602 SGSVI

1603 SGSV2

1604 SGSV3

1605 SGSV4

1606 SGSV5

1596 SGSVF

1597 SGSVF2

1598 SGSVF3

1599 SGSVF4

1600 SGSVF5


1601 SGSVG

1617 SGSWI3

1618 SGSW21

1619 SGSW23

1623 SGSW25

1620 SGSW31

1621 SGSW32

1625 SGSW42

1622 SGSW51

1624 SGSW53

1607 SGSWFI

1608 SGSWF2

1609 SGSWF3

1610 SGSWF4

1611 SGSWF5

1612 SGSWGI

1613 SGSWG2

1614 SGSWG3

1615 SGSWG4

1616 SGSWG5

1627 SGSXI

1628 SGSX2

1629 SGSX3

1630 SGSX4

1631 SGSX5

1879 SGTAU

2369 SGTDB1

2370 SGTDB2

2371 SGTDB3

2372 SGTDB4

2373 SGTDB5

2374 SGTDB6

2375 SGTDB7

2376 SGTDB8

2377 SGTDB9

2368 SGTDBP

1514 SGTHT

2275 SGTIOP

1512 SGTLEN

1513 SGTRK

1511 SGTRP

1516 SGTSAR

1515 SGTSLT

404 SGU12

405 SGU23

406 SGV2AC

407 SGV4MX

408 SGV5MX


1880 SGXTAU

1873 SH2STM

1872 SH2SUB

1633 SHEAT

1567 SHLEVL

1871 SHOTT

823 SHPOPT

1883 SINCON

2292 SITOT

1887 SKAMUL

7 SLABEL

2361 SLFLC

1855 SLHASB

1885 SLIN1T

1685 SLPFLO

1882 SMORE

401 SPACE

1856 SPCONV

1864 SPERIM

1884 SPINIT

1857 SPMIN

1636 SQCLDR

1637 SQCLDS

1644 SQCONT

1634 SQHOTR

1635 SQHOTS

1643 SQLOAD

1874 SQMULT

1638 SQRECN

1639 SQSECN

1645 SQWALI

1646 SQWAL3

1577 SRECIR

1859 SRECMN

1578 SRHOI

1579 SRHO2

1580 SRHO3

1581 SRHO4

1582 SRHO5

1860 SSEPMN

1902 STCAVE

1641 STCOLD

1847 STCONT

1642 STECON

1899 STFINE

1900 STFOTE

1863 STGMAX

1640 STHOT


10 STIME

9 STITLE

1897 STPINE

1898 STPOTE

1588 STREFL

1862 STRMAX

1861 STRTUN

1846 STUNE

1589 STWALL

1595 SUSTM

1866 SUSTMN

1867 SVCONV

2283 SVEL31

1876 SVFREF

1877 SVGREF

1878 SVLEGR

1801 SVSVF

1868 SWFMIN

1626 SWOUT

1869 SX2RGI

585 TABMAX

410 TAUIO

411 TAUPT

409 TAURCI

412 TAUXE

2217 TBASE

391 TBL2NU

398 TBL3NU

597 TCFMUL

598 TCGAP

600 TCHFMU

601 TCLEV

670 TCROD

632 TCSATS

657 TCSTM

631 TCWAT

614 TDHFDP

615 TDHGDP

617 TDTDHS

616 TDTDPS

621 TDVGDH

619 TDVGDP

620 TDVLDH

618 TDVLDP

665 TECOOL

609 TESATL

608 TESATP

610 TESATS



Name

603 TFHTGN

641 TFLASH

659 TFLUX

602 TGAPIN

653 TGSTMB

649 THFB

639 THNB

658 THSTM

640 THSUB

656 TIHT

2218 TIME

2222 TIMQUE

654 TKGAP

669 TKROD

627 TKSATS

626 TKSTM

625 TKWAT

634 TLBOIL

642 TLMIXL

430 TMPTBL

16 TNMAXL

17 TNPROP

629 TPRSTM

630 TPRSTS

628 TPRWAT

599 TPSPCR

643 TQAVE

661 TQAXIL

635 TQCRIT

650 TQDNB

662 TQLIQ

663 TQSTM

655 TQZRWA

667 TRADEX

861 TRTOT

2219 TSCALE

611 TSSATL

612 TSSATS

1386 TSTLST

2220 TSTOP

666 TrCOOL

638 TrCRIT

648 ITCROS

637 TTERM2

636 TFERMT

644 "TFUEL

651 TTNBFC

668 'ITROD


613 TISAT

660 TISURF

268 TrWIFR

624 TUSATS

623 TUSTM

622 TUWAT

647 TXFC

568 UNUSED

2272 USR

2282 V3MULT

396 V3TBI

397 V3TB2

395 V3TBL

2358 VBMISC

447 VELIOO

910 VOLMIX

413 VOLSGS

389 VS'I"BI

390 VSMTB2

388 VSTIBL

415 W32FLC

2276 WARNOP

466 WFWIOO

797 XDISP

195 XNEGUP

802 XOFFAV

800 XOFFST

194 XPOSUP

799 XPOWER

798 XPOWRD

801 XPWRAV

566 XTAB

803 XTCONS

567 YTAB

93 ZANN

193 ZINUP

192 ZOUTUP

95 ZSECVA

822 ZSHPIN


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Part 2 of 2, Rev. 00 to WCAP-15996-NP, Technical ...

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Transcript of Part 2 of 2, Rev. 00 to WCAP-15996-NP, Technical ...