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A new kinetic model for simultaneous interesterification and esterification reactions from methyl acetate and highly acidic oil

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  • Brondani, L.N.
  • Ribeiro, J.S.
  • Castilhos, F.

Abstract

This work presents the development of a kinetic model for simultaneous reactions of esterification and interesterification from macaw oil and methyl acetate using γ-alumina as the heterogeneous catalyst. Experimental data varied between 225 °C and 300 °C, catalyst concentration of 2 wt%, 5 wt%, and 10 wt% and molar ratio (methyl acetate: Oil) of 10:1, 20:1 and 40:1. Arrhenius kinetic parameters were concomitantly estimated for all experimental conditions by minimizing the objective using a hybrid optimization algorithm. From the results, it could be verified that γ-alumina is an active catalyst for both interesterification and esterification reactions with MeA and a high acid glyceride source. The simultaneous reaction system indicated an endothermic character at experimental conditions investigated. The FAME conversions presented a strong limitation of chemical equilibrium. Moreover, it could be verified that the esterification reaction produces about 80% of total fatty acid methyl esters and that acetic acid played the main role as a reagent through reactions with glycerine acetates and not as a catalyst. The proposed kinetic model satisfactorily fitted the experimental results.

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  • Brondani, L.N. & Ribeiro, J.S. & Castilhos, F., 2020. "A new kinetic model for simultaneous interesterification and esterification reactions from methyl acetate and highly acidic oil," Renewable Energy, Elsevier, vol. 156(C), pages 579-590.
    • Handle: RePEc:eee:renene:v:156:y:2020:i:c:p:579-590
    DOI: 10.1016/j.renene.2020.04.063
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    References listed on IDEAS

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    1. Sajjadi, Baharak & Raman, Abdul Aziz Abdul & Arandiyan, Hamidreza, 2016. "A comprehensive review on properties of edible and non-edible vegetable oil-based biodiesel: Composition, specifications and prediction models," Renewable and Sustainable Energy Reviews, Elsevier, vol. 63(C), pages 62-92.
    2. Lopes, Daniela de Carvalho & Steidle Neto, Antonio José & Mendes, Adriano Aguiar & Pereira, Débora Tamires Vítor, 2013. "Economic feasibility of biodiesel production from Macauba in Brazil," Energy Economics, Elsevier, vol. 40(C), pages 819-824.
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    5. Simões, S.S. & Ribeiro, J.S. & Celante, D. & Brondani, L.N. & Castilhos, F., 2020. "Heterogeneous catalyst screening for fatty acid methyl esters production through interesterification reaction," Renewable Energy, Elsevier, vol. 146(C), pages 719-726.
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    1. Abraham Casas & Ángel Pérez & María Jesús Ramos, 2021. "Purification of Methyl Acetate/Water Mixtures from Chemical Interesterification of Vegetable Oils by Pervaporation," Energies, MDPI, vol. 14(3), pages 1-10, February.
    2. Wong, Wan-Ying & Lim, Steven & Pang, Yean-Ling & Shuit, Siew-Hoong & Lam, Man-Kee & Tan, Inn-Shi & Chen, Wei-Hsin, 2023. "A comprehensive review of the production methods and effect of parameters for glycerol-free biodiesel production," Renewable and Sustainable Energy Reviews, Elsevier, vol. 182(C).

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