渗透
膜
膜反应器
化学
固定化酶
碳酸酐酶
化学工程
色谱法
热稳定性
纤维
丙烯酸
中空纤维膜
选择性
核化学
材料科学
聚合物
催化作用
酶
有机化学
共聚物
生物化学
渗透
工程类
作者
Yatao Zhang,Lin Zhang,Huan‐Lin Chen,Weian Zhang
标识
DOI:10.1016/j.ces.2010.02.010
摘要
This paper reported the results of developing a novel hollow fiber membrane reactor contained immobilized enzyme for selective separation of low concentration CO2 from mixed gas streams. In the reactor, two bundles of poly(vinylidene fluoride) (PVDF) hollow fiber membranes were aligned staggered parallel in a tube module, and lab-made poly(acrylic acid-co-acrylamide)/hydrotalcite (PAA-AAm/HT) nanocomposite hydrogel was filled between fibers, in which carbonic anhydrase (CA enzyme) was immobilized. The effects of CA concentration, buffer concentration, the flow rate of sweep gas, operational temperature, and CO2 concentration on separation performance were investigated in detail. The results showed that the transport resistance was mainly from the hydrogel layer, and decreased greatly with immobilization of carbonic anhydrase in hydrogel. Moreover, immobilized CA could retain over 76% enzymatic activity and thermal stability was also improved. The data showed that this enzyme-based membrane reactor could effectively separate CO2 at low concentration from mixed gas streams. For the feed with 0.1% (v/v) of CO2, the selectivity of CO2/N2 was 820, CO2/O2 was 330, and CO2 permeance was 1.65×10−8 mol/m2 s Pa. Prolonged runs lasting 30 h showed that separation performances of the membrane reactor were quite stable.
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