Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor

The purpose of this study was to evaluate the feasibility of producing bioethanol from palm-oil mill effluent generated by the oil-palm industries through direct bioconversion process. The bioethanol production was carried out through the treatment of compatible mixed cultures such as Thrichode...

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Main Authors: Alam, Md. Zahangir, Kabbashi, Nassereldeen Ahmed, Hussin, S. Nahdatul I. S.
Format: Article
Language:English
Published: Springer Science 2009
Subjects:
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http://irep.iium.edu.my/5062/
http://irep.iium.edu.my/5062/1/Paper-bioethanol-JIMB.pdf
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spelling iium-50622012-10-03T04:08:37Z http://irep.iium.edu.my/5062/ Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor Alam, Md. Zahangir Kabbashi, Nassereldeen Ahmed Hussin, S. Nahdatul I. S. QD Chemistry TP Chemical technology TP248.13 Biotechnology The purpose of this study was to evaluate the feasibility of producing bioethanol from palm-oil mill effluent generated by the oil-palm industries through direct bioconversion process. The bioethanol production was carried out through the treatment of compatible mixed cultures such as Thrichoderma harzianum, Phanerochaete chrysosporium, Mucor hiemalis, and yeast, Saccharomyces cerevisiae. Simultaneous inoculation of T. harzianum and S. cerevisiae was found to be the mixed culture that yielded the highest ethanol production (4% v/v or 31.6 g/l). Statistical optimization was carried out to determine the operating conditions of the stirred-tank bioreactor for maximum bioethanol production by a two-level fractional factorial design with a single central point. The factors involved were oxygen saturation level (pO2%), temperature, and pH. A polynomial regression model was developed using the experimental data including the linear,quadratic, and interaction effects. Statistical analysis showed that the maximum ethanol production of 4.6% (v/v) or 36.3 g/l was achieved at a temperature of 32�C, pH of 6, and pO2 of 30%. The results of the model validation test under the developed optimum process conditions indicated that the maximum production was increased from 4.6% (v/v) to 6.5% (v/v) or 51.3 g/l with 89.1% chemicaloxygen-demand removal. Springer Science 2009-06 Article PeerReviewed application/pdf en http://irep.iium.edu.my/5062/1/Paper-bioethanol-JIMB.pdf Alam, Md. Zahangir and Kabbashi, Nassereldeen Ahmed and Hussin, S. Nahdatul I. S. (2009) Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor. Journal of Industrial Microbiology & Biotechnology, 36 (6). pp. 801-808. ISSN 1367-5435 http://dx.doi.org/10.1007/s10295-009-0554-7 doi:10.1007/s10295-009-0554-7
repository_type Digital Repository
institution_category Local University
institution International Islamic University Malaysia
building IIUM Repository
collection Online Access
language English
topic QD Chemistry
TP Chemical technology
TP248.13 Biotechnology
spellingShingle QD Chemistry
TP Chemical technology
TP248.13 Biotechnology
Alam, Md. Zahangir
Kabbashi, Nassereldeen Ahmed
Hussin, S. Nahdatul I. S.
Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor
description The purpose of this study was to evaluate the feasibility of producing bioethanol from palm-oil mill effluent generated by the oil-palm industries through direct bioconversion process. The bioethanol production was carried out through the treatment of compatible mixed cultures such as Thrichoderma harzianum, Phanerochaete chrysosporium, Mucor hiemalis, and yeast, Saccharomyces cerevisiae. Simultaneous inoculation of T. harzianum and S. cerevisiae was found to be the mixed culture that yielded the highest ethanol production (4% v/v or 31.6 g/l). Statistical optimization was carried out to determine the operating conditions of the stirred-tank bioreactor for maximum bioethanol production by a two-level fractional factorial design with a single central point. The factors involved were oxygen saturation level (pO2%), temperature, and pH. A polynomial regression model was developed using the experimental data including the linear,quadratic, and interaction effects. Statistical analysis showed that the maximum ethanol production of 4.6% (v/v) or 36.3 g/l was achieved at a temperature of 32�C, pH of 6, and pO2 of 30%. The results of the model validation test under the developed optimum process conditions indicated that the maximum production was increased from 4.6% (v/v) to 6.5% (v/v) or 51.3 g/l with 89.1% chemicaloxygen-demand removal.
format Article
author Alam, Md. Zahangir
Kabbashi, Nassereldeen Ahmed
Hussin, S. Nahdatul I. S.
author_facet Alam, Md. Zahangir
Kabbashi, Nassereldeen Ahmed
Hussin, S. Nahdatul I. S.
author_sort Alam, Md. Zahangir
title Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor
title_short Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor
title_full Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor
title_fullStr Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor
title_full_unstemmed Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor
title_sort production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor
publisher Springer Science
publishDate 2009
url http://irep.iium.edu.my/5062/
http://irep.iium.edu.my/5062/
http://irep.iium.edu.my/5062/
http://irep.iium.edu.my/5062/1/Paper-bioethanol-JIMB.pdf
first_indexed 2023-09-18T20:13:33Z
last_indexed 2023-09-18T20:13:33Z
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