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
2
V 203
2
80 °C 2 atm
4
2 °C 166 atm
Recovered NH3 98 °C 2 atm
S-2104 27°C 166 atm
TC
9
7
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