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ARTICLE
Preliminary Optimization and Kinetics of SnCl2-HCl Catalyzed Hydrothermal Conversion of Microcrystalline Cellulose to Levulinic Acid
Dexby de Guzman, Rizalinda de Leon*
Fuels, Energy and Thermal Systems Laboratory, Department of Chemical Engineering, University of the Philippines, Quezon City, 1101, Philippines
* Corresponding Author: Rizalinda de Leon. Email:
(This article belongs to the Special Issue: Renewable materials for sustainable development)
Journal of Renewable Materials 2021, 9(1), 145-162. https://doi.org/10.32604/jrm.2021.011646
Received 21 May 2020; Accepted 06 July 2020; Issue published 30 November 2020
Abstract
Levulinic acid (LA) is a platform biorefinery chemical from biomass which can be converted to green solvents, plasticizers, polymer precursors, bio-based cleaning agents, fuels and fuel additives. This study assessed the potential of SnCl
2-based mixed acid systems as catalyst in the hydrothermal conversion of microcrystalline cellulose to levulinic acid. Maximum LA yield of 36.2 mol% was achieved using 0.2 M SnCl
2 concentration at test conditions of 3 h, 180°C and 1% w/v cellulose loading. To reduce precipitate formation and further improve LA yield, the strategy employed was to combine SnCl
2 (a Lewis acid) with conventional mineral acids (Bronsted acids). Evaluation of the catalytic performance of SnCl
2-HCl, SnCl
2-H
2SO
4, SnCl
2-HNO
3, and SnCl
2-H
3PO
4 (1:1 molar ratio, 0.2 M total acid concentration) were done with highest LA yield of 47.0 mol% obtained using the SnCl
2-HCl system at same test conditions. Response surface methodology optimization employing Box-Behnken design generated a quadratic model with a high coefficient of determination (r
2) of 0.964. A maximum LA yield of 63.5 mol% can be achieved at 0.17 M catalyst concentration, 198°C, and 5.15 h reaction time. Rate constants were estimated using nonlinear regression, while activation energies were determined using Arrhenius equation. Cellulose hydrolysis was determined to be the rate-limiting step in the overall process. Low activation energy of 63.3 kJ/mol for glucose dehydration to hydroxymethylfurfural supports the action of SnCl
2 as Lewis acid in the mixed-acid system. LA yield simulations for plug flow reactor (PFR) and continuous stirred tank reactor (CSTR) were done suggesting a similar PFR-CSTR configuration with the established Biofine process. Lastly, a reaction scheme was presented to explain the synergy between SnCl
2 and HCl in LA production from cellulose.
Keywords
Cite This Article
APA Style
Guzman, D.D., Leon, R.D. (2021). Preliminary optimization and kinetics of sncl<sub>2</sub>-hcl catalyzed hydrothermal conversion of microcrystalline cellulose to levulinic acid. Journal of Renewable Materials, 9(1), 145-162. https://doi.org/10.32604/jrm.2021.011646
Vancouver Style
Guzman DD, Leon RD. Preliminary optimization and kinetics of sncl<sub>2</sub>-hcl catalyzed hydrothermal conversion of microcrystalline cellulose to levulinic acid. J Renew Mater. 2021;9(1):145-162 https://doi.org/10.32604/jrm.2021.011646
IEEE Style
D.D. Guzman and R.D. Leon, "Preliminary Optimization and Kinetics of SnCl<sub>2</sub>-HCl Catalyzed Hydrothermal Conversion of Microcrystalline Cellulose to Levulinic Acid," J. Renew. Mater., vol. 9, no. 1, pp. 145-162. 2021. https://doi.org/10.32604/jrm.2021.011646
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