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...
Main Authors: | , , , , , , |
---|---|
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 |
_version_ | 1827951757290897408 |
---|---|
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. |
first_indexed | 2024-04-09T13:47:34Z |
format | Article |
id | doaj.art-f4f4cba199944fbda1bdb5c9b0d38728 |
institution | Directory Open Access Journal |
issn | 2579-8537 2579-9746 |
language | English |
last_indexed | 2024-04-09T13:47:34Z |
publishDate | 2022-10-01 |
publisher | Politeknik Negeri Malang |
record_format | Article |
series | Jurnal Teknik Kimia dan Lingkungan |
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 |
work_keys_str_mv | AT rizkifitriadarmayanti technoeconomicanalysisofextractivebutanolfermentationbyimmobilizedcellswithlargeextractantvolume AT maktummuharja technoeconomicanalysisofextractivebutanolfermentationbyimmobilizedcellswithlargeextractantvolume AT taozhao technoeconomicanalysisofextractivebutanolfermentationbyimmobilizedcellswithlargeextractantvolume AT minggao technoeconomicanalysisofextractivebutanolfermentationbyimmobilizedcellswithlargeextractantvolume AT yukihirotashiro technoeconomicanalysisofextractivebutanolfermentationbyimmobilizedcellswithlargeextractantvolume AT kenjisakai technoeconomicanalysisofextractivebutanolfermentationbyimmobilizedcellswithlargeextractantvolume AT kenjisonomoto technoeconomicanalysisofextractivebutanolfermentationbyimmobilizedcellswithlargeextractantvolume |