Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant Volume

There are several challenges for ABE fermentation to be used in an industrial scale including the low of butanol yield, the high energy requirement for separation and purification, and the competeness of sugar with food demand as substrat. In this study, techno-economical aspects of ABE fermentation...

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Main Authors: Rizki Fitria Darmayanti, Maktum Muharja, Tao Zhao, Ming Gao, Yukihiro Tashiro, Kenji Sakai, Kenji Sonomoto
Format: Article
Language:English
Published: Politeknik Negeri Malang 2022-10-01
Series:Jurnal Teknik Kimia dan Lingkungan
Subjects:
Online Access:http://jurnal.polinema.ac.id/index.php/jtkl/article/view/1624
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author Rizki Fitria Darmayanti
Maktum Muharja,
Tao Zhao
Ming Gao
Yukihiro Tashiro
Kenji Sakai
Kenji Sonomoto
author_facet Rizki Fitria Darmayanti
Maktum Muharja,
Tao Zhao
Ming Gao
Yukihiro Tashiro
Kenji Sakai
Kenji Sonomoto
author_sort Rizki Fitria Darmayanti
collection DOAJ
description There are several challenges for ABE fermentation to be used in an industrial scale including the low of butanol yield, the high energy requirement for separation and purification, and the competeness of sugar with food demand as substrat. In this study, techno-economical aspects of ABE fermentation by using immobilized cells with large extractant volume were studied. Overall production process was designed using rice straw as raw material which is semi-hydrolyzed to produce cellobiose, glucose, xylose, and arabinose mixture. Concentrated sugar was then fed to extractive fed-batch fermentation using immobilized cells. Finally, extractant was recovered and products were purified by distillation column. By evaluating this process design for the small scale capacity of 238 kg-butanol and acetone/day, the energy requirement was 41.3 MJ/kg-butanol and acetone and the cost was 1.91 $/kg-butanol and acetone. Although the cost was higher than butanol produced by petrochemical process of 1.08 $/kg-butanol, it may reduce if the scale is increased.
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spelling doaj.art-f4f4cba199944fbda1bdb5c9b0d387282023-05-09T03:19:38ZengPoliteknik Negeri MalangJurnal Teknik Kimia dan Lingkungan2579-85372579-97462022-10-01629911110.33795/jtkl.v6i2.3371624Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant VolumeRizki Fitria Darmayanti0Maktum Muharja,1Tao Zhao2Ming Gao3Yukihiro Tashiro4Kenji Sakai5Kenji Sonomoto6Department of Chemical Engineering, Faculty of Engineering, Universitas Jember, Jl. Kalimantan 37 Jember 68121, IndonesiaDepartment of Chemical Engineering, Faculty of Engineering, Universitas Jember, Jl. Kalimantan 37 Jember 68121, IndonesiaEnergy-rich Compounds Production by Photosynthetic Carbon Fixation Research Center, College of Life Science, Qingdao Agricultural University, Chengyang District, Qingdao 266109, China3Department of Environmental Engineering, University of Science and Technology Beijing, Beijing 100083, ChinaDepartment of Bioscience and Biotechnology, Faculty of Agriculture, Graduate School, Kyushu University, 744, Motooka, Nishi-ku, Fukuoka 819-0395, JapanDepartment of Bioscience and Biotechnology, Faculty of Agriculture, Graduate School, Kyushu University, 744, Motooka, Nishi-ku, Fukuoka 819-0395, JapanDepartment of Bioscience and Biotechnology, Faculty of Agriculture, Graduate School, Kyushu University, 744, Motooka, Nishi-ku, Fukuoka 819-0395, JapanThere are several challenges for ABE fermentation to be used in an industrial scale including the low of butanol yield, the high energy requirement for separation and purification, and the competeness of sugar with food demand as substrat. In this study, techno-economical aspects of ABE fermentation by using immobilized cells with large extractant volume were studied. Overall production process was designed using rice straw as raw material which is semi-hydrolyzed to produce cellobiose, glucose, xylose, and arabinose mixture. Concentrated sugar was then fed to extractive fed-batch fermentation using immobilized cells. Finally, extractant was recovered and products were purified by distillation column. By evaluating this process design for the small scale capacity of 238 kg-butanol and acetone/day, the energy requirement was 41.3 MJ/kg-butanol and acetone and the cost was 1.91 $/kg-butanol and acetone. Although the cost was higher than butanol produced by petrochemical process of 1.08 $/kg-butanol, it may reduce if the scale is increased.http://jurnal.polinema.ac.id/index.php/jtkl/article/view/1624abefermentationimmobilized cellsugartechno-economic.
spellingShingle Rizki Fitria Darmayanti
Maktum Muharja,
Tao Zhao
Ming Gao
Yukihiro Tashiro
Kenji Sakai
Kenji Sonomoto
Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant Volume
Jurnal Teknik Kimia dan Lingkungan
abe
fermentation
immobilized cell
sugar
techno-economic.
title Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant Volume
title_full Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant Volume
title_fullStr Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant Volume
title_full_unstemmed Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant Volume
title_short Techno-Economic Analysis of Extractive Butanol Fermentation by Immobilized Cells with Large Extractant Volume
title_sort techno economic analysis of extractive butanol fermentation by immobilized cells with large extractant volume
topic abe
fermentation
immobilized cell
sugar
techno-economic.
url http://jurnal.polinema.ac.id/index.php/jtkl/article/view/1624
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