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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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 |
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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 |
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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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