Toluene/water separation using MCM-41/PEBA mixed matrix membrane via pervaporation process

被引:16
作者
Rohani, Ramezan [1 ]
Pakizeh, Majid [2 ]
Chenar, Mahdi Pourafshari [1 ]
机构
[1] Ferdowsi Univ Mashhad, Dept Chem Engn Fac Engn, POB 9177948974, Mashhad, Razavi Khorasan, Iran
[2] Hamedan Univ Technol, Dept Chem Engn, POB 6516913733, Hamadan, Hamadan, Iran
基金
美国国家科学基金会;
关键词
Pervaporation; PEBA-2533; MCM-41; Mixed matrix membrane; Toluene; FUNCTIONALIZED MCM-41; AQUEOUS-SOLUTIONS; COMPOSITE MEMBRANES; PEBA MEMBRANE; N-BUTANOL; ADSORPTION; REMOVAL; SILICA; WATER; PERFORMANCE;
D O I
10.1016/j.memsci.2022.120988
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pervaporation (PV) process with the mixed matrix membrane (MMM) is a feasible and cost-effective alternative to conventional volatile organic compounds (VOC) removal methods. In this study, the mesoporous silicate MCM-41 was synthesized by a new and rapid sol-gel method and incorporated into the polyether-block-amide (PEBA-2533) polymer network. Prepared MMM and MCM-41 were characterized by XRD, FESEM, TEM, AFM, TGA, DSC, FTIR, contact angle, and mechanical analyses. Effect of MCM-41 calcination on the performance of MMM for toluene/water solution separation was studied using a PV setup. Experiments were conducted to determine the effects of MCM-41 loading, feed concentration, and feed temperature on total flux, component flux, separation factor, and pervaporation separation index (PSI). For a 300 ppm toluene aqueous solution at 30 degrees C, the separation factor, from 44.4 to 203.7 (358.7% increment), and toluene flux, from 3.9 to 10.5 g m(-2) h(-1) (163.8% increment), were improved by using 7.5% uncalcined MCM-41 loading. The PSI value of this sample was attained at 67290 g m(-2) h(-1), which was 412% higher than that of a neat PEBA membrane (13142 g m(-2) h(-1)).
引用
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页数:14
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