Network Structure Engineering of Organosilica Membranes for Enhanced CO2 Capture Performance

被引:2
|
作者
Jiang, Qiwei [1 ]
Guo, Meng [2 ]
机构
[1] Wuxi Ginkgo Plast Ind Co Ltd, Wuxi 214216, Jiangsu, Peoples R China
[2] Changzhou Univ, Sch Petrochem Engn, Jiangsu Key Lab Adv Catalyt Mat & Technol, Changzhou 213164, Jiangsu, Peoples R China
关键词
organosilica membranes; CO2; capture; calcination temperatures; pore size tailoring; CARBON-DIOXIDE SEPARATION; COMPOSITE MEMBRANES; RECENT PROGRESS; GAS-PERMEATION; ETHYLENE; ETHANE; MICROSTRUCTURE; FABRICATION; TRANSPORT;
D O I
10.3390/membranes12050470
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The membrane separation process for targeted CO2 capture application has attracted much attention due to the significant advantages of saving energy and reducing consumption. High-performance separation membranes are a key factor in the membrane separation system. In the present study, we conducted a detailed examination of the effect of calcination temperatures on the network structures of organosilica membranes. Bis(triethoxysilyl)acetylene (BTESA) was selected as a precursor for membrane fabrication via the sol-gel strategy. Calcination temperatures affected the silanol density and the membrane pore size, which was evidenced by the characterization of FT-IR, TG, N-2 sorption, and molecular size dependent gas permeance. BTESA membrane fabricated at 500 degrees C showed a loose structure attributed to the decomposed acetylene bridges and featured an ultrahigh CO2 permeance around 15,531 GPU, but low CO2/N-2 selectivity of 3.8. BTESA membrane calcined at 100 degrees C exhibited satisfactory CO2 permeance of 3434 GPU and the CO2/N-2 selectivity of 22, displaying great potential for practical CO2 capture application.
引用
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页数:11
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