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6" 12"
SIDE
/UNIT
VAPOR
HC
(2)
kg/hr (lb/hr)
105)
<STREAM No.> 271 INLET<
r11>
kg/hr (lb/hr) 6(5
OUTLET<r12> 23802(52483)
90083(198633)
82585I(N18L2E1T0<52>
OUTLET<53>
0)
63151(139248)
3mm CS
NO SHELLD STIDUEB:E SIDE:
CS + NAASCMEE SECT
TUBES:
MAX. LENGTH:
CORROS
TUB
MATERI
ETSU:B
UCHLA
MULTITUBES NNE
INLET: ALLOWED:
6IN" LET:
12"
OUTLET: OUTLET:
3CmSm +NCASCE +NACE CS+NA
CHARAC T ER I S T IC S
INLET
OUTLET
INLET
OUTLET
MOLECULAR WEVIGAHPTOR
58.1
kDgE/NkSgImToYl(lAb T/lbOmPoEl)R. TVEISMCPO. SITY AT OPER.
29(.856 kg/m3 (lb/ft3) 504.0(0
STPHEECRIMFIACLHCEOANTD.
kCal/kg.
906.0(1
0.4305(0.4305)
60).0322(0.021
0.6798(0.6798)
kECNaTl/HmA.hLrP.oYC(BTU/ft.hr.oF)
405.2(1
0.0146(0.0098)
67).1313(28.29
Cli ent Sit e: Un it: D
[1] [1
1]
[1
PROC E S S DA TA
PROCESS SPECIFICATION HEAT EXCHANGER
GC28
ITEM NO.: 28-E-1505 -SPP
Rev. TYPE: 3
Pag
CPHale Waihona Puke Baidu
/S2E5R0V5ICE: HP
(AVER
0.00023 (10 TO
SPECIFIC GRAVITY LIQUID
6S0P/E6C0IFIC GRAVITY AT
OVPISECRO. STIETMYPA. T OPER.
TEMP.
STPHEECRIMFIACLHCEOANTD.
kCal/kg.
kECNaTl/HmA.hLrP.oYC(BTU/ft.hr.oF)
AKU TEMA
COMPRESS0R TRIM
AMGMEkCal
(
DOUPETRYA/TUINOINT: SUMMER
1.713 /hr
NO. OF 6.797
CFLAUSIED W: ITHOUTSHGEALSL
UNITS:
TWO
SIDE:
SHELL
TUBE
TOTAL FLOW RATE
S24ID08E4(53
MMkCal/hr (MMBTU/hr)
POUR POINT
cP (cP) oC (oF)
INLET 0.57 407.55 01.15 04.5(9 805.0(7 4- 3( 0.05
OUTLET
0.5761 0.5507 0.1493(0.1493) 0.5997(0.5997) 0-0.0.0704066(0(-.0501) 0.0024)
0.0314(0.0211)
1]
MLAMTkECNaTl/hHrE(MATMBTU/hr)
0(0.
1.8649(7.400)
7)
5.1698(20.5137)
MMkCal/hr (MMBTU/hr)
PA SHELL SIDE: TUBE SIDE:
SHE
LMLA:
XCO.
RMRA
TER
SHE
FLOATING
H20
kg/hr (lb/hr)
178(392)
63(139)
NONCONDENSABLES
LIQUID
HC
213 kg/hr (lb/hr) 68(
282(622)
7042(15528)
26478(58384)
H20
OPERATING TEMPERATURE ODPEESRIGANTITNEGMPPERREASSTURE oC (oF)
INLET
0.5273 0.40176824(0.078 40).7899(0.789 90).0628(0.042 20).0815(0.323 4)
OUTLET
0.4913 0.4256 0.0762(0.0762) 0.7632(0.7632) 0.067(0.045) 0.330(1.3095)
[3]
A4.SSOUUMREDSETROVIBCEE A(GAS
C5.ONATBAOINOST FHO2SR L( UMBAEXI.
O6.IOLPDERRAAITNIINNGG TO BE
[1]
FLOWRATE AND HEAT
CONSTRUCTION MCOANTSETRRIAULC:TION CODE:
DALELSOIGWNAPBRLEESSPURRESESURE DROP VFOAUCLUIUNMG FRAACTTINOGR m2.hr.0C/kCal(ft2.hr.0F/BT FLEXIBILITY
kg/hr (lb/hr) 35.3 (29.957.
kg/cm2 g (psig) (42.
kg/cm2 g (psig) kg/cm2 (psi)
kg/cm2 a (psia)
%
36(96.8) 100 2.97(42.23) ( 21213) .3 (188.6 ) NEGLIGI
0.0100023 TO
278(613)
391(862)
57.8(136)
40(107)
68.26(970.66) 180 67.75(963.41)
( 37566.5) (1008.75.18 (7.25 )
BDOTUTBOLME :PIPE
APRLOLOCWESESDL: INES
DIAMETER:
NO
[1] TE:
1. TRIM COOLER IS BY PACSOSNESDIDIENRWEDINCTAERSE.
W2. HTIWCHO OISUBTALSEETDS FOONR
V3.ARPOEFRR. IGERANT IS
58.12(58.12) 9.8131(0.6123)
29.29(29.29) 100.051.8559(60.60015)
27.16(27.16) 102.99(6.427)
TEMP.
cP (cP) 708.4(2
0.0078(0.0078)
90).6776(0.677
0.0153(0.0153)
SIDE
/UNIT
VAPOR
HC
(2)
kg/hr (lb/hr)
105)
<STREAM No.> 271 INLET<
r11>
kg/hr (lb/hr) 6(5
OUTLET<r12> 23802(52483)
90083(198633)
82585I(N18L2E1T0<52>
OUTLET<53>
0)
63151(139248)
3mm CS
NO SHELLD STIDUEB:E SIDE:
CS + NAASCMEE SECT
TUBES:
MAX. LENGTH:
CORROS
TUB
MATERI
ETSU:B
UCHLA
MULTITUBES NNE
INLET: ALLOWED:
6IN" LET:
12"
OUTLET: OUTLET:
3CmSm +NCASCE +NACE CS+NA
CHARAC T ER I S T IC S
INLET
OUTLET
INLET
OUTLET
MOLECULAR WEVIGAHPTOR
58.1
kDgE/NkSgImToYl(lAb T/lbOmPoEl)R. TVEISMCPO. SITY AT OPER.
29(.856 kg/m3 (lb/ft3) 504.0(0
STPHEECRIMFIACLHCEOANTD.
kCal/kg.
906.0(1
0.4305(0.4305)
60).0322(0.021
0.6798(0.6798)
kECNaTl/HmA.hLrP.oYC(BTU/ft.hr.oF)
405.2(1
0.0146(0.0098)
67).1313(28.29
Cli ent Sit e: Un it: D
[1] [1
1]
[1
PROC E S S DA TA
PROCESS SPECIFICATION HEAT EXCHANGER
GC28
ITEM NO.: 28-E-1505 -SPP
Rev. TYPE: 3
Pag
CPHale Waihona Puke Baidu
/S2E5R0V5ICE: HP
(AVER
0.00023 (10 TO
SPECIFIC GRAVITY LIQUID
6S0P/E6C0IFIC GRAVITY AT
OVPISECRO. STIETMYPA. T OPER.
TEMP.
STPHEECRIMFIACLHCEOANTD.
kCal/kg.
kECNaTl/HmA.hLrP.oYC(BTU/ft.hr.oF)
AKU TEMA
COMPRESS0R TRIM
AMGMEkCal
(
DOUPETRYA/TUINOINT: SUMMER
1.713 /hr
NO. OF 6.797
CFLAUSIED W: ITHOUTSHGEALSL
UNITS:
TWO
SIDE:
SHELL
TUBE
TOTAL FLOW RATE
S24ID08E4(53
MMkCal/hr (MMBTU/hr)
POUR POINT
cP (cP) oC (oF)
INLET 0.57 407.55 01.15 04.5(9 805.0(7 4- 3( 0.05
OUTLET
0.5761 0.5507 0.1493(0.1493) 0.5997(0.5997) 0-0.0.0704066(0(-.0501) 0.0024)
0.0314(0.0211)
1]
MLAMTkECNaTl/hHrE(MATMBTU/hr)
0(0.
1.8649(7.400)
7)
5.1698(20.5137)
MMkCal/hr (MMBTU/hr)
PA SHELL SIDE: TUBE SIDE:
SHE
LMLA:
XCO.
RMRA
TER
SHE
FLOATING
H20
kg/hr (lb/hr)
178(392)
63(139)
NONCONDENSABLES
LIQUID
HC
213 kg/hr (lb/hr) 68(
282(622)
7042(15528)
26478(58384)
H20
OPERATING TEMPERATURE ODPEESRIGANTITNEGMPPERREASSTURE oC (oF)
INLET
0.5273 0.40176824(0.078 40).7899(0.789 90).0628(0.042 20).0815(0.323 4)
OUTLET
0.4913 0.4256 0.0762(0.0762) 0.7632(0.7632) 0.067(0.045) 0.330(1.3095)
[3]
A4.SSOUUMREDSETROVIBCEE A(GAS
C5.ONATBAOINOST FHO2SR L( UMBAEXI.
O6.IOLPDERRAAITNIINNGG TO BE
[1]
FLOWRATE AND HEAT
CONSTRUCTION MCOANTSETRRIAULC:TION CODE:
DALELSOIGWNAPBRLEESSPURRESESURE DROP VFOAUCLUIUNMG FRAACTTINOGR m2.hr.0C/kCal(ft2.hr.0F/BT FLEXIBILITY
kg/hr (lb/hr) 35.3 (29.957.
kg/cm2 g (psig) (42.
kg/cm2 g (psig) kg/cm2 (psi)
kg/cm2 a (psia)
%
36(96.8) 100 2.97(42.23) ( 21213) .3 (188.6 ) NEGLIGI
0.0100023 TO
278(613)
391(862)
57.8(136)
40(107)
68.26(970.66) 180 67.75(963.41)
( 37566.5) (1008.75.18 (7.25 )
BDOTUTBOLME :PIPE
APRLOLOCWESESDL: INES
DIAMETER:
NO
[1] TE:
1. TRIM COOLER IS BY PACSOSNESDIDIENRWEDINCTAERSE.
W2. HTIWCHO OISUBTALSEETDS FOONR
V3.ARPOEFRR. IGERANT IS
58.12(58.12) 9.8131(0.6123)
29.29(29.29) 100.051.8559(60.60015)
27.16(27.16) 102.99(6.427)
TEMP.
cP (cP) 708.4(2
0.0078(0.0078)
90).6776(0.677
0.0153(0.0153)