Biobutanol production from C5/C6 carbohydrates integrated with pervaporation: experimental results and conceptual plant design

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• 作者：Wouter Van Hecke ; Pieter Vandezande…
• 关键词：Bioprocess design ; Biobutanol ; Process integration ; Product inhibition ; In situ product recovery ; Pervaporation
• 刊名：Journal of Industrial Microbiology and Biotechnology
• 出版年：2016
• 出版时间：January 2016
• 年：2016
• 卷：43
• 期：1
• 页码：25-36
• 全文大小：1,392 KB
• 参考文献：1.de Vrije T, Budde M, van der Wal H, Claassen PAM, López-Contreras AM (2013) “In situ” removal of isopropanol, butanol and ethanol from fermentation broth by gas stripping. Bioresour Technol 137:153–159PubMed CrossRef
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• 作者单位：Wouter Van Hecke (1)
  Pieter Vandezande (1)
  Marjorie Dubreuil (1)
  Maarten Uyttebroek (1)
  Herman Beckers (1)
  Heleen De Wever (1)
  
  1. Flemish Institute for Technological Research (VITO), Business Unit Separation and Conversion Technology, Boeretang 200, 2400, Mol, Belgium
  
• 刊物类别：Biomedical and Life Sciences
• 刊物主题：Chemistry
  Biotechnology
  Genetic Engineering
  Biochemistry
  Bioinformatics
  Microbiology
  Microbial Genetics and Genomics
  
• 出版者：Springer Berlin / Heidelberg
• ISSN：1476-5535

文摘

In this study, a simulated lignocellulosic hydrolyzate was used in a continuous two-stage fermentor setup for production of acetone, butanol and ethanol. An organophilic pervaporation unit was coupled to the second fermentor. The dilution rate in the first fermentor was kept constant at 0.109 h−1, while the dilution rate in the second fermentor was gradually decreased from 0.056 to 0.020 h−1. Glucose was completely consumed, while 61 % of the xylose was consumed at the lowest dilution rate, leading to an overall solvent productivity of 0.65 g L−1 h−1 and a high concentration of 185 g kg−1 solvents in the permeate in the last fermentation zone during 192 h. Based on the experimental results, a process integrated with organophilic pervaporation was conceptually designed and compared with a base-case. Chemcad simulations indicate an energy reduction of ~50 % when organophilic pervaporation is used. This study also demonstrates significant reductions in process flows and energy consumption by the use of organophilic pervaporation as in situ product recovery technology.