Enhancement of n-butanol production by in situ butanol removal using permeating–heating–gas stripping in acetone–butanol–ethanol fermentation

•Gas stripping model of ABE from model solutions was characterized.•Integrated fermentation system with gas stripping for in situ butanol recovery.•Fed-batch fermentation with solvent removal at 70°C has been demonstrated.•Permeating–heating–gas stripping greatly enhances butanol productivity and yi...

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Veröffentlicht in:Bioresource technology 2014-07, Vol.164, p.276-284
Hauptverfasser: Chen, Yong, Ren, Hengfei, Liu, Dong, Zhao, Ting, Shi, Xinchi, Cheng, Hao, Zhao, Nan, Li, Zhenjian, Li, Bingbing, Niu, Huanqing, Zhuang, Wei, Xie, Jingjing, Chen, Xiaochun, Wu, Jinglan, Ying, Hanjie
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container_title Bioresource technology
container_volume 164
creator Chen, Yong
Ren, Hengfei
Liu, Dong
Zhao, Ting
Shi, Xinchi
Cheng, Hao
Zhao, Nan
Li, Zhenjian
Li, Bingbing
Niu, Huanqing
Zhuang, Wei
Xie, Jingjing
Chen, Xiaochun
Wu, Jinglan
Ying, Hanjie
description •Gas stripping model of ABE from model solutions was characterized.•Integrated fermentation system with gas stripping for in situ butanol recovery.•Fed-batch fermentation with solvent removal at 70°C has been demonstrated.•Permeating–heating–gas stripping greatly enhances butanol productivity and yield. Butanol recovery from acetone–butanol–ethanol (ABE) fed-batch fermentation using permeating–heating–gas was determined in this study. Fermentation was performed with Clostridium acetobutylicum B3 in a fibrous bed bioreactor and permeating–heating–gas stripping was used to eliminate substrate and product inhibition, which normally restrict ABE production and sugar utilization to below 20g/L and 60g/L, respectively. In batch fermentation (without permeating–heating–gas stripping), C. acetobutylicum B3 utilized 60g/L glucose and produced 19.9g/L ABE and 12g/L butanol, while in the integrated process 290g/L glucose was utilized and 106.27g/L ABE and 66.09g/L butanol were produced. The intermittent gas stripping process generated a highly concentrated condensate containing approximately 15% (w/v) butanol, 4% (w/v) acetone, a small amount of ethanol (
doi_str_mv 10.1016/j.biortech.2014.04.107
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Butanol recovery from acetone–butanol–ethanol (ABE) fed-batch fermentation using permeating–heating–gas was determined in this study. Fermentation was performed with Clostridium acetobutylicum B3 in a fibrous bed bioreactor and permeating–heating–gas stripping was used to eliminate substrate and product inhibition, which normally restrict ABE production and sugar utilization to below 20g/L and 60g/L, respectively. In batch fermentation (without permeating–heating–gas stripping), C. acetobutylicum B3 utilized 60g/L glucose and produced 19.9g/L ABE and 12g/L butanol, while in the integrated process 290g/L glucose was utilized and 106.27g/L ABE and 66.09g/L butanol were produced. The intermittent gas stripping process generated a highly concentrated condensate containing approximately 15% (w/v) butanol, 4% (w/v) acetone, a small amount of ethanol (&lt;1%), and almost no acids, resulting in a highly concentrated butanol solution [∼70% (w/v)] after phase separation. Butanol removal by permeating–heating–gas stripping has potential for commercial ABE production.</description><identifier>ISSN: 0960-8524</identifier><identifier>EISSN: 1873-2976</identifier><identifier>DOI: 10.1016/j.biortech.2014.04.107</identifier><identifier>PMID: 24862004</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>1-Butanol - metabolism ; ABE fermentation ; Acetone ; Acetone - metabolism ; Batch Cell Culture Techniques ; Biological and medical sciences ; Biotechnology ; Biotechnology - methods ; Butanol ; Cell immobilization ; Clostridium acetobutylicum - metabolism ; Ethanol ; Ethanol - metabolism ; Ethyl alcohol ; Fed-batch fermentation ; Fermentation ; Fundamental and applied biological sciences. Psychology ; Gases - chemistry ; Glucose ; Heating ; Kinetics ; Methods. Procedures. Technologies ; Microbial engineering. 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Butanol recovery from acetone–butanol–ethanol (ABE) fed-batch fermentation using permeating–heating–gas was determined in this study. Fermentation was performed with Clostridium acetobutylicum B3 in a fibrous bed bioreactor and permeating–heating–gas stripping was used to eliminate substrate and product inhibition, which normally restrict ABE production and sugar utilization to below 20g/L and 60g/L, respectively. In batch fermentation (without permeating–heating–gas stripping), C. acetobutylicum B3 utilized 60g/L glucose and produced 19.9g/L ABE and 12g/L butanol, while in the integrated process 290g/L glucose was utilized and 106.27g/L ABE and 66.09g/L butanol were produced. The intermittent gas stripping process generated a highly concentrated condensate containing approximately 15% (w/v) butanol, 4% (w/v) acetone, a small amount of ethanol (&lt;1%), and almost no acids, resulting in a highly concentrated butanol solution [∼70% (w/v)] after phase separation. Butanol removal by permeating–heating–gas stripping has potential for commercial ABE production.</description><subject>1-Butanol - metabolism</subject><subject>ABE fermentation</subject><subject>Acetone</subject><subject>Acetone - metabolism</subject><subject>Batch Cell Culture Techniques</subject><subject>Biological and medical sciences</subject><subject>Biotechnology</subject><subject>Biotechnology - methods</subject><subject>Butanol</subject><subject>Cell immobilization</subject><subject>Clostridium acetobutylicum - metabolism</subject><subject>Ethanol</subject><subject>Ethanol - metabolism</subject><subject>Ethyl alcohol</subject><subject>Fed-batch fermentation</subject><subject>Fermentation</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Gases - chemistry</subject><subject>Glucose</subject><subject>Heating</subject><subject>Kinetics</subject><subject>Methods. Procedures. Technologies</subject><subject>Microbial engineering. 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Butanol recovery from acetone–butanol–ethanol (ABE) fed-batch fermentation using permeating–heating–gas was determined in this study. Fermentation was performed with Clostridium acetobutylicum B3 in a fibrous bed bioreactor and permeating–heating–gas stripping was used to eliminate substrate and product inhibition, which normally restrict ABE production and sugar utilization to below 20g/L and 60g/L, respectively. In batch fermentation (without permeating–heating–gas stripping), C. acetobutylicum B3 utilized 60g/L glucose and produced 19.9g/L ABE and 12g/L butanol, while in the integrated process 290g/L glucose was utilized and 106.27g/L ABE and 66.09g/L butanol were produced. The intermittent gas stripping process generated a highly concentrated condensate containing approximately 15% (w/v) butanol, 4% (w/v) acetone, a small amount of ethanol (&lt;1%), and almost no acids, resulting in a highly concentrated butanol solution [∼70% (w/v)] after phase separation. Butanol removal by permeating–heating–gas stripping has potential for commercial ABE production.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><pmid>24862004</pmid><doi>10.1016/j.biortech.2014.04.107</doi><tpages>9</tpages></addata></record>
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subjects 1-Butanol - metabolism
ABE fermentation
Acetone
Acetone - metabolism
Batch Cell Culture Techniques
Biological and medical sciences
Biotechnology
Biotechnology - methods
Butanol
Cell immobilization
Clostridium acetobutylicum - metabolism
Ethanol
Ethanol - metabolism
Ethyl alcohol
Fed-batch fermentation
Fermentation
Fundamental and applied biological sciences. Psychology
Gases - chemistry
Glucose
Heating
Kinetics
Methods. Procedures. Technologies
Microbial engineering. Fermentation and microbial culture technology
Models, Theoretical
Permeating–heating–gas stripping
Solutions
Solvents - chemistry
Stripping
Substrate inhibition
title Enhancement of n-butanol production by in situ butanol removal using permeating–heating–gas stripping in acetone–butanol–ethanol fermentation
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