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Statistical Optimization and Kinetic Modeling of Lipase-Catalyzed Synthesis of Diacylglycerol in the Mixed Solvent System of Acetone/ tert-Butanol

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Statistical Optimization and Kinetic Modeling of Lipase-Catalyzed Synthesis of Diacylglycerol in the Mixed Solvent System of Acetone/ tert-Butanol. / Abd Razak, N.N.; Gew, L.T.; Pérès, Y. et al.
In: Industrial and Engineering Chemistry Research, Vol. 60, No. 39, 06.10.2021, p. 14026-14037.

Research output: Contribution to Journal/MagazineJournal articlepeer-review

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Abd Razak, NN, Gew, LT, Pérès, Y, Cognet, P & Aroua, MK 2021, 'Statistical Optimization and Kinetic Modeling of Lipase-Catalyzed Synthesis of Diacylglycerol in the Mixed Solvent System of Acetone/ tert-Butanol', Industrial and Engineering Chemistry Research, vol. 60, no. 39, pp. 14026-14037. https://doi.org/10.1021/acs.iecr.1c01906

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Vancouver

Abd Razak NN, Gew LT, Pérès Y, Cognet P, Aroua MK. Statistical Optimization and Kinetic Modeling of Lipase-Catalyzed Synthesis of Diacylglycerol in the Mixed Solvent System of Acetone/ tert-Butanol. Industrial and Engineering Chemistry Research. 2021 Oct 6;60(39):14026-14037. Epub 2021 Sept 21. doi: 10.1021/acs.iecr.1c01906

Author

Abd Razak, N.N. ; Gew, L.T. ; Pérès, Y. et al. / Statistical Optimization and Kinetic Modeling of Lipase-Catalyzed Synthesis of Diacylglycerol in the Mixed Solvent System of Acetone/ tert-Butanol. In: Industrial and Engineering Chemistry Research. 2021 ; Vol. 60, No. 39. pp. 14026-14037.

Bibtex

@article{54f95e01a2e14315b7143e148ca9093e,
title = "Statistical Optimization and Kinetic Modeling of Lipase-Catalyzed Synthesis of Diacylglycerol in the Mixed Solvent System of Acetone/ tert-Butanol",
abstract = "Diacylglycerols have been extensively used in food, medicine, cosmetic, and pharmaceutical industries due to their outstanding properties as emulsifiers and stabilizers as well as their nutritional benefits to humans. This study investigated the optimization and kinetics of lipase-catalyzed synthesis of glycerol dioleates (GDO) through esterification of glycerol with oleic acid in a mixed solvent system of acetone/tert-butanol. Process variables, namely, solvent ratio, temperature, and enzyme loading, were optimized to acquire maximum conversion and selectivity. A high oleic acid conversion of 73% and GDO selectivity of 77% were obtained in an acetone/tert-butanol 70:30 (v/v) mixture at 45 °C and an enzyme load of 0.15 g. The bi substrates Ping-Pong Bi-Bi kinetic model was employed for initial rate determination, which was fitted to the experimental results. At an applied temperature of 45 °C, the Ping-Pong Bi-Bi model with no substrate inhibition gives the best fit with parameter values of Vmax = 1.21 M h–1, Km[G] = 1.81 M, and Km[OA] = 6.81 M for glycerol and oleic acid concentrations between 0.31 to 1.32 M and 1.88 to 2.13 M, respectively.",
author = "{Abd Razak}, N.N. and L.T. Gew and Y. P{\'e}r{\`e}s and P. Cognet and M.K. Aroua",
year = "2021",
month = oct,
day = "6",
doi = "10.1021/acs.iecr.1c01906",
language = "English",
volume = "60",
pages = "14026--14037",
journal = "Industrial and Engineering Chemistry Research",
issn = "0888-5885",
publisher = "American Chemical Society",
number = "39",

}

RIS

TY - JOUR

T1 - Statistical Optimization and Kinetic Modeling of Lipase-Catalyzed Synthesis of Diacylglycerol in the Mixed Solvent System of Acetone/ tert-Butanol

AU - Abd Razak, N.N.

AU - Gew, L.T.

AU - Pérès, Y.

AU - Cognet, P.

AU - Aroua, M.K.

PY - 2021/10/6

Y1 - 2021/10/6

N2 - Diacylglycerols have been extensively used in food, medicine, cosmetic, and pharmaceutical industries due to their outstanding properties as emulsifiers and stabilizers as well as their nutritional benefits to humans. This study investigated the optimization and kinetics of lipase-catalyzed synthesis of glycerol dioleates (GDO) through esterification of glycerol with oleic acid in a mixed solvent system of acetone/tert-butanol. Process variables, namely, solvent ratio, temperature, and enzyme loading, were optimized to acquire maximum conversion and selectivity. A high oleic acid conversion of 73% and GDO selectivity of 77% were obtained in an acetone/tert-butanol 70:30 (v/v) mixture at 45 °C and an enzyme load of 0.15 g. The bi substrates Ping-Pong Bi-Bi kinetic model was employed for initial rate determination, which was fitted to the experimental results. At an applied temperature of 45 °C, the Ping-Pong Bi-Bi model with no substrate inhibition gives the best fit with parameter values of Vmax = 1.21 M h–1, Km[G] = 1.81 M, and Km[OA] = 6.81 M for glycerol and oleic acid concentrations between 0.31 to 1.32 M and 1.88 to 2.13 M, respectively.

AB - Diacylglycerols have been extensively used in food, medicine, cosmetic, and pharmaceutical industries due to their outstanding properties as emulsifiers and stabilizers as well as their nutritional benefits to humans. This study investigated the optimization and kinetics of lipase-catalyzed synthesis of glycerol dioleates (GDO) through esterification of glycerol with oleic acid in a mixed solvent system of acetone/tert-butanol. Process variables, namely, solvent ratio, temperature, and enzyme loading, were optimized to acquire maximum conversion and selectivity. A high oleic acid conversion of 73% and GDO selectivity of 77% were obtained in an acetone/tert-butanol 70:30 (v/v) mixture at 45 °C and an enzyme load of 0.15 g. The bi substrates Ping-Pong Bi-Bi kinetic model was employed for initial rate determination, which was fitted to the experimental results. At an applied temperature of 45 °C, the Ping-Pong Bi-Bi model with no substrate inhibition gives the best fit with parameter values of Vmax = 1.21 M h–1, Km[G] = 1.81 M, and Km[OA] = 6.81 M for glycerol and oleic acid concentrations between 0.31 to 1.32 M and 1.88 to 2.13 M, respectively.

U2 - 10.1021/acs.iecr.1c01906

DO - 10.1021/acs.iecr.1c01906

M3 - Journal article

VL - 60

SP - 14026

EP - 14037

JO - Industrial and Engineering Chemistry Research

JF - Industrial and Engineering Chemistry Research

SN - 0888-5885

IS - 39

ER -