Investigation of cellulose acetate and ZIF-8 mixed matrix membrane for CO2 separation from model biogas

被引:9
|
作者
Tanvidkar, Priya [1 ]
Jonnalagedda, Aditya [1 ]
Kuncharam, Bhanu Vardhan Reddy [1 ]
机构
[1] Birla Inst Technol & Sci, Dept Chem Engn, Pilani 333031, Rajasthan, India
关键词
Cellulose acetate membrane; ZIF-8 mixed matrix membrane; MMMs for CO2 separation; METAL-ORGANIC FRAMEWORK; CO2/CH4; SEPARATION; NANOPARTICLES; PERMEABILITY; PERFORMANCE; POLYIMIDE; CO2/N-2;
D O I
10.1080/09593330.2023.2192366
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The separation of CO2 from the biogas mixtures (CH4/CO2) is essential for biogas upgradation. However, polymer membranes used for CO2 separation exhibit low permeability. Mixed Matrix Membranes (MMMs) incorporating inorganic filler in the polymer enhance CO2 separation. In this work, bio-degradable cellulose acetate (CA) based MMMs with varying filler weight percentages (2-20 wt.%) of ZIF-8 were studied for the separation of CO2 from a model biogas (CH4/CO2) mixture. The MMMs were characterized by analysis of TGA and DSC for thermal stability and FTIR for alteration or formation of any new functional group. FESEM was done to evaluate the dispersion and interaction of ZIF-8 in the CA polymer matrix. Considering the economic aspect, the fabricated MMMs were tested for gas separation performance at reasonably lower feed pressure (1.5, 2 bar). MMM with 5 and 10 wt.% of ZIF-8/ CA MMMs showed the best performance with CO2 permeability of 9.65 Barrer and 9.5 Barrer, approximately two folds as compared to pure CA, and CO2/CH4 selectivity was 10.37 and 15.3. The experimental results were compared with the predicted gas permeation results determined using MMM transport predictive models, and found that the permeabilities were higher than the model predictions.
引用
收藏
页码:2867 / 2878
页数:12
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