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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Main Authors: Nurul Nadiah, Abd Razak, Cognet, Patrick, Peres, Yolande, Gew, Lai Ti *, Aroua, Mohamed Kheireddine *
Format: Article
Published: Elsevier 2022
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Online Access:http://eprints.sunway.edu.my/2945/
https://www.sciencedirect.com/science/article/abs/pii/S0959652622033923
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spelling my.sunway.eprints.29452024-08-02T06:09:47Z http://eprints.sunway.edu.my/2945/ Kinetics and hydrodynamics of Candida antartica lipase-catalyzed synthesis of glycerol dioleate (GDO) in a continuous flow packed-bed millireactor Nurul Nadiah, Abd Razak Cognet, Patrick Peres, Yolande Gew, Lai Ti * Aroua, Mohamed Kheireddine * QL Zoology QP Physiology TD Environmental technology. Sanitary engineering 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, Km values increased with increasing flow rates, whereas, Vmax 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. Elsevier 2022 Article PeerReviewed Nurul Nadiah, Abd Razak and Cognet, Patrick and Peres, 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 (3). ISSN 0959-6526 https://www.sciencedirect.com/science/article/abs/pii/S0959652622033923 10.1016/j.jclepro.2022.133816
institution Sunway University
building Sunway Campus Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Sunway University
content_source Sunway Institutional Repository
url_provider http://eprints.sunway.edu.my/
topic QL Zoology
QP Physiology
TD Environmental technology. Sanitary engineering
spellingShingle QL Zoology
QP Physiology
TD Environmental technology. Sanitary engineering
Nurul Nadiah, Abd Razak
Cognet, Patrick
Peres, 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
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, Km values increased with increasing flow rates, whereas, Vmax 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
author Nurul Nadiah, Abd Razak
Cognet, Patrick
Peres, Yolande
Gew, Lai Ti *
Aroua, Mohamed Kheireddine *
author_facet Nurul Nadiah, Abd Razak
Cognet, Patrick
Peres, Yolande
Gew, Lai Ti *
Aroua, Mohamed Kheireddine *
author_sort Nurul Nadiah, Abd Razak
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
publisher Elsevier
publishDate 2022
url http://eprints.sunway.edu.my/2945/
https://www.sciencedirect.com/science/article/abs/pii/S0959652622033923
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