Page 172 - Gas Purification 5E

A41konolamiiies for Hydrogen Surfde and Carbon Dioxide Removal 159

250 GPM
A

+ 250 GPM
EDUCTOR
AMINE
SElTLER
I

4
85 GPM
120psi AP

COz = 3.2 mols/hr.
4

REGEN.
15 GPM

0 00

SOUR SWEET RICH LEAN RICH SEMI LEA^
H.C. H.C. MEAT0 MEAFRON MEA MEA
PRODUCT PRODUCl REGEN. REGEN. RECIRC. RECIRC
HYDROCARBON, MoVhr. 1406.11 1406.11
COZ 3.10 NIL 4.026 0.926 22.814 23.740
H2O 353.889 353.889 2005.371 2359.260
MEA 18.515 18.515 104.918 123.433
TOTAL, MoVhr. 1409.21 1406.11 376.430 373.330 2133.103 2506.433
LBS. PER HR. 60472 60336 7678 7542 43511 51053
MW 42.91 42.91 20.40 20.20 20.40 20.37
SP. GR. 0.483 0.483 1.006 1.006 1.006 1.006
GPM 250 250 15 15 85 100
PRESSURE, PSIA 445 44.5 565 565 565
TEMP., "F 55 55 90 55 60

Figure 2-97. Single-stage liquid hydrocarbon COP removal system with material
balance. (Bacon, 7972)