Modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents

The biosynthesis of sugar esters, molecules with biosurfactant properties, can occur through the esterification of sugars with fatty acids by enzymatic catalysis. An alternative to reduce the impact of raw materials on the final biosurfactant production cost and the reuse of industrial waste is to u...

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Main Authors: Cansian Ana Bárbara Moulin, Tardioli Paulo Waldir, Furlan Felipe Fernando, de Sousa Ruy Júnior
Format: Article
Language:English
Published: Association of the Chemical Engineers of Serbia 2022-01-01
Series:Chemical Industry and Chemical Engineering Quarterly
Subjects:
Online Access:http://www.doiserbia.nb.rs/img/doi/1451-9372/2022/1451-93722200001C.pdf
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author Cansian Ana Bárbara Moulin
Tardioli Paulo Waldir
Furlan Felipe Fernando
de Sousa Ruy Júnior
author_facet Cansian Ana Bárbara Moulin
Tardioli Paulo Waldir
Furlan Felipe Fernando
de Sousa Ruy Júnior
author_sort Cansian Ana Bárbara Moulin
collection DOAJ
description The biosynthesis of sugar esters, molecules with biosurfactant properties, can occur through the esterification of sugars with fatty acids by enzymatic catalysis. An alternative to reduce the impact of raw materials on the final biosurfactant production cost and the reuse of industrial waste is to use residues from vegetable oil industries as a source of free fatty acids, such as oleic acid, and lignocellulosic residues of 2G ethanol as a source of sugar (xylose). In this scenario, the present work aimed at modeling the biosurfactants production via heterogeneous biocatalysis using lipase, oleic acid, and xylose. Product separation and purification were performed using a sequence of precipitations (adding ethanol, water, and methyl ethyl ketone). The simulation was performed using the equation-oriented software EMSO (Environment for Modeling, Simulation, and Optimization), CAPE-OPEN compliant. The percentage of biosurfactants in the product was around 86%, with a recovery of 88% in the purification. Regarding the study of energy expenditure, a value of -604.1 kW of heat associated with cooling and a value of 137.6 kW associated with heating was observed. Developed mathematical models successfully described the process. The initial economic analysis of the process indicates a minimum biosurfactant selling price of US$ 72.37/kg.
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spelling doaj.art-1023ce4e781b4b86aa8f7b3f98fa5c022022-12-22T04:21:13ZengAssociation of the Chemical Engineers of SerbiaChemical Industry and Chemical Engineering Quarterly1451-93722217-74342022-01-0128426527610.2298/CICEQ210621001C1451-93722200001CModeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagentsCansian Ana Bárbara Moulin0Tardioli Paulo Waldir1Furlan Felipe Fernando2de Sousa Ruy Júnior3Federal University of São Carlos, Graduate Program in Chemical Engineering, São Carlos, BrasilFederal University of São Carlos, Graduate Program in Chemical Engineering, São Carlos, SP + Federal University of São Carlos, Department of Chemical Engineering, São Carlos, SP, BrasilFederal University of São Carlos, Department of Chemical Engineering, São Carlos, BrasilFederal University of São Carlos, Graduate Program in Chemical Engineering, São Carlos, Brasil + Federal University of São Carlos, Department of Chemical Engineering, São Carlos, BrasilThe biosynthesis of sugar esters, molecules with biosurfactant properties, can occur through the esterification of sugars with fatty acids by enzymatic catalysis. An alternative to reduce the impact of raw materials on the final biosurfactant production cost and the reuse of industrial waste is to use residues from vegetable oil industries as a source of free fatty acids, such as oleic acid, and lignocellulosic residues of 2G ethanol as a source of sugar (xylose). In this scenario, the present work aimed at modeling the biosurfactants production via heterogeneous biocatalysis using lipase, oleic acid, and xylose. Product separation and purification were performed using a sequence of precipitations (adding ethanol, water, and methyl ethyl ketone). The simulation was performed using the equation-oriented software EMSO (Environment for Modeling, Simulation, and Optimization), CAPE-OPEN compliant. The percentage of biosurfactants in the product was around 86%, with a recovery of 88% in the purification. Regarding the study of energy expenditure, a value of -604.1 kW of heat associated with cooling and a value of 137.6 kW associated with heating was observed. Developed mathematical models successfully described the process. The initial economic analysis of the process indicates a minimum biosurfactant selling price of US$ 72.37/kg.http://www.doiserbia.nb.rs/img/doi/1451-9372/2022/1451-93722200001C.pdfbiosurfactantsesterificationmodeling and simulationpurificationprecipitation
spellingShingle Cansian Ana Bárbara Moulin
Tardioli Paulo Waldir
Furlan Felipe Fernando
de Sousa Ruy Júnior
Modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents
Chemical Industry and Chemical Engineering Quarterly
biosurfactants
esterification
modeling and simulation
purification
precipitation
title Modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents
title_full Modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents
title_fullStr Modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents
title_full_unstemmed Modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents
title_short Modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents
title_sort modeling and simulation of the biosurfactant production by enzymatic route using xylose and oleic acid as reagents
topic biosurfactants
esterification
modeling and simulation
purification
precipitation
url http://www.doiserbia.nb.rs/img/doi/1451-9372/2022/1451-93722200001C.pdf
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AT tardiolipaulowaldir modelingandsimulationofthebiosurfactantproductionbyenzymaticrouteusingxyloseandoleicacidasreagents
AT furlanfelipefernando modelingandsimulationofthebiosurfactantproductionbyenzymaticrouteusingxyloseandoleicacidasreagents
AT desousaruyjunior modelingandsimulationofthebiosurfactantproductionbyenzymaticrouteusingxyloseandoleicacidasreagents