TY - JOUR
T1 - Ultrathin membrane with robust and superior CO2 permeance by precision control of multilayer structures
AU - Han, Hoseong
AU - Scofield, Joel M.P.
AU - Gurr, Paul A.
AU - Webley, Paul A.
AU - Qiao, Greg G.
N1 - Funding Information:
We thank Billy Murdoch at RMIT University's Microscopy and Microanalysis Facility (RMMF) for the XPS measurement.
Publisher Copyright:
© 2023
PY - 2023/4/15
Y1 - 2023/4/15
N2 - Reducing CO2 emissions in the atmosphere is an urgent task to resolve serious environmental issues including global warming. Polymer-based ultrathin film composite (UTFC) membranes are an attractive strategy compared with other CO2 separation technologies due to their lower environmental impacts, higher cost-efficiency, and ease of scale-up. However, improving the gas separation performance with a simplified fabrication process is still needed for practical uses. The key to designing a high-performing gas separation composite membrane is the development of a highly gas-permeable gutter layer and ultrathin high-selective top layer. While the top layers in nanoscale thicknesses have been recently developed, achieving high gas permeance is still challenging due to the existing less controlled gutter layer. Gutter layers afford a uniform and highly permeable base to which an ultrathin selective layer can be coated, minimising the gas permeance loss while maintaining the gas selectivity. Polydimethylsiloxane (PDMS) is a common and widely used material for gutter layers due to its inherent high gas permeability. However, the CO2 permeance of these films is limited to between 1,500 and 5,000 GPU as the current uncontrollable fabrication methods tend to produce thicker layers. Here we report a new fabrication method with precise thickness control, which results in ultrathin gutter layers showing consistent CO2 permeance with 13,920 ± 1,770 GPU without any reduction in CO2/N2 selectivity. When this gutter layer was coated with a selective layer of PolyActive™ (PA), the resultant PAN/PDMS/PA composite membranes outperformed previously reported UTFC membranes with a CO2 permeance of 3,555 GPU and CO2/N2 selectivity of 40.
AB - Reducing CO2 emissions in the atmosphere is an urgent task to resolve serious environmental issues including global warming. Polymer-based ultrathin film composite (UTFC) membranes are an attractive strategy compared with other CO2 separation technologies due to their lower environmental impacts, higher cost-efficiency, and ease of scale-up. However, improving the gas separation performance with a simplified fabrication process is still needed for practical uses. The key to designing a high-performing gas separation composite membrane is the development of a highly gas-permeable gutter layer and ultrathin high-selective top layer. While the top layers in nanoscale thicknesses have been recently developed, achieving high gas permeance is still challenging due to the existing less controlled gutter layer. Gutter layers afford a uniform and highly permeable base to which an ultrathin selective layer can be coated, minimising the gas permeance loss while maintaining the gas selectivity. Polydimethylsiloxane (PDMS) is a common and widely used material for gutter layers due to its inherent high gas permeability. However, the CO2 permeance of these films is limited to between 1,500 and 5,000 GPU as the current uncontrollable fabrication methods tend to produce thicker layers. Here we report a new fabrication method with precise thickness control, which results in ultrathin gutter layers showing consistent CO2 permeance with 13,920 ± 1,770 GPU without any reduction in CO2/N2 selectivity. When this gutter layer was coated with a selective layer of PolyActive™ (PA), the resultant PAN/PDMS/PA composite membranes outperformed previously reported UTFC membranes with a CO2 permeance of 3,555 GPU and CO2/N2 selectivity of 40.
KW - CO/N separation
KW - crosslinked PDMS
KW - PolyActive
KW - post-combustion CO capture
KW - ultrathin film composite membranes
UR - http://www.scopus.com/inward/record.url?scp=85149283003&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2023.142087
DO - 10.1016/j.cej.2023.142087
M3 - Article
AN - SCOPUS:85149283003
SN - 1385-8947
VL - 462
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 142087
ER -