A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production

The objective of this study was to develop an efficient method for enhancing the production of bioethanol in a single-reactor system (SRS) by implementing acid–base pretreatment and enzymatic hydrolysis techniques, thereby eliminating differentiation and removal processes. The aim was to establish a...

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Main Authors: Deb, Nibedita, Rahman, Tawfkur, Alam, Md Zahangir, Miah, Md Shohidullah, Kamal, Reashad
Format: Article
Language:English
English
English
Published: Wiley 2024
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Online Access:http://irep.iium.edu.my/115430/1/115430_A%20single-reactor%20system.pdf
http://irep.iium.edu.my/115430/2/115430_A%20single-reactor%20system_SCOPUS.pdf
http://irep.iium.edu.my/115430/3/115430_A%20single-reactor%20system_WOS.pdf
http://irep.iium.edu.my/115430/
https://onlinelibrary.wiley.com/doi/10.1155/2024/5264918
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spelling my.iium.irep.1154302024-11-01T08:04:50Z http://irep.iium.edu.my/115430/ A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production Deb, Nibedita Rahman, Tawfkur Alam, Md Zahangir Miah, Md Shohidullah Kamal, Reashad TP248.13 Biotechnology The objective of this study was to develop an efficient method for enhancing the production of bioethanol in a single-reactor system (SRS) by implementing acid–base pretreatment and enzymatic hydrolysis techniques, thereby eliminating differentiation and removal processes. The aim was to establish a process for bioethanol synthesis using hydrolyzed palm oil mill effluent (POME) and a locally sourced cellulase enzyme. The pretreatment and enzymatic hydrolysis methods were successfully optimized, resulting in a maximum yield of reducing sugars of 26.6 g/L (53.14%). To achieve the highest bioethanol yield, fermentation was carried out using both the one-factor-at-a-time (OFAT) and face-centered central composite design (FCCCD) approaches. The OFAT approach was employed to obtain the maximum bioethanol production, which yielded 6.75% v/v of bioethanol from the hydrolyzed POME using the same bioreactor. In the case of the FCCCD process, the optimal conditions led to a bioethanol production of 7.64% v/v during the fermentation stage. Kinetic analyses of the bioethanol produced revealed a specific growth rate (μ) of 0.198 h−1 and a specific product formation rate (qp) of 0.239 h−1 after 3 days of fermentation. These findings highlight a promising strategy for efficient management of POME through the production of biofuels, which could contribute to the economic growth of the country. Wiley 2024-09-16 Article PeerReviewed application/pdf en http://irep.iium.edu.my/115430/1/115430_A%20single-reactor%20system.pdf application/pdf en http://irep.iium.edu.my/115430/2/115430_A%20single-reactor%20system_SCOPUS.pdf application/pdf en http://irep.iium.edu.my/115430/3/115430_A%20single-reactor%20system_WOS.pdf Deb, Nibedita and Rahman, Tawfkur and Alam, Md Zahangir and Miah, Md Shohidullah and Kamal, Reashad (2024) A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production. International Journal of Polymer Science, 2024 (1). pp. 1-21. ISSN 1687-9422 E-ISSN 1687-9430 https://onlinelibrary.wiley.com/doi/10.1155/2024/5264918 10.1155/2024/5264918
institution Universiti Islam Antarabangsa Malaysia
building IIUM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider International Islamic University Malaysia
content_source IIUM Repository (IREP)
url_provider http://irep.iium.edu.my/
language English
English
English
topic TP248.13 Biotechnology
spellingShingle TP248.13 Biotechnology
Deb, Nibedita
Rahman, Tawfkur
Alam, Md Zahangir
Miah, Md Shohidullah
Kamal, Reashad
A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production
description The objective of this study was to develop an efficient method for enhancing the production of bioethanol in a single-reactor system (SRS) by implementing acid–base pretreatment and enzymatic hydrolysis techniques, thereby eliminating differentiation and removal processes. The aim was to establish a process for bioethanol synthesis using hydrolyzed palm oil mill effluent (POME) and a locally sourced cellulase enzyme. The pretreatment and enzymatic hydrolysis methods were successfully optimized, resulting in a maximum yield of reducing sugars of 26.6 g/L (53.14%). To achieve the highest bioethanol yield, fermentation was carried out using both the one-factor-at-a-time (OFAT) and face-centered central composite design (FCCCD) approaches. The OFAT approach was employed to obtain the maximum bioethanol production, which yielded 6.75% v/v of bioethanol from the hydrolyzed POME using the same bioreactor. In the case of the FCCCD process, the optimal conditions led to a bioethanol production of 7.64% v/v during the fermentation stage. Kinetic analyses of the bioethanol produced revealed a specific growth rate (μ) of 0.198 h−1 and a specific product formation rate (qp) of 0.239 h−1 after 3 days of fermentation. These findings highlight a promising strategy for efficient management of POME through the production of biofuels, which could contribute to the economic growth of the country.
format Article
author Deb, Nibedita
Rahman, Tawfkur
Alam, Md Zahangir
Miah, Md Shohidullah
Kamal, Reashad
author_facet Deb, Nibedita
Rahman, Tawfkur
Alam, Md Zahangir
Miah, Md Shohidullah
Kamal, Reashad
author_sort Deb, Nibedita
title A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production
title_short A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production
title_full A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production
title_fullStr A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production
title_full_unstemmed A single-reactor system for simultaneous pretreatment and fermentation of POME for bioethanol production
title_sort single-reactor system for simultaneous pretreatment and fermentation of pome for bioethanol production
publisher Wiley
publishDate 2024
url http://irep.iium.edu.my/115430/1/115430_A%20single-reactor%20system.pdf
http://irep.iium.edu.my/115430/2/115430_A%20single-reactor%20system_SCOPUS.pdf
http://irep.iium.edu.my/115430/3/115430_A%20single-reactor%20system_WOS.pdf
http://irep.iium.edu.my/115430/
https://onlinelibrary.wiley.com/doi/10.1155/2024/5264918
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