Section 1 PFD

Page 1

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

C-101 S-1007

S-1005

S-1012

S-1010

S-1009

TIC

E-101 V-101

S-1057

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

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 Process Steam 373.3°C 40.8 atm

S-1032

E-108

S-1015

S-1014

Fuel Gas 42.0°C 40.8 atm

S-1041

Furnace Air 26.7°C 1atm

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

BFW 90.5°C 95.3 atm

S-1039

E-107 S-1016 426.7°C

426.7°C

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




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