D 203D 204

E 206

P 202

S-2100

From Purge Stream2 °C

166 atm

Cooling Water

S-2101

Waste Gas112 °C

166 atmS-2102

Recycled H2O123 °C

166 atm

S-2103

S-210427°C

166 atm

S-2105

S-2106

1

10

1

8

4

9

2

7

2

LC

HP STEAM

Cooling Water

LC

TC

TC

E 207

Recovered NH398 °C2 atm

80 °C2 atm

2 °C166 atm

LC

V 203

D 203NH3 Absorption

Column

D 204NH3 Stripping

Column

V203NH3 Stripper

Condenser Accumulator

E 206Ammonia Recovery Fisrt Heat Exchanger

0.383 GJ/hr

E 203NH3 Stripper Condenser

4.47 GJ/hr

E 204NH3 Stripper

Reboiler7.22 GJ/hr

P201H2O Recycle

Pump25.31 kW

E 208

S-2107

S-2108S-2109

AMMONIA PROCESSING PLANT

NH3 RECOVERY

PROCESS FLOW DIAGRAM

SECTION 2 – REMOVAL AND RECOVERY

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 3

DATE 06-06-2012 CLIENT – HP CHEMICAL SHEET 2 OF 2