Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development
Edible oil-based feedstocks based biodiesel is still leading the industry around the world. Canola oil (Brassica napus L.) contributes significantly to that race. Process optimisation and the development of reaction kinetic models of edible oil feedstocks are still required since the knowledge of ki...
Saved in:
Main Authors: | , , , , , , |
---|---|
Other Authors: | |
Format: | Article |
Published: |
Springer Science and Business Media B.V.
2024
|
Subjects: | |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
id |
my.uniten.dspace-33975 |
---|---|
record_format |
dspace |
spelling |
my.uniten.dspace-339752024-10-14T11:17:33Z Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. 55936470700 6603918185 57221158930 55962751500 58776756000 55310784800 56997615100 Biodiesel Homogeneous alkaline catalyst Optimisation Reaction kinetics RSM Transesterification activation energy biofuel catalyst chemical reaction herb industrial production numerical model optimization reaction kinetics response surface methodology Edible oil-based feedstocks based biodiesel is still leading the industry around the world. Canola oil (Brassica napus L.) contributes significantly to that race. Process optimisation and the development of reaction kinetic models of edible oil feedstocks are still required since the knowledge of kinetics is needed for designing industrial facilities and evaluating the performance of catalysts during transesterification or other related processes in a biorefinery. This research focuses on the transesterification process for biodiesel production because of its higher output efficiency, reactivity with feedstock, techno-economic feasibility in terms of FFA content, and environmental sustainability. The response surface method with the Box�Behnken model was used to optimise the process. Multivariate analysis of variance (ANOVA) was also performed to investigate the effectiveness of the regression model. The optimal process conditions were found to be 5.89�M methanol, 0.5% (w/w) KOH, 60��C and 120�min. The predicted yield was 99.5% for a 95% confidence interval (99.1, 99.9). The experimental yield was 99.6% for these conditions. Two different kinetic models were also developed in this study. The activation energy was 16.9% higher for the pseudo-first-order irreversible reaction than for the pseudo-homogenous irreversible reaction. Such a comprehensive analysis will assist stakeholders in evaluating the technology for industrial development in biodiesel fuel commercialisation. � 2022, The Author(s). Final 2024-10-14T03:17:33Z 2024-10-14T03:17:33Z 2023 Article 10.1007/s10668-022-02506-0 2-s2.0-85135258505 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85135258505&doi=10.1007%2fs10668-022-02506-0&partnerID=40&md5=0458706aa5938c359ac9f901b5a10283 https://irepository.uniten.edu.my/handle/123456789/33975 25 11 12247 12272 All Open Access Hybrid Gold Open Access Springer Science and Business Media B.V. Scopus |
institution |
Universiti Tenaga Nasional |
building |
UNITEN Library |
collection |
Institutional Repository |
continent |
Asia |
country |
Malaysia |
content_provider |
Universiti Tenaga Nasional |
content_source |
UNITEN Institutional Repository |
url_provider |
http://dspace.uniten.edu.my/ |
topic |
Biodiesel Homogeneous alkaline catalyst Optimisation Reaction kinetics RSM Transesterification activation energy biofuel catalyst chemical reaction herb industrial production numerical model optimization reaction kinetics response surface methodology |
spellingShingle |
Biodiesel Homogeneous alkaline catalyst Optimisation Reaction kinetics RSM Transesterification activation energy biofuel catalyst chemical reaction herb industrial production numerical model optimization reaction kinetics response surface methodology Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development |
description |
Edible oil-based feedstocks based biodiesel is still leading the industry around the world. Canola oil (Brassica napus L.) contributes significantly to that race. Process optimisation and the development of reaction kinetic models of edible oil feedstocks are still required since the knowledge of kinetics is needed for designing industrial facilities and evaluating the performance of catalysts during transesterification or other related processes in a biorefinery. This research focuses on the transesterification process for biodiesel production because of its higher output efficiency, reactivity with feedstock, techno-economic feasibility in terms of FFA content, and environmental sustainability. The response surface method with the Box�Behnken model was used to optimise the process. Multivariate analysis of variance (ANOVA) was also performed to investigate the effectiveness of the regression model. The optimal process conditions were found to be 5.89�M methanol, 0.5% (w/w) KOH, 60��C and 120�min. The predicted yield was 99.5% for a 95% confidence interval (99.1, 99.9). The experimental yield was 99.6% for these conditions. Two different kinetic models were also developed in this study. The activation energy was 16.9% higher for the pseudo-first-order irreversible reaction than for the pseudo-homogenous irreversible reaction. Such a comprehensive analysis will assist stakeholders in evaluating the technology for industrial development in biodiesel fuel commercialisation. � 2022, The Author(s). |
author2 |
55936470700 |
author_facet |
55936470700 Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. |
format |
Article |
author |
Hazrat M.A. Rasul M.G. Khan M.M.K. Ashwath N. Fattah I.M.R. Ong H.C. Mahlia T.M.I. |
author_sort |
Hazrat M.A. |
title |
Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development |
title_short |
Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development |
title_full |
Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development |
title_fullStr |
Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development |
title_full_unstemmed |
Biodiesel production from transesterification of Australian Brassica napus L. oil: optimisation and reaction kinetic model development |
title_sort |
biodiesel production from transesterification of australian brassica napus l. oil: optimisation and reaction kinetic model development |
publisher |
Springer Science and Business Media B.V. |
publishDate |
2024 |
_version_ |
1814061160484306944 |
score |
13.214268 |