Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization

This work proposes the optimization of 2-ethylhexyl (2-EH) caprylate/caprate synthesis in a pulsed loop reactor, and the energy efficiency of the reactor was assessed. 2-EH caprylate/caprate can be used as a biodegradable base fluid. Only 0.4 wt% catalyst concentration was used in the reaction. The...

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Main Authors: Razali, S.Z., Yunus, R., Abdul Rashid, Suraya, Lim, Hong Ngee, Mohamed Jan, Badrul, Hamid, H.A.
Format: Article
Published: Elsevier 2020
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Online Access:http://eprints.um.edu.my/25314/
https://doi.org/10.1016/j.cep.2020.107837
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spelling my.um.eprints.253142020-08-12T00:56:48Z http://eprints.um.edu.my/25314/ Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization Razali, S.Z. Yunus, R. Abdul Rashid, Suraya Lim, Hong Ngee Mohamed Jan, Badrul Hamid, H.A. TP Chemical technology This work proposes the optimization of 2-ethylhexyl (2-EH) caprylate/caprate synthesis in a pulsed loop reactor, and the energy efficiency of the reactor was assessed. 2-EH caprylate/caprate can be used as a biodegradable base fluid. Only 0.4 wt% catalyst concentration was used in the reaction. The face-centred central composite design (FCCD) experiment coupled response surface methodology (RSM) has been implemented to screen independent parameters. The optimization process showed that vacuum pressure was the most influential factor followed by oscillation speed, temperature and time. The maximum conversion of 98 % and yield of 89 % were achieved under optimal conditions of 78 °C, 10 mbar, 20 min and 155 rpm. Meanwhile, energy balance calculation indicated that the usage of low vacuum pressure not only significantly reduced the total heat duty from 1381 kJ (1 atm) to 823 kJ (10 mbar) but also alleviated the reaction temperature from 172 °C (1 atm) to 78 °C (10 mbar). The calculation also demonstrated that the reflux-stirred tank reactor produced a lower conversion and yield of ester yet 6 kJ higher total heat duty compared to the pulsed loop reactor, indicating a cost-saving with the pulsed loop reactor. © 2020 Elsevier B.V. Elsevier 2020 Article PeerReviewed Razali, S.Z. and Yunus, R. and Abdul Rashid, Suraya and Lim, Hong Ngee and Mohamed Jan, Badrul and Hamid, H.A. (2020) Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization. Chemical Engineering and Processing - Process Intensification, 149. p. 107837. ISSN 0255-2701 https://doi.org/10.1016/j.cep.2020.107837 doi:10.1016/j.cep.2020.107837
institution Universiti Malaya
building UM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaya
content_source UM Research Repository
url_provider http://eprints.um.edu.my/
topic TP Chemical technology
spellingShingle TP Chemical technology
Razali, S.Z.
Yunus, R.
Abdul Rashid, Suraya
Lim, Hong Ngee
Mohamed Jan, Badrul
Hamid, H.A.
Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization
description This work proposes the optimization of 2-ethylhexyl (2-EH) caprylate/caprate synthesis in a pulsed loop reactor, and the energy efficiency of the reactor was assessed. 2-EH caprylate/caprate can be used as a biodegradable base fluid. Only 0.4 wt% catalyst concentration was used in the reaction. The face-centred central composite design (FCCD) experiment coupled response surface methodology (RSM) has been implemented to screen independent parameters. The optimization process showed that vacuum pressure was the most influential factor followed by oscillation speed, temperature and time. The maximum conversion of 98 % and yield of 89 % were achieved under optimal conditions of 78 °C, 10 mbar, 20 min and 155 rpm. Meanwhile, energy balance calculation indicated that the usage of low vacuum pressure not only significantly reduced the total heat duty from 1381 kJ (1 atm) to 823 kJ (10 mbar) but also alleviated the reaction temperature from 172 °C (1 atm) to 78 °C (10 mbar). The calculation also demonstrated that the reflux-stirred tank reactor produced a lower conversion and yield of ester yet 6 kJ higher total heat duty compared to the pulsed loop reactor, indicating a cost-saving with the pulsed loop reactor. © 2020 Elsevier B.V.
format Article
author Razali, S.Z.
Yunus, R.
Abdul Rashid, Suraya
Lim, Hong Ngee
Mohamed Jan, Badrul
Hamid, H.A.
author_facet Razali, S.Z.
Yunus, R.
Abdul Rashid, Suraya
Lim, Hong Ngee
Mohamed Jan, Badrul
Hamid, H.A.
author_sort Razali, S.Z.
title Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization
title_short Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization
title_full Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization
title_fullStr Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization
title_full_unstemmed Process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: Multi-objective optimization
title_sort process intensification of 2-ethylhexyl caprylate/caprate synthesis via a pulsed loop reactor: multi-objective optimization
publisher Elsevier
publishDate 2020
url http://eprints.um.edu.my/25314/
https://doi.org/10.1016/j.cep.2020.107837
_version_ 1680857017987629056