Process Air 26.7°C 1.0 atm
C-101 1st Stage Natural Gas Compressor Power = 2,070.82 kW
E-101 Natural Gas Compressor Intercooler Duty = 7.52 GJ/hr
E-105 Steam Generation Exchanger Duty = 356.20 GJ/hr
E-109 2nd Stage Natural Gas-Flue Gas Exchanger Duty =27.28 GJ/hr
V-101 Natural Gas Knock-Out Drum 1.22m D X 1.22m H
R-101 Primary Reformer 1.76m D X 8m H
C-102 2nd Stage Natural Gas Compressor Power = 2113.57 kW
E-102 1st Stage Air Compressor Intercooler Duty = 15.12 GJ/hr
E-106 Shift Reactors Intercooler Duty = 238.45 GJ/hr
E-110 1st Stage Air-Flue Gas Exchanger Duty = 23.85 GJ/hr
V-102 1st Stage Air Knock-Out Drum 2.74m D X 2.74m H
R-102 Secondary Reformer 3.15m D X 5m H
C-103 1st Stage Air Compressor Power = 5,012.78 kW
E-103 2nd Stage Air Compressor Intercooler Duty = 21.33 GJ/hr
E-107 2nd Stage Air-Flue Gas Exchanger Duty = 33.42 GJ/hr
E-111 1st Stage Natural Gas-Flue Gas Exchanger Duty = 20.20 GJ/hr
V-103 2nd Stage Air Knock-Out Drum 1.83m D X 1.83m H
R-103 High Temperature Shift Reactor 4.89m D X 8m H
C-104 2nd Stage Air Compressor Power =5,893.63 kW
E-104 3rd Stage Air Compressor Intercooler Duty = 20.29 GJ/hr
E-108 Process Steam-Flue Gas Exchanger Duty = 16.25 GJ/hr
E-112 Exiting Flue Gas Cooler Duty = 39.98 GJ/hr
V-104 3rd Stage Air Knock-Out Drum 2.13m D X 2.13m H
R-104 Low Temperature Shift Reactor 1.14m D X 3m H
C-105 3rd Stage Air Compressor Power = 5,554.90 kW
Cooling Water
C-106 4th Stage Air Compressor Power = 4,533.60 kW
Cooling Water
S-1046
Cooling Water
S-1049
S-1050
S-1047
TIC
TIC
S-1022
S-1019
C-103
S-1024
S-1023
E-102
S-1027
E-103
C-104
V-102
S-1048
S-1030
S-1026
S-1020
S-1028
E-104
C-105
V-103
S-1021
S-1006
S-1004
S-1029
S-1055
Flue Gas 93.3°C 0.272 atm
S-1002 TIC
R-106 S-1001
S-1003
E-101
C-101
V-101
S-1057
S-1007
S-1005
S-1012
S-1010
S-1009
TIC
E-112
113.4°C 34.0 atm
S-1011 S-1008
S-1045
Cooling Water
S-1059
S-1056
Natural Gas 42°C 8 atm
C-106
V-104
S-1054
S-1025 S-1051
Cooling Water
R-107 Desulfurization Swing Reactor 2 4.35m D X 5m H
S-1053
TIC
S-1018
R-106 Desulfurization Swing Reactor 1 4.35m D X 5m H
S-1052
S-1058 V-15
S-1060
E-111
C-102 S-1013
E-110
S-1031 145.5°C 34.0 atm
S-1029
E-109
R-107
S-1032
Process Steam 373.3°C 40.8 atm
E-108
S-1015
BFW 90.5°C 95.3 atm
S-1039
E-107 S-1014
Fuel Gas 42.0°C 40.8 atm
S-1016 426.7°C
S-1041 426.7°C
Furnace Air 26.7°C 1atm
S-1033 482.2°C
S-1043
Cooling Water
TIC
SECTION 1 – FEED PREP AND REFORMING APPROVED BY: CRYSTAL LIN, PM
S-1062 S-1042
PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA
AMMONIA PROCESSING PLANT FEED PREPARATION REFORMING SHIFT REACTION PROCESS FLOW DIAGRAM
R-101 760.0°C
E-105
S-1017
R-102 880.3°C
SCALE
PROJECT NUMBER
DRAWING NUMBER
REV
NONE
01-2012
108A-PANG-108B
7
DATE
06-06-2012 CLIENT – HP CHEMICAL
SHEET
1 OF 1
TIC
S-1044 S-1034
MY CHEMICAL ROMANCE SOLUTION INC. LOS ANGELES, CALIFORNIA
S-1061
S-1035 387.8°C
S-1036
E-106 R-103 450.2°C
S-1063
S-1040
S-1037 160.0°C
S-1038
To Section 2 159.1°C 32.8 atm
R-104 159.1°C Steam (Utilities) 507.8°C 95.3 atm
D 201 CO2 Absorption Column D=4.82 m, H=48.5m
D 202 CO2 Stripping Column
V201 H2O Removal Flash Drum D = 1.01 m , H= 3.02 m
V202 MDEA Stripper Condenser Accumulator
T 201 CO2 Stripper Feed Expander 13,386.25 kW
E 201 Second Stage Intercooler 7.27 GJ/hr
E 202 First Stage Intercooler 256.71 GJ/hr
E 203 CO2 Stripper Condenser 46.23 GJ/hr
E 204 CO2 Stripper High Pressure Reboiler 335.63 GJ/hr
E205 CO2 Stripper Low Pressure Reboiler 51.79 GJ/hr
Cooling Water S-2006
E 203
To Section 3 23.8°C 27.2 atm
LC S-2005
Recycled MDEA Solution 23.88 °C 1 atm
1
1 S-2010
V 202 2
2
97.11°C 27.7 atm S-2003
T 201
S-2008
Removed CO2 64.5 °C 2 atm
30
S-2009
TC 83.7 °C 2 atm
V 201
S-2014
82.2 °C 27.4 atm
49
49
LC
S-2002
E 202 50
50
LC
E 201
S-2012
S-2007
Cooling Water
LC
S-2004
LP STEAM
D 202 D 201
S-2013
E 204
S-2011
HP STEAM
P 201
TC
S-2001
TC
E 205
S-2000
From Shift Reaction 230.56 °C 31 atm
PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA AMMONIA PROCESSING PLANT CO2 REMOVAL PROCESS FLOW DIAGRAM
SECTION 2 – REMOVAL AND RECOVERY APPROVED BY: CRYSTAL LIN, PM
TC
MY CHEMICAL ROMANCE SOLUTION INC. LOS ANGELES, CALIFORNIA SCALE
PROJECT NUMBER
DRAWING NUMBER
REV
NONE
01-2012
108A-PANG-108B
3
DATE
06-06-2012
CLIENT – HP CHEMICAL
SHEET
1 OF 2
P201 MDEA Recycle Pump 1,637.46 kW
D 203 NH3 Absorption Column
D 204 NH3 Stripping Column
V203 NH3 Stripper Condenser Accumulator
E 206 Ammonia Recovery Fisrt Heat Exchanger 0.383 GJ/hr
E 203 NH3 Stripper Condenser 4.47 GJ/hr
E 204 NH3 Stripper Reboiler 7.22 GJ/hr
Cooling Water
E 207
S-2101
Waste Gas 112 °C 166 atm
LC S-2102
Recycled H2O 123 °C 166 atm
1
1 S-2105
V 203 2
2
80 °C 2 atm
4
2 °C 166 atm
Recovered NH3 98 °C 2 atm
S-2104 27°C 166 atm
TC
7
9
LC E 206 S-2100
10
8
LC
From Purge Stream 2 °C 166 atm
HP STEAM
D 204 D 203
S-2107
S-2103 S-2106
Cooling Water
S-2109 S-2108
P 202 E 208
TC PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA AMMONIA PROCESSING PLANT NH3 RECOVERY PROCESS FLOW DIAGRAM
SECTION 2 – REMOVAL AND RECOVERY APPROVED BY: CRYSTAL LIN, PM
MY CHEMICAL ROMANCE SOLUTION INC. LOS ANGELES, CALIFORNIA SCALE
PROJECT NUMBER
DRAWING NUMBER
REV
NONE
01-2012
108A-PANG-108B
3
DATE
06-06-2012
CLIENT – HP CHEMICAL
SHEET
2 OF 2
P201 H2O Recycle Pump 25.31 kW
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
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 S3018 -195.6 C 1 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
1 OF 1
Compressor ID C-4001 C-4002 C-4003 C-4004 Description 1st Compresser 2nd Comrpessor 3rd Compressor 4th Compressor for synthesis gas for synthesis gas for synthesis gas for synthesis gas KW 12845.81 12523.96 13001.23 8201.36
ID Description
Duty [GJ/hr] ID Description
Refrigerant NH3 Level 2
Refrigerant NH3 Level 1
Coolant water
Reactor ID R-4001 R-4002 Description First reactor for Second reactor for synthesis gas synthesis gas Height[m] 12 7 Diameter[m] 3.5 3.5
Duty [GJ/hr]
V-21
V-18
E-4001 E-4002 first Second Intercooler Intercooler C-4001 C-4001 16.0 6.6 E-4008 E4009 1st HX 2nd HX for mixed gas for mixed gas before 1st reactor after 1st reactor 170.938462 6.693264
LIC-4002
LIC-4001
S4004
From Section 3 S4002
S4003
E-4001
C-4001
Recycle HX
HX for Coolant water 224.73113
45.594416
Refrigerant NH3 Level 1
Coolant water
S4001
4.2C° 23.5atm
Steam heat Exchanger 70.708466
E-4005 Second Intercooler C-4002 5.3 E-4012
E-4006 Third Intercooler C-4002 5.3 E-4013 HX for Refrigerent Level 1 80.245074
Flash Drum V-4001 Flash Drum for Seperation
E-4007 HX for feed stream 223.1 E-4014 HX for Refrigerent Level 2 18.53569
V-16
FIC-4001
81.7C°, 45.5atm
Heat Exchanger E-4004 first Intercooler C-4002 14.5 E-4011
E-4003 Third Intercooler C-4001 2.6 E-4010
S4005
Refrigerant NH3 Level 2
-9.0°C, 4.0atm
23.8°C,1atm
-33.3°C,1atm
2°C, 166.1atm
2°C, 45.5atm
E-4002
E-4003
76.3°C, 86.1atm
FIC-4004 V-35
C-4002
S4024 67.2°C, 180.0atm S4023 2°C, 166.1atm V-33
V-32
V-31
FIC-4003
S4018 Refrigerant NH3 Level 1
Coolant water
S4021
S4020
S4019
191.2°C, 178.5atm
10.0°C,178.2atm
37.8°C,178.4atm
E-4013
E-4012
2°C,178.1atm
E-4014
V-4001
V-22
FIC-4002
S4022 LIC-4004
V-23
LIC-4003
V-34 2°C, 86.1atm
S4007
2°C,166.1atm 33.8°C,0.80atm
S4006
S4008
E-4004
LIC-4006
Refrigerant NH3 Level 2
E-4011 V-24
LIC-4005
-37.8°C,0.8atm
-2.3°C,3.8atm
E-4006
E-4005
C-4003
C-4004
S4009 FIC-4005 S4025
S4009
67.2°C, 180atm
287.7°C, 98.7atm
Ammonia Production V-30
I-31
S4015 476.7°C,178.9atm
385.0°C,179.6atm S4011 385°C,179.6atm
R-4001
310.3°C,98.3atm
S4012
S4014
531.7°C,179.4atm
418.3°C,178.8atm
E-4010
R-4002 287.7°C.98.7atm
S4017 271.1°C,178.6atm
E-4007 PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA
S4016
AMMONIA PROCESSING PLANT COMPRESSION AND SYNTHESIS PROCESS FLOW DIAGRAM
E-4009
421.6°C,179.2atm
MY CHEMICAL ROMANCE SOLUTIONS INC. LOS ANGELES, CALIFORNIA
S4013 S4010
E-4008 246.1°C,179.8atm
SECTION 4 – COMPRESSION & SYNTHESIS APPROVED BY: CRYSTAL LIN, PM
SCALE
PROJECT NUMBER
DRAWING NUMBER
REV
NONE
01-2012
108A-PANG-108B
5
DATE
06-09-2012 CLIENT – HP CHEMICAL
SHEET
1 OF 1
E-522 E-523 1st Recovery Reboiler 2nd Recovery Reboiler Duty: 247 kJ/hr Duty: 105 kJ/hr
E-521 Removal Reboiler Duty: 218 kJ/hr
E-524 Flue Gas Heater Duty: 525 kJ/hr
E-525 E-526 E-527 1st Synthesis Heater 2nd Synthesis Heater 3rd Synthesis Heater Duty: 45 kJ/hr Duty: 227 kJ/hr Duty: 58 kJ/hr
S-5202 T: 374 C P: 41 ATM
T-521
T-522
E-528 4th Synthesis Heater Duty: 44 kJ/hr
S-5204 T: 152 C P: 3.7 ATM
E-529 5th Synthesis Heater Duty: 171 kJ/hr
E-523
S-5201 T: 482 C P: 95 ATM T-528
T-523
T-529
T-524
S-5203 T: 374 C P: 41 ATM T-525 E-529
To Section 1 T-526 E-528
T-527 E-527
E-524
S-5206 T: 10 C P: 1 ATM
E-526
E-521
E-522 E-525
S-5205 T: 152 C P: 95 ATM
P-521 Steam System Pump Work: 1257 kW T-527 3 Syn Comp Turbine Work: 10 kW rd
PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA AMMONIA PROCESSING PLANT STEAM SYSTEM PROCESS FLOW DIAGRAM
SECTION 5 - UTILITIES 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
3 OF 3
T-521 st 1 Pre-Cryo Comp Turbine Work: 15853 kW
T-523 th 4 Syn Comp Turbine Work: 60 kW
T-522 2 Pre-Cryo Comp Turbine Work: 5132 kW
T-524 Recovery Pump Turbine Work: 25 kW
nd
T-525 st 1 Syn Comp Turbine Work: 9.21 kW
T-526 2 Syn Comp Turbine Work: 9.47 kW nd
P-521
T-528 Removal Pump Turbine Work: 1673 kW T-529 Steam System Pump Turbine Work: 1257 kW
C-501 Primary Compressor 8292 kW
C-502 Compressor 2 6432 kW
C-503 Compressor 3 234.5 kW
E-502 Interstage Cooler 1785 m2 11.4 GJ/hr
E-501 Condensor 144 GJ/hr
E-303a 9.5 GJ/hr
E-407 68.8 GJ/hr
E-409a 7.9 GJ/hr
E-503 Precooler 1011 m2 33.6 GJ/hr
E-410a 7.9 GJ/hr
S-5012
V-501 Primary Knockout Drum 1.2 m-D x 6.7 m-H
E-303b 3.8 GJ/hr
E-408 27.4 GJ/hr
V-502 Secondary Knockout Drum 0.6 m-D x 6.7 m-H
E-409b 3.9 GJ/hr
E-410b 4.0 GJ/hr
S-5010
8900 kg-mol/hr
6 atm 13.3 C
1727 kg-mol/hr
6 atm 35.6 C S-5016
2731 kg-mol/hr
Used Cold Water
6 atm 10 C
S-5025
S-5001
C-503
6 atm 10 C 17 atm 93.3 C
17 atm 65.5 C
41 atm 166 C
41 atm 87.8 C
S-5002
S-5003
S-5004
S-5005
40 atm 78.8 C
S-5006
6 atm 10 C
437 kg-mol/hr S-5021
C-502
E-303a
E-501
C-501
E-502
S-5007
E-503
3162 kg-mol/hr
V-501 E-407
TIC I-1 6169 kg-mol/hr
370 kg-mol/hr
E-409a
S-5013 Cold Water S-5015
6 atm 10 C
370 kg-mol/hr 3.4 atm -5.6 C
E-410a
108 kg-mol/hr
S-5011
168 kg-mol/hr 3.4 atm -5.6 C 1835 kg-mol/hr
E-303b
S-5008 1209 kg-mol/hr
E-408
V-502 174 kg-mol/hr 3.4 atm -5.6 C
E-409b S-5009 1727 kg-mol/hr
176 kg-mol/hr
PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA E-410b
AMMONIA PROCESSING PLANT REFRIGERATION SYSTEM PROCESS FLOW DIAGRAM
SECTION 5 - UTILITIES APPROVED BY: CRYSTAL LIN, PM
MY CHEMICAL ROMANCE SOLUTION INC. LOS ANGELES, CALIFORNIA SCALE
PROJECT NUMBER
DRAWING NUMBER
REV
NONE
01-2012
108A-PANG-108B
5
DATE
06-06-2012
CLIENT – HP CHEMICAL
SHEET
1 OF 3
W-511 Cooling Water Filter 20247 kg-mol/hr
E-511 Cooling Tower 90-W x 14.6-L x 10-H (m)
T-511 Chemical Additive Tank 3-D x 3-H (m)
E-101 15.1 GJ/hr
E-102 21.2 GJ/hr
E-103 20.2 GJ/hr
E-104 7.6 GJ/hr
E-204C 4.5 GJ/hr
E-203 0.4 GJ/hr
E-202C 280 GJ/hr
E-201 8.3 GJ/hr
E-106 240 GJ/hr
E-112 40 GJ/hr
E-409 24.5 GJ/hr
E-409a 14.4 GJ/hr
E-410a 13 GJ/hr
E-411 5.8 GJ/hr
E-406 224 GJ/hr
E-501 137 GJ/hr
E-302 10.4 GJ/hr
T-511 12053 kg-mol/hr
E-101 16996 kg-mol/hr Quality
E-102
I-1 16162 kg-mol/hr
E-103
S-5109 5990 kg-mol/hr S-5108
E-104 848927 kg-mol/hr 190011 kg-mol/hr
E-106
S-5111 31838 kg-mol/hr
273050 kg-mol/hr
E-112 S-5112
S-5105 S-5102
S-5103 S-5104
S-5101
20247 kg-mol/hr 1.5 atm 27 C
Makeup Water 20247 kg-mol/hr 1 atm 27 C
233941 kg-mol/hr
848927 kg-mol/hr 3.4 atm 27 C
1 atm 27 C
W-511
E-204c
S-5114
P-512
346 kg-mol/hr
S-5115
E-203 223453 kg-mol/hr
224321 kg-mol/hr
P-512 Cooling Water Pump 1050 kW 848927 kg-mol/hr
3554 kg-mol/hr
E-511
P-513
P-511 Cooling Tower Feed Pump 450 kW 848927 kg-mol/hr
P-513 Filtration Pump 7.5 kW 20247 kg-mol/hr
E-202c 19580 kg-mol/hr 6588 kg-mol/hr
E-409 E-201 11616 kg-mol/hr
S-5113
E-409a
8308 kg-mol/hr
10334 kg-mol/hr
109306 kg-mol/hr
AMMONIA PROCESSING PLANT COOLING WATER SYSTEM PROCESS FLOW DIAGRAM
4529 kg-mol/hr
E-501 E-411
MY CHEMICAL ROMANCE SOLUTION INC. LOS ANGELES, CALIFORNIA
178262 kg-mol/hr
E-406
APPROVED BY: CRYSTAL LIN, PM
848927 kg-mol/hr 1.5 atm 43.3 C
E-302 E-410a
PLANT LOCATION – REPUBLIC OF TATARSTAN, RUSSIA
SECTION 5 - UTILITIES
S-5107
SCALE
PROJECT NUMBER
DRAWING NUMBER
REV
NONE
01-2012
108A-PANG-108B
5
DATE
06-06-2012
CLIENT – HP CHEMICAL
SHEET
2 OF 3
848927 kg-mol/hr 1 atm 43.3 C
S-5106
P-511