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Evaluation of hydrophobic micro-zeolite-mixed matrix membrane and integrated with acetone-butanol-ethanol fermentation for enhanced butanol production

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    • 바이오플라스틱
      1. 플라스틱
    • 바이오정밀화학
      1. 용매
      2. 화학제품
      3. 연료
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      1. 계면활성제⁄증점제
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      1. 치료제
      2. 식품첨가제
논문

Evaluation of hydrophobic micro-zeolite-mixed matrix membrane and integrated with acetone-butanol-ethanol fermentation for enhanced butanol production

학술지

Biotechnology for biofuels

저자명

Xue, Chuang; Yang, Decai; Du, Guangqing; Chen, Lijie; Ren, Jiangang; Bai, Fengwu

초록

<P><B>Background</B></P><P>Butanol is regarded as an advanced biofuel that can be derived from renewable biomass. However, the main challenge for microbial butanol production is low butanol titer, yield and productivity, leading to intensive energy consumption in product recovery. Various alternative separation technologies such as extraction, adsorption and gas stripping, etc., could be integrated with acetone&#x2013;butanol&#x2013;ethanol (ABE) fermentation with improving butanol productivity, but their butanol selectivities are not satisfactory. The membrane-based pervaporation technology is recently attracting increasing attention since it has potentially desirable butanol selectivity.</P><P><B>Results</B></P><P>The performance of the zeolite-mixed polydimethylsiloxane (PDMS) membranes were evaluated to recover butanol from butanol/water binary solution as well as fermentation broth in the integrated ABE fermentation system. The separation factor and butanol titer in permeate of the zeolite-mixed PDMS membrane were up to 33.0 and 334.6&nbsp;g/L at 80°C, respectively, which increased with increasing zeolite loading weight in the membrane as well as feed temperature. The enhanced butanol separation factor was attributed to the hydrophobic zeolites with large pore size providing selective routes preferable for butanol permeation. In fed-batch fermentation incorporated with pervaporation, 54.9&nbsp;g/L ABE (34.5&nbsp;g/L butanol, 17.0&nbsp;g/L acetone and 3.4&nbsp;g/L ethanol) were produced from 172.3&nbsp;g/L glucose. The overall butanol productivity and yield increased by 16.0 and 11.1%, respectively, which was attributed to the alleviated butanol inhibition by pervaporation and reassimilation of acids for ABE production. The zeolite-mixed membrane produced a highly concentrated condensate containing 169.6&nbsp;g/L butanol or 253.3&nbsp;g/L ABE, which after phase separation easily gave the final product containing >600&nbsp;g/L butanol.</P><P><B>Conclusions</B></P><P>Zeolite loading in the PDMS matrix was attributed to improving the pervaporative performance of the membrane, showing great potential to recover butanol with high purity. Therefore, this zeolite-mixed PDMS membrane had the potential to improve biobutanol production when integrating with ABE fermentation.</P>

발행연도

2015

발행기관

BioMed Central

ISSN

1754-6834

8

페이지

pp.105

주제어

ABE fermentation; Pervaporation; Butanol recovery; Zeolite-mixed membrane

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1 2023-12-11
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논문; 2015-12-31

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