Page 157 - Chemical engineering design

136 CHEMICAL ENGINEERING

9316 no.
C & R Construction Inc per 60 acid t/y 100,000 Client BOP Chemicals SLIGO Sheet Trace 2554.6 2146.0 Date by 25/7/1980 Checked
cent

Water 13 Product acid Nitric Trace Trace Trace Trace 1704.0 1136.0 4700.6 Dwg 1 43

11 Absorber Mixer Product 1
12 13 12 Absorber acid Trace Trace Trace 1376.9 2840.0 40

Tail gas 10 9 11 Water feed (Trace) (1) 26.3 1376.9 8 25 4.2)

10 Tail(2) gas 371.5 10,014.7 21.9 967.2 29.4 10,434.4 1 25
1 7
8 6 (Example

To sheet no 9317 Cooler Condenser 9 Absorber feed 683.9 10,014.7 202.5 11,897.7 8 40 process

Steam 5 Filter 8 Secondary air 408.7 1346.1 967.2 850.6 1010.1 29.4 1754.8 8 40 acid nitric example

W. H. B. 7 Condenser acid Trace Trace 1860.7 1 40 simplified See

Condenser 275.2 8668.8 202.5 Nil 1161.0 10,143.1 8 40 (1)
6 gas (?) (1)
4
3
Reactor (Oxidiser) 5 W.H.B. outlet (935.7) (1) 8668.8 (1238.4) (1) Trace Nil 1161.0 12,003.9 8 234 Flow-sheet:

Oxidiser 4 outlet Nil 935.7 8668.8 1238.4 12,003.9 8 907 4.2.
2A
1A Figure
Compressor 1
2 Vaporiser 3 Oxidiser feed 731.0 2628.2 8644.7 12,003.9 8 204

Filter 2A Oxidiser air 2628.2 8644.7 Trace 11,272.9 8 230

Ammonia 14 From sheet no 9315 2 Filtered air 3036.9 9990.8 13,027.7 1 15

Air

nominal 1A Ammonia vapour 731.0 731.0 8 20

Pressures 1 Ammonia feed 731.0 731.0 8 15

kg/h no. Component bar ° C
Flows Line Stream NH 3 O 2 N 2 NO NO 2 HNO 3 H 2 O Total Press Temp.