Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol

To save cost and input energy for bioethanol production, a consolidated continuous solid-state fermentation system composed of a rotating drum reactor, a humidifier, and a condenser was developed. Biomass, saccharifying enzymes, yeast, and a minimum amount of water are introduced into the system. Et...

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Main Authors: Churairat Moukamnerd, Masahiro Kino-Oka, Minetaka Sugiyama, Yoshinobu Kaneko, Chuenchit Boonchird, Satoshi Harashima, Hideo Noda, Kazuaki Ninomiya, Suteaki Shioya, Yoshio Katakura
Other Authors: Osaka University
Format: Article
Published: 2018
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Online Access:https://repository.li.mahidol.ac.th/handle/123456789/28648
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spelling th-mahidol.286482018-09-24T16:04:46Z Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol Churairat Moukamnerd Masahiro Kino-Oka Minetaka Sugiyama Yoshinobu Kaneko Chuenchit Boonchird Satoshi Harashima Hideo Noda Kazuaki Ninomiya Suteaki Shioya Yoshio Katakura Osaka University Mahidol University Kansai Chemical Engineering Co. Ltd. Kanazawa University Sojo University Biochemistry, Genetics and Molecular Biology Immunology and Microbiology To save cost and input energy for bioethanol production, a consolidated continuous solid-state fermentation system composed of a rotating drum reactor, a humidifier, and a condenser was developed. Biomass, saccharifying enzymes, yeast, and a minimum amount of water are introduced into the system. Ethanol produced by simultaneous saccharification and fermentation is continuously recovered as vapor from the headspace of the reactor, while the humidifier compensates for the water loss. From raw corn starch as a biomass model, 95∈±∈3, 226∈±∈9, 458∈±∈26, and 509∈±∈64 g∈l-1of ethanol solutions were recovered continuously when the ethanol content in reactor was controlled at 10-20, 30-50, 50-70 and 75-85 g∈kg-mixture-1, respectively. The residue showed a lesser volume and higher solid content than that obtained by conventional liquid fermentation. The cost and energy for intensive waste water treatment are decreased, and the continuous fermentation enabled the sustainability of enzyme activity and yeast in the system. © 2010 Springer-Verlag. 2018-09-24T08:43:08Z 2018-09-24T08:43:08Z 2010-09-01 Article Applied Microbiology and Biotechnology. Vol.88, No.1 (2010), 87-94 10.1007/s00253-010-2716-y 01757598 2-s2.0-77955852609 https://repository.li.mahidol.ac.th/handle/123456789/28648 Mahidol University SCOPUS https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=77955852609&origin=inward
institution Mahidol University
building Mahidol University Library
continent Asia
country Thailand
Thailand
content_provider Mahidol University Library
collection Mahidol University Institutional Repository
topic Biochemistry, Genetics and Molecular Biology
Immunology and Microbiology
spellingShingle Biochemistry, Genetics and Molecular Biology
Immunology and Microbiology
Churairat Moukamnerd
Masahiro Kino-Oka
Minetaka Sugiyama
Yoshinobu Kaneko
Chuenchit Boonchird
Satoshi Harashima
Hideo Noda
Kazuaki Ninomiya
Suteaki Shioya
Yoshio Katakura
Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol
description To save cost and input energy for bioethanol production, a consolidated continuous solid-state fermentation system composed of a rotating drum reactor, a humidifier, and a condenser was developed. Biomass, saccharifying enzymes, yeast, and a minimum amount of water are introduced into the system. Ethanol produced by simultaneous saccharification and fermentation is continuously recovered as vapor from the headspace of the reactor, while the humidifier compensates for the water loss. From raw corn starch as a biomass model, 95∈±∈3, 226∈±∈9, 458∈±∈26, and 509∈±∈64 g∈l-1of ethanol solutions were recovered continuously when the ethanol content in reactor was controlled at 10-20, 30-50, 50-70 and 75-85 g∈kg-mixture-1, respectively. The residue showed a lesser volume and higher solid content than that obtained by conventional liquid fermentation. The cost and energy for intensive waste water treatment are decreased, and the continuous fermentation enabled the sustainability of enzyme activity and yeast in the system. © 2010 Springer-Verlag.
author2 Osaka University
author_facet Osaka University
Churairat Moukamnerd
Masahiro Kino-Oka
Minetaka Sugiyama
Yoshinobu Kaneko
Chuenchit Boonchird
Satoshi Harashima
Hideo Noda
Kazuaki Ninomiya
Suteaki Shioya
Yoshio Katakura
format Article
author Churairat Moukamnerd
Masahiro Kino-Oka
Minetaka Sugiyama
Yoshinobu Kaneko
Chuenchit Boonchird
Satoshi Harashima
Hideo Noda
Kazuaki Ninomiya
Suteaki Shioya
Yoshio Katakura
author_sort Churairat Moukamnerd
title Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol
title_short Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol
title_full Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol
title_fullStr Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol
title_full_unstemmed Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol
title_sort ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol
publishDate 2018
url https://repository.li.mahidol.ac.th/handle/123456789/28648
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