Author:
Rezaee Parham,Naeij Hamid Reza
Abstract
AbstractIn order to separate a mixture of hydrogen ($$\text {H}_{2}$$
H
2
) and carbon dioxide ($$\text {CO}_{2}$$
CO
2
) gases, we have proposed a new approach employing the graphdiyne-like membrane (GDY-H) using density functional theory (DFT) calculations and molecular dynamics (MD) simulations. GDY-H is constructed by removing one-third diacetylenic ($${{-}\text {C}{\equiv}\text {C}{-}\text {C}{\equiv}\text {C}{-}}$$
-
C
≡
C
-
C
≡
C
-
) bonds linkages and replacing with hydrogen atoms in graphdiyne structure. Our DFT calculations exhibit poor selectivity and good permeances for $$\text {H}_{2}$$
H
2
/$$\text {CO}_{2}$$
CO
2
gases passing through this membrane. To improve the performance of the GDY-H membrane for $$\text {H}_{2}$$
H
2
/$$\text {CO}_{2}$$
CO
2
separation, we have placed two layers of GDY-H adjacent to each other which the distance between them is 2 nm. Then, we have inserted 1,3,5-triaminobenzene between two layers. In this approach, the selectivity of $$\text {H}_{2}$$
H
2
/$$\text {CO}_{2}$$
CO
2
is increased from 5.65 to completely purified $$\text {H}_{2}$$
H
2
gas at 300 K. Furthermore, GDY-H membrane represents excellent permeance, about $$10^8$$
10
8
gas permeation unit (GPU), for $$\text {H}_{2}$$
H
2
molecule at temperatures above 20 K. The $$\text {H}_{2}$$
H
2
permeance is much higher than the value of the usual industrial limits. Moreover, our proposed approach shows a good balance between the selectivity and permeance parameters for the gas separation which is an essential factor for $$\text {H}_{2}$$
H
2
purification and $$\text {CO}_{2}$$
CO
2
capture processes in the industry.
Publisher
Springer Science and Business Media LLC
Cited by
17 articles.
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