Environmental Engineering Reference
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10% CO 2
90% N 2
5 atm
Permeate
1 atm
Figure 7.3.1 Single-stage membrane for carbon capture
Table 7.3.1 Typical conditions for a membrane separation of fl ue gas
p F
5 atm
p p
1 atm
500 m 3 /s
Φ F
x CO 2 , F
0.1
P CO 2
1,000 gpu
p F — pressure of the flue gas, p P — pressure of the permeate, P
CO 2 — permeance of the mem-
brane where gpu = (10 6 cm 3 (STP)/cm 2 sec cm-Hg), x CO 2 , F — flue gas composition, and Φ F
emissions of flue gas.
membrane independently. For example, we can increase the selectivity
of our membrane by decreasing the N 2 permeability of our membrane
while keeping the permeability of CO 2 fi xed.
As we saw in the previous section, the values in Table 7.3.1 together
with the selectivity fully specify our membrane and we can use the
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