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Dichloroethane Removal from Gas Streams by an Extractive Membrane Bioreactor

机译:萃取膜生物反应器从气流中去除二氯乙烷

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AbstractA novel extractive membrane bioreactor (EMB) system, in which a silicone rubber membrane separates a contaminated gas stream from an aerated biomedium, extracted and biodegraded 1,2‐dichloroethane (DCE) from a gaseous waste stream. Selective transfer of the organic compound takes place through the silicone membrane to the biomedium, where biodegradation occurs. At a gas flow rate of 770 mL min−1and an average DCE concentration of 0.65 mg L−1, the EMB, with 2.5 m2of membrane surface contained in a spirally wound module, degraded 91 of the DCE. A biofilm grew on the membrane surface and caused a 600 mbar pressure drop at steady state conditions. The chloride ions released by DCE mineralization were 99 of the stoichiometric amount, while 60 of the total amount of carbon crossing the membrane as DCE was bioconverted to CO2. The overall mass transfer coefficient across the membrane in the absence of microbial activity was (0.8‐1.3) × 10−6m s−1and was controlled by the liquid film resistance. Extensive biofilm growth significantly lowered the DCE flux. Comparison of the EMB to a direct bioscrubbing process showed that the EMB system has superior volumetri
机译:摘要一种新型的萃取膜生物反应器(EMB)系统,其中硅橡胶膜将受污染的气流与充气生物介质分离,从气态废物流中提取和生物降解1,2-二氯乙烷(DCE)。有机化合物的选择性转移通过硅胶膜转移到生物介质中,在那里发生生物降解。在气体流速为770 mL min−1,平均DCE浓度为0.65 mg L−1时,具有2.5 m2膜表面的EMB在螺旋缠绕模块中降解了91%的DCE。生物膜在膜表面生长,并在稳态条件下产生 600 mbar 的压降。DCE矿化释放的氯离子占化学计量量的99%,而DCE生物转化为CO2时穿过膜的碳总量的60%。在没有微生物活性的情况下,膜上的总传质系数为(0.8-1.3)×10−6m s−1,并受液膜阻力控制。广泛的生物膜生长显著降低了DCE通量。将 EMB 与直接生物洗涤工艺进行比较表明,EMB 系统具有优越的体积三

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