19. Appendiks c
-
Upload
yosita-dyah-anindita -
Category
Documents
-
view
221 -
download
0
Transcript of 19. Appendiks c
-
7/25/2019 19. Appendiks c
1/102
C-1
APPENDIKS C
PERHITUNGAN SPESIFIKASI ALAT
1. HAMMER MILL (C-110)
Fungsi :Memperkecil ukuran batubara (50 mm menjadi 1 mm)
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 1 bar = 14.50 psi
Tekanan desain = 1.1 x Tekanan total
= 1.0 psi
Temperatur = !." #C = $0.0 #%
K%"%si&%s :
Mass rate = &5000 k'jam = &5 tonjam
P#$'i&ung%n D%% :
Bond Postulate
(War
= &5 tonjam
= 1&
= 50 mm
= 1 mm
Power = 1!&.5! k* = 15.5 +p
S"#sii*%si A+%& :
%un'si = Memperkecil ukuran batubara (50 mm menjadi 1Tipe =
,apasitas maksimum = 40 - 0 tonjam
= &0 x &0 in
= 1!00 rpm
= ! in
Power = 15.5 +p
,. !PEN ARD C!AL (F-111)
Fungsi : eba'ai tempat pen/impanan atau penampun'an batubara
di'unakan seba'ai ba+an baku proses
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 1 bar = 14.50 psi
Tekanan desain = 1.1 x Tekanan total
= 1.0 psi
Temperatur = !." #C = $0.0 #%
%ng %*%n i'i&ung :
Reversible Haer Mill odel no.505
kuran rotor
,ecepatan ills
Maksimum!eed si"e
olume2 tin''i2 diameter2 dan jumla+ o#en $ard/an' dibutu+kan untuk konstruksi
=0.316 (1/ )1/ ))/ 2_ (_ (_
_
_
_
-
7/25/2019 19. Appendiks c
2/102
C-!
P#$'i&ung%n :
Massa batubara masuk = &5000 k'jam = $40000 k'+
3ensitas batubara = 1&4
eriode pen/impanan = &0 +ariolume batubara masuk = !4.0"
,apasitas pen/impanan = 1$"!!.1&"
,apasitas maksimum = !00000
den'an se+in''a
= 1$"!!.1&"
= 1"$$"&.
3 = 5.&4 m
= 1!0 m
6 = !!.54 m
= 50 m
S"#sii*%si A+%& :
%un'si = eba'ai tempat pen/impanan atau penampun'an batubara /an'
di'unakan seba'ai ba+an baku proses
Tipe =
olume = 1$"!!.1&"
Tin''i = !!.54 m
3iameter = 5.&4 m
6uas = $&0."0
7umla+ = 1 unit
. /ELT C!NE!R I (-11,)
Fungsi :
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 1 bar = 14.50 psi
Tekanan desain = 1.1 x Tekanan total
= 1.0 psi
Temperatur = !." #C = $0.0 #%
K%"%si&%s :
Mass rate = &5000 k'jam = &5 tonjam
S"#sii*%si A+%& :
%un'si =
Buc%et &levator 'Tipe =
k'm&
m&+ari
m&
m&
m&
3& m&
3maks
6maks
Pile #en ard2 den'an tutup berbentuk kerucut
m&
m!
Men'an'kut batubara dari #en ardmenujuBuc%et &leva
Men'an'kut batubara dari #en ard Coalmenuj
*rou+et Belt on -oidler
= ^2/12 =0.4
=0.4 ^3/12
-
7/25/2019 19. Appendiks c
3/102
C-&
,apasitas maksimum = 40 tonjam
= 1 in
6uas pen'an'kutan = 0.14
= 100 8tmin
Power otor = 0.5 +p100 8t,emirin'an =
= &&." in
9a+an = Carbon steel
2. /UCKET ELEAT!R I (-11)
Fungsi :
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 1 bar = 14.50 psi
Tekanan desain = 1.1 x Tekanan total
= 1.0 psi
Temperatur = !." #C = $0.0 #%
K%"%si&%s :
Mass rate = &5000 k'jam = &5 tonjam
S"#sii*%si A+%& :
%un'si =
Haer Mill.
Tipe = Continuous Buc%et &levator,apasitas maksimum = 45 tonjam
= 10 x x : in
Buc%et s#acin+ = 1 in
= !!5 8tmin
Tin''i ele;ator = !5 8t
Power otor = & +p
9a+an = Carbon steel
3. /ALL MILL (C-1,0)
Fungsi : Memperkecil ukuran batubara (1 mm menjadi 021 mm)
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 1 bar = 14.50 psi
Tekanan desain = 1.1 x Tekanan total
= 1.0 psi
Temperatur = !." #C = $0.0 #%
K%"%si&%s :
Mass rate = "0000 k'jam = 1$0 ton+ari
6ebar belt
8t!
,ecepatan belt
!0o
anjan' belt
Men'an'kut batubara dariBelt Conve$or 'menuju
Men'an'kut batubara dariBelt Conve$or'menuj
kuran buc%et
,ecepatan buc%et
-
7/25/2019 19. Appendiks c
4/102
C-4
P#$'i&ung%n D%% :
Bond Postulate (War
= "0 tonjam
= 1&
= 1 mm
= 0.1 mm
Power = !!.1$ k* = $&4.&5 +p
S"#sii*%si A+%& :
%un'si = Memperkecil ukuran batubara (1 mm menjadi 021
Tipe = Marc$ Ball Mill /o. 0 2ieve
,apasitas maksimum = 1"00 ton+ari
= 10 x 10 8t
9eban bola = 5.5 ton
= 1$ rpmPower = $&4.&5 +p
4. SCREENER (H-1,1)
Fungsi : Mendapatkan ukuran sera'am (021 mm) dari serbuk batuba
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 1 bar = 14.50 psi
Tekanan desain = 1.1 x Tekanan total= 1.0 psi
Temperatur = !." #C = $0.0 #%
K%"%si&%s :
Mass rate = "0000 k'jam = "0 tonjam
:
3iameter ka
-
7/25/2019 19. Appendiks c
5/102
C-5
= 1
= 41."
S"#sii*%si A+%& :
%un'si = Mendapatkan ukuran sera'am (021 mm) s
Tipe = Hi+ 2#eed ibratin+ 2creenskuran = 1"0 mes+
3iameter ka
-
7/25/2019 19. Appendiks c
6/102
C-
Temperatur = !." #C = $0.0 #%
K%"%si&%s :
Mass rate = &5000 k'jam = &5 tonjam
S"#sii*%si A+%& :
%un'si =
Tipe =
,apasitas maksimum = 40 tonjam
= 1 in
6uas pen'an'kutan = 0.14
= 100 8tmin
o
-
7/25/2019 19. Appendiks c
7/102
C-"
.
L56 ratio = 4." (memenu+i s/arat)
P#$'i&ung%n D%% :
= 0.!5 - 0.5 ms
Peri#eral s#eed = 0.4 ms = "$."4 8tmin
= = !."!! rpm
3a/a motor = &".& k*
P#$'i&ung%n 9%*&u Tingg%+ :
= 10@
= &04.$$
= &04.
Mass rate = 1510$.5 k'jam
3ensitas = 1&4.00
8eed rate = !.00 = 1$.!
*aktu tin''al = = 0.&&! jam
P#n#n&u%n K#5i$ing%n :
=
-
7/25/2019 19. Appendiks c
8/102
C-$
3iameter = .!1 8t
anjan' = 45." 8t
utaran = !."!! rpm
,emirin'an = &.1 derajat
*aktu tin''al = 0.&&! jam
= !!
= 0."" 8t
9a+an = Carbon steel
Power = 50.0! +p
7umla+ = 1 unit
10. SCRE9 C!NE!R I (-11)
Fungsi :
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 1 bar = 14.50 psiTekanan desain = 1.1 x Tekanan total
= 1.0 psi
Temperatur = !." #C = $0.0 #%
K%"%si&%s :
Mass rate = &5000 k'jam
3ensitas batubara = 1&4
,apasitas = !.00 = 1$.!
S"#sii*%si A+%& :
%un'si =Bin Pulveri"ed Coal
Tipe = Loadin+ o! Material in *rou+t Class '':7/@
-
7/25/2019 19. Appendiks c
36/102
C-&
= ".! 8t = 1.41 in
Tekanan total = Tekanan operasi
= !" bar = &1.0 psi
Tekanan desain = 1.1 x Tekanan total
= 4&0.$ psi
Temperatur = 1".$ #C = &$$.04 #%
9a+an konstruksi = 2=:10G 4rade 11 *$#e 310
=llowable stress = 1"500 psi
Corrosion !actor = 0.1!5 in
Welded !actor = 0.$0
a). Tebal dan Tin''i ilinder
Tebal silinder = = 1.5 in = 1.
3iameter luar = 4. in = .00 in (standarisasi)
3iameter dalam = !."5 in
Tin''i silinder = 1&.1& in
b). Tebal dan Tin''i Tutup 9a
-
7/25/2019 19. Appendiks c
37/102
C-&"
3iameter = .00 in
Tin''i total = 1"0.4" in
Tebal silinder = 1.& in
Tipe tutup atas = 2tandard dised ead
Tebal tutup atas = 1.&$ in
Tipe tutup ba
-
7/25/2019 19. Appendiks c
38/102
C-&$
aD = 0.!1$
aE = 0.&
Clearance = 0.!5 in
Pitc = 1.!5 in (trian+ular #itc)
Passes = !K%"%si&%s :
2$n+as = $!"50.$4 k'jam = 1$!4&4.1"$ lbjam
Boiler 8eed Water = !1!1$.5$&5 k'jam = 4""$.1$& lbjam
= 4&0 #%
= 1."4
= 0.&
= 0.50
= 40$ #%
Caloric Temperature $
= = "1."! #%= = !"!.!1 #%
&erall !eat Transfer Coefficient $
= 0.01
= 40
= 5."0Q0" k7 = 5.40Q0" 9tu
= &&0".4 = 4"!"&.
= 505.&4 = 5&$ (standarisasi)
= &".5"
E%+u%si P#$"in%'%n P%n%s :
(oiler Feed 'ater $ Shell Side Syngas $ Tu
= 0.55 =
8t!8t
in!
P#n#n&u%n BTLMTD
:
ST!actor (%T)
ST6MT3
TC
Ta;e
tC
ta;e
,arena air dan s$n+as dapat diasumsikan seba'ai non:viscous !luid dan buk+/drocarbon2 maka perbandin'an antara (AA
(6_ ) )^(1/3)? /1
' =' )_ _ (_/_
=(' ' )/(' +' )_6 _ < _ _ _
: = __ (_6)/ (_6 <
)_
2 +1))/(5.22_ (# < 10 ^10 < _> )_
=_ ( _ ^2 )/(5.2 = 2< 10
$^2/ *25 62.5/144
= ^2/ *_ 4=/ $ 25
=_ +_
= )/(_:> (_ < _> 2.42)? _ )/( < _ 2.42)? (6_ ) )^(1/3) )^0.14? /1 (?/?_B
$=_/(3600 )
' =' )_ _ (_/_
=(' ' )/(_6 _ < _ '_+'_)
: = __ (_6)/ (_6 <
)_
2 +1))/(5.22_ (# < 10 ^10 < _> )_ =_ ( _ ^2 )/(5.2 = 2< 10
$^2/ *25 62.5/144
= ^2/ *_ 4=/ $ 25
=_ _+
-
7/25/2019 19. Appendiks c
47/102
C-4"
Fungsi :
Konisi !"#$%si :
Temperatur &! #C
Tekanan ! bar = &"".10 psi
C%$% K#$;% :
1) Deaktan masuk > melalui ba'ian atas
M#ng'i&ung o+u5# To&%+ Aso$=#n :
= $0$ k'jam
= !!.
6aju massa aliran produk = 44!1.&1 k'jam
= "44". k'jam
9entuk Pellet (s#ere)
50
2ur!ace area 0."
0.& mm
0.&
,apasitas pen/erapan 0.!!
= =
= $$"!.&"$$& k'
= 1&&.5
= &5!!.4&
= 0.0$ ms = !$4.40
6uas permukaan (>) = = 1!.&
3iameter adsorben = &." m = 15.&$
Tin''i adsorben = 10." m = 4!4.$4
olume ruan' koson' = 10@
olume total = 14$.50 = 5!44.!!
Tekanan total = Tekanan operasi
= ! bar = &"".10 psi
Tekanan desain = 1.1 x Tekanan total= 414.$ psi
Memisa+kan produk +idro'en dari i#urities +in''a kemurnian
!)8eedakan mele terdapat 4 bua+ vessel2 se+in''a olecular sieveuntuk tiap vesseln/a
Molecular sievetiap vessel
olume bed m&
M#ng'i&ung Di%5#$ %n TinggiPressure Swing ,dsorption:
6aju ;olumetrik!eed m&jam
2u#er!icial velocit$(;)
m!
m&
Konisi D#s%inPressure Swing ,dsorption:
)(_
)/ )(@ 5> (7 >=D>=
!/$
-
7/25/2019 19. Appendiks c
48/102
C-4$
Temperatur = &! #C = $. #%
9a+an konstruksi = Carbon steel 2=:-; 4rade 6 *$#e ;3
=llowable stress = 1"500 psi
Corrosion !actor = 0.1!5 in
Welded !actor = 0.$0
a). Tebal dan Tin''i ilinder
Tebal silinder = = !.4$ in = !.
3iameter luar = 11.&$ in = 1$.00 in (standarisasi)
3iameter dalam = 1&.00 in
Tin''i silinder = 45.40 in
b). Tebal dan Tin''i Tutup 9atas
r = 144 inicr = 10 1$ in
= = !.0! in
= = !".54" in
Tin''i total = Tin''i silinder Tin''i tutup atas Tin
= 511.4 in
S"#sii*%si A+%& :
%un'si =
Memisa+kan produk +idro'en dari impurities +in''a k
Tipe = 8ied Bed
Temperatur operasi = &! #C
Tekanan operasi = ! bar
,apasitas = 5!44.!!
3iameter = 1$.00 in
Tin''i total = 511.4 inTebal silinder = !.50 in
P#n#n&u%n T#=%+ %n TinggiPressure Swing ,dsorption:
Tebalstandard dised ead
Tin''istandard dised ead
Tebalstandard dised ead
Tin''istandard dised ead
d). Tin''i TotalPressure 2win+ =dsor#tion
8t&
(_)/2 0,6_ (,) +C_
(0,%%5_)/2 0, ) (, ._
+C
0,169_
(0,%%5_)/2 0, ) (, ._
+C
0,169_
-
7/25/2019 19. Appendiks c
49/102
C-4
Tipe tutup atas = 2tandard dised ead
Tebal tutup atas = !.!5 in
Tipe tutup ba
-
7/25/2019 19. Appendiks c
50/102
C-50
Tekanan operasi = !5.& bar
,apasitas = 1$05."&
3iameter = 54.00 in
Tebal = 4.00 in
9a+an konstruksi = Hi+ =llo$ 2teel 2=:-; 4rade BTipe pen'elasan = 6ouble Welded Butt >oint
7umla+ alat = $ bua+
Fungsi :
Konisi !"#$%si :
Tekanan total = Tekanan operasi
= 0.&4 bar = 4.& psi
Tekanan desain = 1.1 x Tekanan total= 5.4 psi
Temperatur = !5.1 #C = "".1$ #%
K%"%si&%s :
Mass rate = "44". k'jam = 1$5&$.&0$ lbjam
P produk = 5!.4
Residence tie = 1! jam
olume produk = 1"4"".0
7umla+ tan'ki = $
2a!et$ !actor = 10@
= !40&.10
= = 0.5!
3iameter dalam = 14. m = 5$$.4 in
Material ba+an = Hi+ =llo$ 2teel 2=:-; 4rade B
=llowable stress = 1"500 psi
Welded !actor = 0.$0
Corrosion !actor = 0.1!5 in
Trial tebal tan'ki = 0.$$ in
3iameter luar = 50. in
= = !5.&5 in
= &.&$ in
9 = = 5000.00
= 14.$1 psi
8t&
0. C!,-RICH ST!RAGE TANK (F-,,)
Menampun' sementara produk CH!-ric
k'm&
m&
,apasitasstora+e m&
olumes#erical m&
,arena tekanan dalam tan'ki lebi+ kecil dari tekanan atmos8ir2 perlu didetekanan eksternal.
rc
3en'an ?ra8ik $.$ (9rollo
-
7/25/2019 19. Appendiks c
51/102
C-51
= .!$ psi
3iameter luar = 5!.44 in = 00.00 in (standarisasi)
3iameter dalam = 5$.!5 in
S"#sii*%si A+%& :
%un'si =
Tipe = 2#erical *an%
Temperatur operasi = !5.1 #C
Tekanan operasi = 0.&4 bar
,apasitas = !40&.10
3iameter = 00.00 in
Tebal = 0.$$ in
9a+an konstruksi = Hi+ =llo$ 2teel 2=:-; 4rade BTipe pen'elasan = 6ouble Welded Butt >oint
7umla+ alat = $ bua+
>ctual
7ika dibandin'kan antara >lloctual
2 maka tebal tan'kis#ericalmemenu+i.
Menampun' sementara produk CH!-ric
8t&
-
7/25/2019 19. Appendiks c
52/102
C-5!
ren L. Mc Cabe, 1993)
m)
(Perr$, 199G)
an'
.
-
7/25/2019 19. Appendiks c
53/102
C-5&
ari
(www.sietric.co.u%)
(Ilric, 197;)
(Ilric, 197;)
(Ilric, 197;)
(Ilric, 197;)
(Ilric, 197;)
tor '
-
7/25/2019 19. Appendiks c
54/102
C-54
(Perr$, 199G)
(Perr$, 199G)
Haer Mill
-
7/25/2019 19. Appendiks c
55/102
C-55
ren L. Mc Cabe, 1993)
mm)
(Perr$,199G)
a
(Perr$,199G)
(Perr$,199G)
(Perr$,199G)
(Perr$,199G)
-
7/25/2019 19. Appendiks c
56/102
C-5
(Perr$,199G)
rbuk batubara
(Perr$,199G)
''
ill untuk di-rec$cle
-
7/25/2019 19. Appendiks c
57/102
C-5"
(Perr$,199G)
ren L. Mc Cabe, 1993)
ren L. Mc Cabe, 1993)
ren L. Mc Cabe, 1993)
uju
n'
T!
-
7/25/2019 19. Appendiks c
58/102
C-5$
(Ilric, 197;)
(Perr$,199G)
(Robert *re$bal, 1971)
(Perr$,199G)
ri 11! sampai den'anmpai den'an ti'a kali
oisture
-
7/25/2019 19. Appendiks c
59/102
C-5
(www.sietric.co.u%)
ull
(2tanle$ Walas, 199)
Coal
m
r
-
7/25/2019 19. Appendiks c
60/102
C-0
(www.sietric.co.u%)
(Ilric, 197;)
(=2M& 190)
$$15.55
$$15.55
$$15.55
(Ilric, 197;)
(Brownell, 19G9)
(=2M& 190)
1 in (standarisasi)
1 in (standarisasi)
8t&
8t&
8t&
si!ier
-
7/25/2019 19. Appendiks c
61/102
C-1
(www.sietric.co.u%)
ull
(2tanle$ Walas, 199)
r$er
m
l
s
a+ +asi!ier,sedan'kan
-
7/25/2019 19. Appendiks c
62/102
C-!
(Levens#iel, 1999)
(6avid =. Bell, -11)
1
(Rule o! tubs)
radian
2tandard dised ead)
t diasumsikan seba'aialiran solid #lu+ !low2
n
8t&
-
7/25/2019 19. Appendiks c
63/102
C-&
(Conical)
in
ess 'nternational, inc)
(=2M&, 190)
1 in (standarisasi)
1 in (standarisasi)
= 0.&1 in
(standarisasi)
dised ead
-
7/25/2019 19. Appendiks c
64/102
C-4
(*.>. Par%, -)
(6.@. Fern, 190)
(6.@. Fern, 190)
ess 'nternational, inc)
(6.@. Fern, 190)
= 0.$ m
m
iasa di'unakan untuktas renda+. edan'kan
si melalui ba+an padat
an%o#lis ;ted., -3)
_ ) ) )(1_) ()
_2 )
-
7/25/2019 19. Appendiks c
65/102
C-5
m
m
m
in
ess 'nternational, inc)
(=2M&, 190)
1 in (standarisasi)
m!
m!
m!
m!
'ambar di sampin'2a dalam satu vessel.tup ba
-
7/25/2019 19. Appendiks c
66/102
C-
= 0.&$ in
(standarisasi)
ara
toit
-
7/25/2019 19. Appendiks c
67/102
C-"
(Perr$, 199G)
(www.sietric.co.u%)
(=2M&, 190)
er
-
7/25/2019 19. Appendiks c
68/102
C-$
(Hesse and Ruston)
in
(Brownell, 19G9)
(Brownell, 19G9)
(=2M&, 190)
in (standarisasi)
sasi)
(Brownell, 19G9)
4 in (standarisasi)
0.&$ in
(standarisasi)
er
!ier
-
7/25/2019 19. Appendiks c
69/102
C-
(=s#en Plus)
(=2M&, 190)
(Fusnaro, -1)
-
7/25/2019 19. Appendiks c
70/102
C-"0
(standarisasi)
1 in
(standarisasi)
1 in
(standarisasi)
(6.@. Fern, 190)
(6.@. Fern, 190)
= 5.1$ m
m
m
m
m
an%o#lis ;ted., -3)
m!
m!
_ ) ) )(1_) ()
_2 )
-
7/25/2019 19. Appendiks c
71/102
C-"1
in
m!
m!
lam
si
_5 _4 )& _ ) ) )( (1_ (
-
7/25/2019 19. Appendiks c
72/102
C-"!
(=s#en Plus)
(6.@. Fern, 190)
'kan pipa.
,
-
7/25/2019 19. Appendiks c
73/102
C-"&
8t.lb8lb
m
an%o#lis ;ted., -3)
-
7/25/2019 19. Appendiks c
74/102
C-"4
(6.@. Fern, 190)
(6.@. Fern, 190)
tur
-
7/25/2019 19. Appendiks c
75/102
C-"5
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(=s#en Plus)
e Side
0.1!
an #etroleu maupun
8t!
!
-
7/25/2019 19. Appendiks c
76/102
C-"
.
0.01$"$ cp
(=s#en Plus)
1!10$4
e Side
1!10$4.1
0.0001&
(6.@. Fern, 190)
= 0.0001 psi
0.01 psi
(6.@. Fern, 190)
0.04 psi
0.04 psi
.
9tu+r.8t!.#%
andar desain)
8t!in!
n
10 )< _
-
7/25/2019 19. Appendiks c
77/102
C-""
(2.. Foarov, -;)
(Rule o! tubs)
2tandard dised ead)
2tandard dised ead)
-
7/25/2019 19. Appendiks c
78/102
C-"$
(Brownell, 19G9)
(=2M&, 190)
in (standarisasi)
= !.!5 in
(standarisasi)
= !.!5 in
(standarisasi)
tup ba
-
7/25/2019 19. Appendiks c
79/102
-
7/25/2019 19. Appendiks c
80/102
C-$0
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(=s#enPlus)
#e Side
0."0
."
0.0& cp
(6.@. Fern, 190)
100.
an #etroleu maupun
8t!
lbjam.8t!
-
7/25/2019 19. Appendiks c
81/102
C-$1
(6.@. Fern, 190)
(=s#en Plus)
9tulb.#%
(=s#en Plus)
.4
e Side
100.
0.00015
(6.@. Fern, 190)
= 0.000! psi
0.0!5 psi
(6.@. Fern, 190)
0.!0 psi
0.!0 psi
9tu+r.8t!.(#%8t)
9tu+r.8t!.#%
9tu+r.8t!.#%
andar desain)
8t!in!
)^0.14?/?_B
^10 )
-
7/25/2019 19. Appendiks c
82/102
C-$!
(>in+in+ ao, -1-)
(=2M&, 190)
(Rule o! tubs)
2tandard dised ead)
2tandard dised ead)
(Brownell, 19G9)
(=2M&, 190)
$ in
(standarisasi)
-
7/25/2019 19. Appendiks c
83/102
C-$&
= 1."5 in
(standarisasi)
= 1."5 in
(standarisasi)
'i tutup ba
-
7/25/2019 19. Appendiks c
84/102
C-$4
ri H. Hassan, -7)
apasitas adsorpsi 0@)
(Rule o! tubs)
2tandard dised ead)
2tandard dised ead)
in
bas dari G!
8t&
-
7/25/2019 19. Appendiks c
85/102
C-$5
ess 'nternational, inc)
(=2M&, 190)
in (standarisasi)
= 0.50 in
(standarisasi)
= 0.50 in
(standarisasi)
utup ba
-
7/25/2019 19. Appendiks c
86/102
C-$
(Haidre"a B., -7)
(Rule o! tubs)
2tandard dised ead)
2tandard dised ead)
!
-
7/25/2019 19. Appendiks c
87/102
C-$"
(Brownell, 19G9)
(=2M&, 190)
& in(standarisasi)
= 1.&$ in
(standarisasi)
= 1.&$ in
(standarisasi)
ba
-
7/25/2019 19. Appendiks c
88/102
C-$$
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
untuk
-
7/25/2019 19. Appendiks c
89/102
C-$
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(=s#enPlus)
#e Side
1.1
an #etroleu maupun
8t!
!
-
7/25/2019 19. Appendiks c
90/102
C-0
.
0.0& cp
(6.@. Fern, 190)
440$.1
(6.@. Fern, 190)
(=s#en Plus)
9tulb.#%
(=s#en Plus)
."
e Side
440$.1
0.00015
(6.@. Fern, 190)
= 0.0000! psi
0.0!5 psi
(6.@. Fern, 190)
0.!0 psi
0.!0 psi
.
9tu+r.8t!.(#%8t)
9tu+r.8t!.#%
9tu+r.8t!.#%
andar desain)
8t!in!
)^0.14?/?_B
^10 )
-
7/25/2019 19. Appendiks c
91/102
C-1
(Rule o! tubs)
(Brownell, 19G9)
(=2M&, 190)
5 in
(standarisasi)
-
7/25/2019 19. Appendiks c
92/102
C-!
= 1.1& in
(standarisasi)
= 1.1& in
(standarisasi)
ba
-
7/25/2019 19. Appendiks c
93/102
C-&
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
-
7/25/2019 19. Appendiks c
94/102
C-4
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(=s#enPlus)
e Side
0.$4
.0
0."5 cp
(6.@. Fern, 190)
!!45".
!.1"
&.&5 8ts
0.5
(6.@. Fern, 190)
$"
an #etroleu maupun
8t!
lbjam.8t!
lb8t&
9tu+r.8t!.#%
9tu+r.8t!.#%
9tu+r.8t!.#%
-
7/25/2019 19. Appendiks c
95/102
C-5
e Side
!!45".
0.00015
(6.@. Fern, 190)
= 0.01 psi
0. psi
(6.@. Fern, 190)
4.$0 psi
4.$1 psi
andar desain)
8t!in!
suki
^10 < _)
-
7/25/2019 19. Appendiks c
96/102
C-
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(6.@. Fern, 190)
(=s#enPlus)
an #etroleu maupun
-
7/25/2019 19. Appendiks c
97/102
C-"
e Side
1.54
.4
0."5 cp
(6.@. Fern, 190)
115&.4
!.1"
1."! 8ts
(6.@. Fern, 190)
$"
e Side
115&.4
0.00015
(6.@. Fern, 190)
= 0.005 psi
0. psi
(6.@. Fern, 190)
4.$0
4.$1 psi
8t!
lbjam.8t!
lb8t&
9tu+r.8t!
.#%
9tu+r.8t!.#%
9tu+r.8t!.#%
andar desain)
8t!in!
^10 )
-
7/25/2019 19. Appendiks c
98/102
C-$
&4"4$.515& k'
mjam
in
in
2@
den'an data seba'ai
(Perr$ 0ted, 197;)
8t&
-
7/25/2019 19. Appendiks c
99/102
C-
(Brownell, 19G9)
(=2M&, 190)
0 in
(standarisasi)
= !.!5 in
(standarisasi)
= !.!5 in
(standarisasi)
''i tutup ba
-
7/25/2019 19. Appendiks c
100/102
C-100
2@
(Browneel, 199)
in (standarisasi)
2@
-
7/25/2019 19. Appendiks c
101/102
-
7/25/2019 19. Appendiks c
102/102