refrigeration screw compressor package - GPA Midstream
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Transcript of refrigeration screw compressor package - GPA Midstream
REFRIGERATION SCREW
COMPRESSOR PACKAGE
“WHAT FEATURES DO I NEED
FOR MY GAS PROCESSING
FACILITY?”
April 2019
Introduction
• Most midstream gas dew point or liquid recovery facilities require
mechanical refrigeration equipment.
• Compression is a key component of any mechanical refrigeration
plant.
• Since the 1980’s, oil flooded screw compressors have been the
compressor of choice in refrigeration systems.
• Despite their wide use, screw compressor drivetrain specifications
are not clear or uniform throughout the industry.
Presentation Outline
• Oil flooded screw compressors;
• Types of compressor drivetrains;
• Compressor lubrication system;
• Other parts of the drivetrain;
• Package specifications; and
• Case study.
Oil Flooded Screw CompressorsGeneral overview
• Positive displacement machines;
• Off-the-shelf design with standardized rotor diameters and typically 3-4
various rotor lengths for each rotor diameter;
• Approximately 10,000 ACFM (maximum) at suction per machine;
• Driven by 2 or 4 motor drives or gas engines, up to 10,000 BHP;
• Lube oil is used for bearing and seal lubrications, sealing of meshing
rotors sealing, and cooling of the compressed gas;
• Slide valve capacity control is set to 15-20% of its maximum capacity;
• Oil carryover is less than 10 or 1 parts per million on weight basis.
*Illustration courtesy of Howden
Oil Flooded Screw CompressorCompressor standard design features
Standard features include:
• Cast or ductile iron compressor casing;
• Machined steel or ductile iron rotors;
• Forged steel design is preferred with larger diameters.
• Sleeve or anti-friction radial bearings;
• Angular contact thrust bearings;
• Single mechanical shaft seal;
• Slide valve capacity control;
• Vi radial discharge port size adjustment (axial port size fixed); and
• Single side port for economizing of the refrigeration cycle.
Oil Flooded Screw CompressorCompressor options
Common options include:
• Steel compressor casing;
• Forged steel small diameter rotors;
• Tilting pad thrust bearings;
• Dual wet/dry mechanical shaft seal with seal support system; and
• Male/female rotors proximity position probes.
Other options (not common):
• Radial bearing RTD probes;
• Dual or tandem wet/wet mechanical shaft seal;
• Dry gas shaft seal; and
• Flanged compressor casing connections.
Oil Flooded Screw CompressorCompressor – sectional view with dual shaft seal
and tilting pad thrust bearings
*Illustration courtesy of Howden
Oil Flooded Screw CompressorJournal and Thrust bearings, shaft seal details
*Illustrations courtesy of Howden
Oil Flooded Screw CompressorDual/Wet shaft seal support system
• API 75 plan
collects oil from
the seal in the
accumulator.
• Optional API 72
plan provides a
buffer gas to
cavity between
the seals.
Compressor DrivetrainsDriver types
• Screw compressors can be driven by an electric motor or a gas
engine.
• Majority of the electric motor drivetrains are direct coupled and
operate at two-pole motor speed (3550 or 2950 rpm for 60 or 50
Hertz power, respectively).
• Typical midstream refrigeration compressor power is between 1500
and 4000 HP per train.
• Engine operating speeds range between 1400 and 1000 rpm for the
above horsepower range and engine drives typically require a
gearbox to speed the compressor above the engine speed.
• Gearboxes can be stand alone, bolted to the engine, or built into the
compressor. The two latter options are typical for horsepower below
2000.
Compressor DrivetrainsElectric motor drivetrain
Lube oil separator
Electric motor Compressor
Compressor discharge piping
Package
discharge piping
Compressor/package
suction piping
Compressor
sideport piping
Compressor DrivetrainsEngine drive with a compressor internal gearbox
Compressor with a gearbox
Gas engine
Utility water cooler
Engine exhaust
and silencer
Lube oil separator
Compressor/package
suction piping
Package
discharge piping
Compressor sideport piping
Compressor DrivetrainsEngine drive with external gearbox
Gas engine
Compressor
External gearbox
Engine exhaust
Engine air intake
Lube oil separator
Lube oil cooler
Compressor/package
suction piping
Package
discharge piping
Compressor LubricationTypical components
• Lube oil separator
• Lube oil filter(s)
• Instrumentation and controls
• Lube oil pump(s) (if required)
• Lube oil cooler(s) (if required)
• Pipes, valves, etc.
Compressor LubricationOil Cooling methods
Basic lube oil cooling methods include:
• Separate dedicated aerial lube oil cooler:
• Oil cooled directly;
• Oil cooled by glycol/water solution (glycol cooled in the air cooler);
• Pros – proven and reliable; and
• Cons – additional cost, additional motor and a fan, cooler mounted externally.
• Thermosyphon lube oil cooler:
• Oil cooled by condensed refrigerant;
• Pros – proven, reliable, utilizing excess condenser surface for oil cooling duty; and
• Cons – careful refrigerant piping required, condenser elevation requires careful
evaluation.
Compressor LubricationOil Cooling methods
Basic lube oil cooling methods (cont’d):
• Liquid Injection oil cooling:
• Liquid refrigerant injected into the compressor chamber keeping the discharge
gas/oil mix temperature below maximum allowable.
• Pros – lube oil cooler not required.
• Cons:
• Liquid refrigerant injected into compression chamber via a high quality
control valve;
• Compressor capacity decreases and power draw increases due to additional
volume of gas compressed by the machine for the same refrigeration duty;
• Expected capacity decrease is 3-5%;
• Expected power increase is 3-5%;
• May not be an issue if compressor frame has excess capacity.
• Sudden changes in compressor condensing/discharge pressure could cause
foaming of the oil due to increased refrigerant dilution in lube oil.
Compressor LubricationNote on oil carryover and recovery
• Typical oil carryover for
a compressor package
is less than 10 ppmw.
• This typically is not an
issue in the refrigeration
systems because oil
can be recovered from
the system evaporators
and returned to the
compressor.
• If liquid refrigerant is fed to brazed aluminum exchangers, a secondary
high efficiency coalescing oil separator reducing the oil carryover to less
than 1 ppmw would be recommended.
Other parts of the drivetrain
Other parts of the system consist
of:
• Structural steel baseplates;
• Piping and valves; and
• Control systems.
Items to consider also include:
• The role of economizer port;
• Volume ratio (discharge port)
adjustment; and
• A need of suction scrubber.
For details refer to the 2019
Convention paper submitted to GPA
Midstream
Package Specifications
• Reciprocating compressors can be specified as manufacturer
standard, in accordance to API 11P - ISO 13631 (Specification for
Packaged Reciprocating Compressors for Oil and Gas Production
Services) or to API 618 (Reciprocating Compressors for Petroleum,
Chemical, and Gas Industry Services).
• Midstream industry very rarely requires reciprocating compressors
built to API 618.
• Screw compressors can be supplied to manufacturer standard or
API 619 (Rotary-Type Positive-Displacement Compressors for
Petroleum, Petrochemical, and Natural Gas Industries).
• There is not a specification that would be equivalent to API 11P for
the screw compressor packages.
Package SpecificationsAPI versus non-API - compressor
Design features API 619 style unit Midstream standard unit
Compressor design
Casing material Cast Steel for flammable gases Cast Iron for small compressors
Nod Iron for large compressors
Rotors Forged steel Ductile iron, Steel bar or forged steel
based on suppliers’ manufacturing
process
Mechanical seal Double mechanical type with seal
support systems
Single mechanical
Lube oil connections for
compressor casing
NPT or optional flanged with stub pipe NPT
Condition monitoring X-Y casing vibration transmitters,
male/female rotor axial position
proximity probes, optional radial
bearing RTD’s
Single casing vibration transmitters
Compressor testing Witnessed or Unwitnessed
API 619 4 hr performance test
Casing hydraulic test
Rotor balance test
Air under water leak test
Additional optional tests
Helium under water leak test
Casing RT
Casing MPI
UT of casting and rotor stock
Noise test
Vibration spectrum
Unwitnessed
Vendor standard mechanical run test
Casing hydraulic test
Rotor balance test
Air under water leak pressure test
Studies Torsional and lateral study
Gas correlation or performance test
None (except for special drive train
configuration)
Package SpecificationsAPI versus non-API - package
Design features API 619 style unit Midstream standard unit
Package design
Baseplate Multi-runner heavy duty structural skid
with deckplate and drip rim
Multi-runner structural steel skid with
optional deckplate and drip rim.
Process Piping B31.3 piping with minimum 5% RT, 1/8”
corrosion allowance, API style isolation
valves
B31.3 piping 5% RT, 1/16” corrosion
allowance, Refrigeration or API style
isolation valves.
Oil separator design 2-minute lube oil retention time
minimum
Packager standard lube oil retention
time, typically in a range between
30 seconds and 1 minute.
Lube oil pumps Dual (2x100%)
Steel casing (option)
None or Single
Cast iron casing
Lube oil coolers Dual (2x100%) Single or Liquid Injection
Lube oil filters Dual Single or dual
Lube oil piping Carbon steel piping upstream of the
filters, stainless steel piping
downstream of the filters. Optional
stainless steel piping upstream of the
filters. Stainless or carbon steel valves.
Carbon steel piping upstream of the
filters, carbon steel or optional stainless
steel piping downstream of filters with
carbon steel valves.
Coupling API 671 Non API, flexible disc
Relief Valves API 520/521, optional dual API 520/521, single
Valves API valves API or refrigeration valves
Control Instruments and
wiring
Separate Instruments for control and
shutdown (SIS), both having SIL 2/SIL 3
rating, SMART, Class 1, Div.2, Group C
&D (or IEC Zone 2, Group IIB)
Single instruments for control and
shutdown, SMART Class 1, Div.2, Group C
&D (or IEC Zone 2, Group IIB) for most
cases, optional blind non-rated
Control Panel PLC or DCS control panel. Separate
panel for shutdown (SIS) functionality
Single PLC control panel. Optional
microprocessor panels with blind
instruments.
Case StudyRefrigeration Compression for a typical cryo plant
• A typical 200-300
mmscfd cryo plant
utilizes multiple
compressors driven by
2000-3500 HP motors,
depending on the plant
design and inlet gas
composition.
• We decided to look at a
3500 HP compressor
drivetrain, and compare the typical design
versus a unit following API 619 guidelines.
Case StudyTypical midstream compressor package
Basic design consists of: • Non-API motor;
• Cast iron compressor case;
• Single compressor mechanical shaft
seal;
• Single lube oil pump;
• Dual lube oil filters;
• ASME vessels and piping;
• Air cooled lube oil cooler;
• 1/16” corrosion allowance;
• 5% RT;
• API gate and globe isolation;
• all carbon steel;
• PLC control system with SMART
instrumentation;
• common devices for shutdown and
control; and
• rotor axial position probes.
Case StudyCompressor package following API 619 guidelines
API design consists of: • API motor;
• Cast steel compressor case;
• Dual compressor mechanical shaft seal
with API 72/75 seal plan;
• Dual API lube oil pumps and dual lube oil
filters;
• ASME vessels and piping;
• API air cooled lube oil cooler;
• 1/8” corrosion allowance;
• 100% RT;
• Ball isolation valves;
• All carbon steel;
• PLC control system with SMART
instrumentation including separate
instruments for shutdown and control; and
• Extensive Machine Monitoring
instruments.
Case StudyHow do units compare?
• No rating difference;
• Both packages have the
same refrigeration capacity,
efficiency, and motor power.
• Typical package would be about
40% less expensive.
• Typical package delivery would be
about 3 months shorter.
• Removing external lube oil cooler
would reduce both package costs
by about 10%, decrease unit
capacity by 3% and increase
power draw by 4%.
Case StudyConclusion
• Careful features considerations
are recommended.
• Some API 619 features may be
worthwhile depending on the plant
operating philosophy, number of
units employed, etc.
• Simply requiring “API 619
compliance” should be properly
evaluated.
• There is not a right or wrong
design.