Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor

Diacylglycerols (DAG) have been widely used in many industries due to their remarkable capabilities as emulsifiers and stabilisers. However, developing a sustainable and an effective synthesis method for DAG remains a challenge. Continuous flow bio-reactor is recognized to be more productive, contro...

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Published in:Journal of Cleaner Production
Main Authors: Abd Razak, Nurul Nadiah, Cognet, Patrick, Pérès, Yolande, Gew, Lai Ti, Aroua, Mohamed Kheireddine
Format: Article in Journal/Newspaper
Language:unknown
Published: 2022
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Online Access:https://eprints.lancs.ac.uk/id/eprint/190082/
https://doi.org/10.1016/j.jclepro.2022.133816
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spelling ftulancaster:oai:eprints.lancs.ac.uk:190082 2023-08-27T04:06:23+02:00 Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor Abd Razak, Nurul Nadiah Cognet, Patrick Pérès, Yolande Gew, Lai Ti Aroua, Mohamed Kheireddine 2022-11-01 https://eprints.lancs.ac.uk/id/eprint/190082/ https://doi.org/10.1016/j.jclepro.2022.133816 unknown Abd Razak, Nurul Nadiah and Cognet, Patrick and Pérès, Yolande and Gew, Lai Ti and Aroua, Mohamed Kheireddine (2022) Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor. Journal of Cleaner Production, 373. ISSN 0959-6526 Journal Article PeerReviewed 2022 ftulancaster https://doi.org/10.1016/j.jclepro.2022.133816 2023-08-03T22:43:05Z Diacylglycerols (DAG) have been widely used in many industries due to their remarkable capabilities as emulsifiers and stabilisers. However, developing a sustainable and an effective synthesis method for DAG remains a challenge. Continuous flow bio-reactor is recognized to be more productive, controllable, and reliable instrument for developing green and intensified processes. In this work, a continuous flow packed bed millireactor was employed for the synthesis of glycerol dioelate (GDO) catalyzed by immobilized lipase namely Candida antartica. Experiments were carried out to evaluate the kinetic parameters as well as to assess the internal and external mass transfer limitations. Using one-factor-at-a-time variables method, maximum oleic acid conversion and GDO selectivity were achieved at 85% and 74% respectively, at 0.15 g of lipase, 77 min of residence time with 1.6:1 molar ratio of oleic acid/glycerol. Hydrodynamic studies showed that the esterification reaction is kinetically controlled and unaffected by external and internal mass transfer. Employing Lilly–Hornby model for kinetic evaluation, K m values increased with increasing flow rates, whereas, V max appeared to be flow rate independent. Reusability tests revealed that the activity of immobilized lipase remained the same after 9 successive reaction cycles. At 11 days of operation, the stability of the lipase in the continuous packed bed millireactor decreased only 5–7%, indicating satisfying operational results and recyclability. This work may promote the enzymatic engineering synthesis of DAG, facilitating the creation of a cleaner and safer process. It has the potential to broaden the application of enzymes in continuous flow micro or millireactors. Article in Journal/Newspaper antartic* Lancaster University: Lancaster Eprints Journal of Cleaner Production 373 133816
institution Open Polar
collection Lancaster University: Lancaster Eprints
op_collection_id ftulancaster
language unknown
description Diacylglycerols (DAG) have been widely used in many industries due to their remarkable capabilities as emulsifiers and stabilisers. However, developing a sustainable and an effective synthesis method for DAG remains a challenge. Continuous flow bio-reactor is recognized to be more productive, controllable, and reliable instrument for developing green and intensified processes. In this work, a continuous flow packed bed millireactor was employed for the synthesis of glycerol dioelate (GDO) catalyzed by immobilized lipase namely Candida antartica. Experiments were carried out to evaluate the kinetic parameters as well as to assess the internal and external mass transfer limitations. Using one-factor-at-a-time variables method, maximum oleic acid conversion and GDO selectivity were achieved at 85% and 74% respectively, at 0.15 g of lipase, 77 min of residence time with 1.6:1 molar ratio of oleic acid/glycerol. Hydrodynamic studies showed that the esterification reaction is kinetically controlled and unaffected by external and internal mass transfer. Employing Lilly–Hornby model for kinetic evaluation, K m values increased with increasing flow rates, whereas, V max appeared to be flow rate independent. Reusability tests revealed that the activity of immobilized lipase remained the same after 9 successive reaction cycles. At 11 days of operation, the stability of the lipase in the continuous packed bed millireactor decreased only 5–7%, indicating satisfying operational results and recyclability. This work may promote the enzymatic engineering synthesis of DAG, facilitating the creation of a cleaner and safer process. It has the potential to broaden the application of enzymes in continuous flow micro or millireactors.
format Article in Journal/Newspaper
author Abd Razak, Nurul Nadiah
Cognet, Patrick
Pérès, Yolande
Gew, Lai Ti
Aroua, Mohamed Kheireddine
spellingShingle Abd Razak, Nurul Nadiah
Cognet, Patrick
Pérès, Yolande
Gew, Lai Ti
Aroua, Mohamed Kheireddine
Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor
author_facet Abd Razak, Nurul Nadiah
Cognet, Patrick
Pérès, Yolande
Gew, Lai Ti
Aroua, Mohamed Kheireddine
author_sort Abd Razak, Nurul Nadiah
title Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor
title_short Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor
title_full Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor
title_fullStr Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor
title_full_unstemmed Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor
title_sort kinetics and hydrodynamics of candida antartica lipase-catalyzed synthesis of glycerol dioleate (gdo) in a continuous flow packed-bed millireactor
publishDate 2022
url https://eprints.lancs.ac.uk/id/eprint/190082/
https://doi.org/10.1016/j.jclepro.2022.133816
genre antartic*
genre_facet antartic*
op_relation Abd Razak, Nurul Nadiah and Cognet, Patrick and Pérès, Yolande and Gew, Lai Ti and Aroua, Mohamed Kheireddine (2022) Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor. Journal of Cleaner Production, 373. ISSN 0959-6526
op_doi https://doi.org/10.1016/j.jclepro.2022.133816
container_title Journal of Cleaner Production
container_volume 373
container_start_page 133816
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