Fatty Acid Epoxidation on Enzymes: Experimental Study and Modeling of Batch and Semibatch Operation

Biolubricants, plasticizers, bio-based rigid foams, and non-isocyanate polyurethanes can be made in a green way from epoxidized fatty acids. The classical technology for fatty acid epoxidation requires a reaction carrier, which acts as the real epoxidation agent. The process is complicated and invol...

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Veröffentlicht in:Industrial & engineering chemistry research 2023-06, Vol.62 (23), p.9169-9187
Hauptverfasser: Wikström, Wilhelm, Freites Aguilera, Adriana, Tolvanen, Pasi, Lassfolk, Robert, Medina, Ananias, Eränen, Kari, Salmi, Tapio
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container_end_page 9187
container_issue 23
container_start_page 9169
container_title Industrial & engineering chemistry research
container_volume 62
creator Wikström, Wilhelm
Freites Aguilera, Adriana
Tolvanen, Pasi
Lassfolk, Robert
Medina, Ananias
Eränen, Kari
Salmi, Tapio
description Biolubricants, plasticizers, bio-based rigid foams, and non-isocyanate polyurethanes can be made in a green way from epoxidized fatty acids. The classical technology for fatty acid epoxidation requires a reaction carrier, which acts as the real epoxidation agent. The process is complicated and involves a safety risk because of the appearance of percarboxylic acids. Therefore, the direct epoxidation of fatty acids in the presence of an immobilized enzyme is an attractive pathway to epoxidized fatty acids. Oleic acid was used as the model compound is this work, and commercial immobilized lipase Novozym 435 was used as the catalyst and hydrogen peroxide as the epoxidation agent. Batch and semibatch operation modes were tested in a laboratory-scale stirred tank reactor. The experimental results showed that almost complete conversions of the double bonds in oleic acid were achievable under isothermal batch and semibatch operation, with low concentrations of ring-opening byproducts. Semibatch operation gave an improvement of the product yield. Mathematical modeling of the experimental data was based on the reaction stoichiometry OA + HP → POA + W and OA + POA → EOA + OA, where OA = oleic acid, HP = hydrogen peroxide, POA = peroleic acid, W = water, and EOA = epoxized OA. Rate equations for the formation of peroleic acid and epoxide were derived, and the numerical values of the kinetic and adsorption parameters were estimated with nonlinear regression analysis. The reactor models consisted of ordinary differential equations, which were solved numerically during the parameter estimation until the optimal parameter values were reached. The model gave a very good description of the experimental data.
doi_str_mv 10.1021/acs.iecr.3c00890
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title Fatty Acid Epoxidation on Enzymes: Experimental Study and Modeling of Batch and Semibatch Operation
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