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V-101 Natural Gas Knock-Out Drum
1.22m D X 1.22m H
V-102 1st Stage Air Knock-Out Drum
2.74m D X 2.74m H
V-103 2nd Stage Air Knock-Out Drum
1.83m D X 1.83m H
V-104 3rd Stage Air Knock-Out Drum
2.13m D X 2.13m H
C-103 C-104 C-105 C-106
C-101 C-102
R-102880.3°C
R-103450.2°C
R-104159.1°C
CoolingWater
CoolingWater
CoolingWater
CoolingWater
CoolingWater
C-1011st Stage Natural Gas Compressor
Power = 2,070.82 kW
C-102 2nd Stage Natural Gas Compressor
Power = 2113.57 kW
C-1031st Stage Air Compressor
Power = 5,012.78 kW
C-104 2nd Stage Air Compressor
Power =5,893.63 kW
C-105 3rd Stage Air Compressor
Power = 5,554.90 kW
C-106 4th Stage Air Compressor
Power = 4,533.60 kW
E-101 Natural Gas Compressor Intercooler
Duty = 7.52 GJ/hr
E-102 1st Stage Air Compressor Intercooler
Duty = 15.12 GJ/hr
E-1032nd Stage Air Compressor Intercooler
Duty = 21.33 GJ/hr
E-104 3rd Stage Air Compressor Intercooler
Duty = 20.29 GJ/hr
E-105 Steam Generation Exchanger
Duty = 356.20 GJ/hr
E-106 Shift Reactors Intercooler
Duty = 238.45 GJ/hr
E-107 2nd Stage Air-Flue Gas Exchanger
Duty = 33.42 GJ/hr
E-108 Process Steam-Flue Gas Exchanger
Duty = 16.25 GJ/hr
E-109 2nd Stage Natural Gas-Flue Gas Exchanger
Duty =27.28 GJ/hr
E-110 1st Stage Air-Flue Gas Exchanger
Duty = 23.85 GJ/hr
E-111 1st Stage Natural Gas-Flue Gas Exchanger
Duty = 20.20 GJ/hr
E-112 Exiting Flue Gas Cooler
Duty = 39.98 GJ/hr
R-101 Primary Reformer1.76m D X 8m H
R-102 Secondary Reformer
3.15m D X 5m H
R-103 High Temperature Shift Reactor
4.89m D X 8m H
R-104 Low Temperature Shift Reactor
1.14m D X 3m H
R-106 Desulfurization Swing Reactor 1
4.35m D X 5m H
R-107 Desulfurization Swing Reactor 2
4.35m D X 5m H
R-106
R-107
S-1016
S-1017
S-1018 S-1020
S-1021
S-1022
S-1023 S-1024
S-1025
S-1026
S-1027 S-1028
S-1001
S-1002
S-1003
S-1004
S-1005
S-1006
S-1007
S-1008 S-1009
S-1029
S-1032
S-1033
S-1034 S-1035 S-1036 S-1037 S-1038
S-1047
S-1049
S-1050
S-1051
S-1052
S-1053
S-1054
S-1055
S-1061
S-1062
387.8°C 160.0°C
E-102 E-103V-102 V-104
E-101
E-104
V-101
V-103
R-101760.0°C
CoolingWater
S-1013
113.4°C34.0 atmS-1011
S-1012S-1010
426.7°C
S-1014
426.7°C
S-1039
S-1040
S-1015
S-1029
145.5°C34.0 atm
S-1030
S-1031
482.2°C
S-1059
S-1060
E-107
E-108
E-109
E-110
E-111
E-112
TIC
Natural Gas42°C
8 atm
Process Air26.7°C
1.0 atm
Process Steam373.3°C
40.8 atm BFW90.5°C
95.3 atm
Steam (Utilities)507.8°C
95.3 atm
To Section 2159.1°C
32.8 atm
Fuel Gas42.0°C
40.8 atm
Furnace Air26.7°C1atm
TIC TIC TIC
TICV-15
TIC
TIC
Flue Gas93.3°C
0.272 atm
S-1041
S-1019
S-1042
S-1043
S-1044
S-1045
S-1046
S-1048
S-1056
S-1057
S-1058
S-1063
E-106E-105
AMMONIA PROCESSING PLANT
FEED PREPARATION
REFORMING
SHIFT REACTION
PROCESS FLOW DIAGRAM
SECTION 1 – FEED PREP AND REFORMING
APPROVED BY: CRYSTAL LIN, PM
PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA
MY CHEMICAL ROMANCE SOLUTION INC.
LOS ANGELES, CALIFORNIA
SCALE PROJECT NUMBER DRAWING NUMBER REV
NONE 01-2012 108A-PANG-108B 7
DATE 06-06-2012 CLIENT – HP CHEMICAL SHEET 1 OF 1
