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
2
V 202
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-2007
Cooling Water
LC
S-2004
D 202
D 201
S-2012
LP STEAM
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