渗透汽化
聚二甲基硅氧烷
乙醇
发酵
膜
化学
渗透
乙醇发酵
色谱法
膜技术
化学工程
乙醇燃料
制浆造纸工业
食品科学
有机化学
生物化学
工程类
作者
Chaohui Fu,Di Cai,Song Hu,Qi Miao,Yong Wang,Peiyong Qin,Zheng Wang,Tianwei Tan
标识
DOI:10.1016/j.biortech.2015.09.117
摘要
The polydimethylsiloxane (PDMS) membrane, prepared in water phase, was investigated in separation ethanol from model ethanol/water mixture and fermentation-pervaporation integrated process. Results showed that the PDMS membrane could effectively separate ethanol from model solution. When integrated with batch ethanol fermentation, the ethanol productivity was enhanced compared with conventional process. Fed-batch and continuous ethanol fermentation with pervaporation were also performed and studied. 396.2-663.7g/m(2)h and 332.4-548.1g/m(2)h of total flux with separation factor of 8.6-11.7 and 8-11.6, were generated in the fed-batch and continuous fermentation with pervaporation scenario, respectively. At the same time, high titre ethanol production of ∼417.2g/L and ∼446.3g/L were also achieved on the permeate side of membrane in the two scenarios, respectively. The integrated process was environmental friendly and energy saving, and has a promising perspective in long-terms operation.
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