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Low energy intensity production of fuel-grade bio-butanol enabled by membrane-based extractionopen access

Authors
Kim, Ji HoonCook, MarcusPeeva, LudmilaYeo, JetBolton, Leslie W.Lee, Young MooLivingston, Andrew G.
Issue Date
Dec-2020
Publisher
ROYAL SOC CHEMISTRY
Citation
ENERGY & ENVIRONMENTAL SCIENCE, v.13, no.12, pp.4862 - 4871
Indexed
SCIE
SCOPUS
Journal Title
ENERGY & ENVIRONMENTAL SCIENCE
Volume
13
Number
12
Start Page
4862
End Page
4871
URI
https://scholarworks.bwise.kr/hanyang/handle/2021.sw.hanyang/133923
DOI
10.1039/d0ee02927k
ISSN
1754-5692
Abstract
Widespread use of biofuels is inhibited by the significant energy burden of recovering fuel products from aqueous fermentation systems. Here, we describe a membrane-based extraction (perstraction) system for the recovery of fuel-grade biobutanol from fermentation broths which can extract n-butanol with high purity (> 99.5%) while using less than 25% of the energy of current technology options. This is achieved by combining a spray-coated thin-film composite membrane with 2-ethyl-1-hexanol as an extractant. The membrane successfully protects the micro-organisms from the extractant, which, although ideal in other respects, is a metabolic inhibitor. In contrast to water, the extractant does not form a heterogeneous azeotrope with n-butanol, and the overall energy consumption of for n-butanol production is 3.9 MJ kg(-1), substantially less than other recovery processes (17.0-29.4 MJ kg(-1)). By (a) extracting n-butanol from the fermentation broth without a phase change, (b) breaking the heterogeneous azeotrope relationship (less energy consumption for distillation), and (c) utilizing a small volume ratio of extractant : fermentation broth (1 : 100, v/v), the need for high energy intensity processes such as pervaporation, gas stripping or liquid-liquid extraction is avoided. The application of this perstraction system to continuous production of a range of higher alcohols is explored and shown to be highly favourable.
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