Glycerol Carbonate Production via Transesterification: The Effect of Support Porosity and Catalyst Basicity

Glycerol transesterification with diethyl carbonate (DEC) using catalysts with different porosities as support for CaO was performed, seeking the evaluation of how textural properties influence glycerol conversion and product selectivity. A total of 20% CaO was supported on ZSM-5, K-10, MCM-41, SiO2, and γ-Al2O3. Catalysts showed a well-dispersed active phase of CaO in all the supports and no changes in the support crystalline structure were noticed. Reactions were performed in dimethyl sulfoxide (DMSO), 10 wt.% of catalyst in relation to glycerol, at 130 °C, and 1:3 glycerol/DEC molar ratio. According to our results, the higher the pore volume and pore size, the higher the glycerol conversion. On the other hand, concerning selectivity, higher glycerol carbonate selectivities were reached when strong basic sites were present. A total of 86% glycerol conversion and 91% glycerol carbonate selectivity were found using 60% CaO supported on γ-Al2O3 after 5 h of reaction.

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Publication Details

Journal
Processes
Published
2024-10-16
DOI
https://doi.org/10.3390/pr12102256
Citations
6
Primary Topic
Carbon dioxide utilization in catalysis
Type
article
Field-Weighted Citation Impact
1.07

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article

Glycerol Carbonate Production via Transesterification: The Effect of Support Porosity and Catalyst Basicity

Ricardo L. Souza Júnior, Chaline Detoni, Mariana M.V.M. Souza, Larissa C. Eira
6 citations
Processes
Carbon dioxide utilization in catalysis
1.07
article

Glycerol Carbonate Production via Transesterification: The Effect of Support Porosity and Catalyst Basicity

Ricardo L. Souza Júnior, Chaline Detoni, Mariana M.V.M. Souza, Larissa C. Eira
article en
6 citations

Abstract

Glycerol transesterification with diethyl carbonate (DEC) using catalysts with different porosities as support for CaO was performed, seeking the evaluation of how textural properties influence glycerol conversion and product selectivity. A total of 20% CaO was supported on ZSM-5, K-10, MCM-41, SiO2, and γ-Al2O3. Catalysts showed a well-dispersed active phase of CaO in all the supports and no changes in the support crystalline structure were noticed. Reactions were performed in dimethyl sulfoxide (DMSO), 10 wt.% of catalyst in relation to glycerol, at 130 °C, and 1:3 glycerol/DEC molar ratio. According to our results, the higher the pore volume and pore size, the higher the glycerol conversion. On the other hand, concerning selectivity, higher glycerol carbonate selectivities were reached when strong basic sites were present. A total of 86% glycerol conversion and 91% glycerol carbonate selectivity were found using 60% CaO supported on γ-Al2O3 after 5 h of reaction.

ProcessesVol. 12(10)
Universidade Federal do Rio de Janeiro (BR)
Coordenação de Aperfeiçoamento de Pessoal de Nível Superior, Conselho Nacional de Desenvolvimento Científico e Tecnológico, Fundação Carlos Chagas Filho de Amparo à Pesquisa do Estado do Rio de Janeiro, Universidade Federal do Rio de Janeiro
Responsible consumption and production
Openalex Percentile: Top 29%
Carbon dioxide utilization in catalysis
1.07
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Glycerol Carbonate Production via Transesterification: The Effect of Support Porosity and Catalyst Basicity — Ricardo L. Souza Júnior, Chaline Detoni, et al. · Processes (2024) | TGRS Research Map | TGRS