Modeling of Hydrogen Production Plant Using Aspen Hysys
1
Wed Jan 25 17:31:36 2017 Case: D:\6543 H2O2\Final Hydrogen Model\6543_H2Sim_Rev.19 (1400withWaterSaturation 5-DEC-2017).hsc Flowsheet: Case (Main) HYDROGEN RECYCLE MIX-100 NG + H2 C-101 A E-102 E-102 R-110 A/N TO R-103- TO E-103 S.S FROM E-103 S.S TO E-102 TS TO E-107 TS E-107 TO E-108 TS E-108 TO E-107 S.S MIX-101 E-111 INLET PSA UNIT TO H2 HANDLING B-101 INLET FLUE GASES PRE HEATED AIR E-111 FLUE GASES TO E-113 E-113 B FROM V-103 FLUE GASES TO E-115 E 113B TS Out E-115 IN E-106 TO E-106 TS TO TEE_107 MAKE-UP BFW TO V-105 TOP SIDE FCV-1 LCV-1 TEE-103 TO E-103 TS TCV-1 TO TCV-1 TO SHIFT CONVERTOR R-103 TO H2 SPLITTER H2 FOR HYDROTREATING CWR C-101 A/B Q R-103 T R-110 A/N T TO R-106 A/B DRAIN HC FEED GAS TO V-203 C-101 B Intercooler To Intercooler To Second Stage C-101 B Q Intercooler Q FROM TCV-1 TO E-111 INLET RECYCLE RCY-2 R B-101 RECYCLE TO PSA UNIT TO E-111 MIX-102 TO E-107 SHELL RCY-3 R E-107 S.S RECYCLE P-104 A/B Q E-106 S.S P-104 A/B TO P-104 AB V-203 PROCESS STEAM RCY-4 R AIR TO E-115 E-103 MIX-103 TEE-101 MIX-104 B-101 IN BURNER (B-101) C B-101 DRAIN H-101 (RAD) FLUE GASES TO E-111 REACTOR DUTY V-103B DUMMY P.D E-107 (S.S) ADJ-3 A MIX-105 TEE-105 TO E-102 (S.S) E-102 BY-PASS FROM E-102 (S.S) TCV-2 FROM E-102 BY-PASS PCV-3 TO HC / STEAM MIX FLUE GASES (DUMMY) TO R-110 A/N (DUMMY) PRE HEATED AIR (DUMMY) B-101 RECYCLE (DUMMY) E-111 INLET (DUMMY) FROM V-1403 (DUMMY) SET-3 S V-107 R-110 A/N Outlet E-111 Outlet Outlet R-106 A/B BED-2 R-106 A/B BED-1 C TO BED-2 BED-1 DRAIN H2S TO HEAT LOSS R-106 A/B OUT PIPE HEAT LOSS ADJ-6 A DEMIN BFW HC FUEL GAS FROM E-108 (T.S) E STEAM V-105 Tower Vap to Column From Column V-105 Drum RCY-5 R To Separator VENT STEAM L.P STEAM- TO P-104 AB Phase Comp Mass Flow (Overall-CO2) 0.0000 kg/h HC FEED GAS SATURATOR HC FEED (SAT) WATER IN HC FUEL GAS SATURATOR HC FUEL (SAT) WATER INLET AIR SATURATOR AIR (SAT) WATER INLE ADJ-4 A C-112 A/B FD FCV-1 IN C-112 A/B Q C-111 A/B ID C-111 A/B Q TO C-111 A/B FLUE GAS OUT TEE-107 BFW TO TCV 220 TCV 220 TO RECYCLE RCY-6 R TO V- 105 CWS HC FUEL GAS (DUMMY) TEE-104 SET-1 S SET-2 S CRV-100 C 2 3 TO E-103 TEE-108 E-113A To E113A TO E113A TS TEE-109 E 113 A TS Out To E113 B TS MIX-107 To Steam Drum VLV-100 BFW Dummy V-100 5AA 6AA 6A RCY-8 R 5A RCY-9 R ADJ-1 A
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Transcript of Modeling of Hydrogen Production Plant Using Aspen Hysys
Wed Jan 25 17:31:36 2017 Case: D:\6543 H2O2\Final Hydrogen Model\6543_H2Sim_Rev.19 (1400withWaterSaturation 5-DEC-2017).hsc Flowsheet: Case (Main)
HYDROGENRECYCLE
MIX-100 NG+H2
C-101A
TOE-102
E-102
TOR-110A/N
TOR-103-
TOE-103S.S
FROME-103S.S
TOE-102TS
TOE-107TS
E-107
TOE-108TS
E-108
TOE-107S.S
MIX-101
E-111INLET
PSAUNIT
TO H2HANDLING
B-101INLET
FLUEGASES
PREHEATEDAIR
E-111
FLUEGASESTOE-113
E-113B
FROMV-103
FLUEGASESTOE-115
E113BTSOut
E-115AIRIN
E-106
TOE-106TS
TOTEE_107
MAKE-UPBFW
TOV-105TOPSIDE
FCV-1
LCV-1
TEE-103
TOE-103TS
TCV-1TOTCV-1
TO SHIFTCONVERTORR-103
TO H2SPLITTER
H2 FORHYDROTREATING
CWR
C-101A/B Q
R-103
TR-110A/N
T
TOR-106A/B
DRAIN
HCFEEDGAS
TOV-203
C-101B
IntercoolerToIntercooler
ToSecondStage
C-101B Q
IntercoolerQ
FROMTCV-1
TO E-111INLETRECYCLE
RCY-2
R
B-101RECYCLE
TOPSAUNIT
TOE-111
MIX-102
TOE-107SHELL
RCY-3
R
E-107 S.SRECYCLE
P-104A/B Q
TOE-106S.S
P-104A/BTO
P-104AB
V-203
V-103B
PROCESSSTEAM
RCY-4
R
AIRTOE-115
E-103
MIX-103
TEE-101
MIX-104
B-101IN
BURNER(B-101)
C
B-101DRAIN
H-101(RAD)
FLUEGASESTOE-111
REACTORDUTY
V-103BDUMMY
P.DE-107(S.S)
ADJ-3
AMIX-105TEE-105
TOE-102(S.S)
E-102BY-PASS
FROME-102(S.S)
TCV-2FROME-102BY-PASS
PCV-3
TO HC/STEAM MIX
H-101(DUMMY)
FLUEGASES(DUMMY)
TO R-110A/N(DUMMY)
PREHEATEDAIR(DUMMY) B-101
RECYCLE(DUMMY)
E-111INLET(DUMMY)
FROMV-1403(DUMMY)
SET-3
S
V-107
R-110A/NOutlet
E-111Outlet
E-113Outlet
R-106A/BBED-2
R-106A/BBED-1C
TOBED-2
BED-1DRAIN
H2S
TOHEATLOSS
R-106A/B OUTPIPE
HEATLOSS
ADJ-6
A
DEMINBFW
HCFUELGAS
FROME-108(T.S)
ESTEAM
V-105Tower
Vap toColumn
FromColumn
V-105Drum
RCY-5
RToSeparator
VENTSTEAM
L.PSTEAM-
TO P-104 ABPhase Comp Mass Flow (Overall-CO2) 0.0000 kg/h
HC FEEDGASSATURATOR
HCFEED(SAT)
WATERIN
HC FUELGASSATURATOR
HCFUEL(SAT)
WATERINLET
AIRSATURATOR
AIR(SAT)
WATERINLE
ADJ-4
A
C-112A/BFD
FCV-1IN
C-112A/B Q
C-111A/BID
C-111A/B Q
TOC-111A/B
FLUEGASOUT
TEE-107
BFW
TOTCV220
TCV220
TORECYCLE
RCY-6
R
TOV-105
CWS
HC FUELGAS(DUMMY)
TEE-104
SET-1
S
SET-2
S
1CRV-100
C
2
3
TOE-103
TEE-108
E-113A
ToE113A
TOE113ATS
TEE-109
E113ATSOut
ToE113B TSMIX-107
ToSteamDrum
VLV-100BFWDummy
V-100
5AA
6AA
6A
RCY-8
R
5A
RCY-9
R
4
ADJ-1
A
Yousaf.Muhammad1
Callout
MODEL OF HYDROGEN PLANT Complete Modeling Of Hydrogen Production Plant. Complete reactions Modeling at various reactors including Equilibrium & conversion reactions. Model was developed to Develop H & MB For Complete Plant. Two major findings were explored from this modeling. One regarding Duty of Compressor & Other in Take of Excess air which was the waste of energy. Model was developed to consider the behavior of plant on various production rates. & changed composition of Fuel gas.
