TY - JOUR
T1 - Effect of Light Gas Components on CO2Permeation through DD3R Membranes
AU - Song, Jieyu
AU - Peng, Xingyu
AU - You, Lekai
AU - Du, Peng
AU - Zhou, Tao
AU - Jin, Xiang
AU - Gao, Xuechao
AU - Wang, Xuerui
AU - Gu, Xuehong
N1 - Publisher Copyright:
© 2022 American Chemical Society. All rights reserved.
PY - 2022/12/14
Y1 - 2022/12/14
N2 - Membrane technology has emerged to be a promising alternative for natural gas upgrading. Zeolite membranes are attracting more and more attention because of the hydrothermal and chemical stability. However, the zeolite membranes are generally evaluated in the unary or binary CO2/CH4components, which is far from the real applications. Herein we investigated the CO2permeation through DD3R zeolite membranes under the presence of light gas components (e.g., N2, CH4, C2H6, and SF6). The CO2diffusivity was calculated by the generalized Maxwell-Stefan model for more insights on CO2transport. The diffusion of CO2molecules was slightly affected by the presence of N2, CH4, and SF6. However, the CO2diffusivity in equimolar CO2/C2H6was one magnitude lower than that of pure CO2component because of the strong competitive adsorption and slow diffusion of C2H6molecules. An empirical formula was proposed to predict the CO2diffusivity in the CO2/CH4/C2H6ternary mixture. The predicted CO2flux matched well with the experimental one for the mixture containing less than 15 mol % C2H6. This would provide a facile method to determine the required membrane area for multicomponent mixture separation.
AB - Membrane technology has emerged to be a promising alternative for natural gas upgrading. Zeolite membranes are attracting more and more attention because of the hydrothermal and chemical stability. However, the zeolite membranes are generally evaluated in the unary or binary CO2/CH4components, which is far from the real applications. Herein we investigated the CO2permeation through DD3R zeolite membranes under the presence of light gas components (e.g., N2, CH4, C2H6, and SF6). The CO2diffusivity was calculated by the generalized Maxwell-Stefan model for more insights on CO2transport. The diffusion of CO2molecules was slightly affected by the presence of N2, CH4, and SF6. However, the CO2diffusivity in equimolar CO2/C2H6was one magnitude lower than that of pure CO2component because of the strong competitive adsorption and slow diffusion of C2H6molecules. An empirical formula was proposed to predict the CO2diffusivity in the CO2/CH4/C2H6ternary mixture. The predicted CO2flux matched well with the experimental one for the mixture containing less than 15 mol % C2H6. This would provide a facile method to determine the required membrane area for multicomponent mixture separation.
UR - http://www.scopus.com/inward/record.url?scp=85143523851&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.2c03474
DO - 10.1021/acs.iecr.2c03474
M3 - 文章
AN - SCOPUS:85143523851
SN - 0888-5885
VL - 61
SP - 18100
EP - 18108
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 49
ER -