V302-1 Molecular Sieve Dryer No.1
R301 V301 MethanatIon Water Reactor Knockout Drum
V302-2 Molecular Sieve Dryer No.2
V303 D301 Distillation Column Cryogenic Distillation Condensate Tank Column
E301 Methanator Pre-heat Exchanger Duty= 99.7 GJ/hr
E303 MethanatIon Effluent 1st Level Refrigerant Cooler Duty= 9.56 GJ/hr
E302 Methanation Effluent Water Cooler Duty= 9.84 GJ/hr
E304 MethanatIon Effluent 2nd Level Refrigerant Cooler Duty=3.71 GJ/hr
E305 First Cold Box Heat Exchanger Duty= 0.26 GJ/hr
E306 Second Cold Box Heat Exchanger Duty= 73.3 GJ/hr
E307 Cryogenic Distillation Condenser Duty=9.15 GJ/hr
E308 Methanator Effluent Air Cooler Duty= 15.5 GJ/hr
S3002 315.6 C 26.9 atm
PIC
R301
S3003 352.2 C 25.8 atm
S3001 65.6 C 27 atm
Process Stream
V302-1 E301 S3004 102.4 C 25.6 atm
S3005 37.8 C 25.4 atm
E302
E308
S3006 E304
TIC
TIC
Air 19.0 C 1 atm
15.0 C 25.2 atm
E303
1st Level Liq. NH3 10.0 C 6.1 atm
Water 20 C 1 atm
S3007
S3008
5.5 C 25.1 atm
5.5 C 25.1 atm V301
TIC
V302-2 2nd Level Liq. NH3 -4.0 C 4.1 atm
H2O S3011 6.0 C 24.1 atm
E307 LIC
S3015 -181.6 C 23.3 atm
S3029 3.7 C 23.3 atm
N2,H2, Argon
H2, N2, Argon
Syngas To Compressor
V303
Waste Gas
S3024
N2, Argon, CH4
E306
E305
CH4, H2, N2, Argon
3.7 C 1.1 atm
S3014 -173.3 C 23.4 atm P301
D301
S3018 -195.6 C 1 atm
S3020 -182.1 C 1.1 atm
PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA AMMONIA PROCESSING PLANT CRYOGENIC PURIFICATION PROCESS FLOW DIAGRAM
S3016 -174.7 C 23.5 atm
P301 Bottoms Pump Power= 664.5 kW
SECTION 3 – CRYOGENIC PURIFICATION APPROVED BY: CRYSTAL LIN, PM
MY CHEMICAL ROMANCE SOLUTIONS INC. LOS ANGELES, CALIFORNIA SCALE
PROJECT NUMBER
DRAWING NUMBER
REV
NONE
01-2012
108A-PANG-108B
6
DATE
06-09-2012 CLIENT – HP CHEMICAL
SHEET
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