Easy and Fast Production of Solketal from Glycerol Acetalization via Heteropolyacids

This work presents an effective and fast procedure to valorize the main waste produced from the biodiesel industry, i.e., the glycerol. The acetalization of glycerol with acetone represents an effective strategy to produce the valuable solketal, a fuel additive component. In this work, the catalytic...

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Main Authors: Diana Julião, Fatima Mirante, Salete S. Balula
Format: Article
Language:English
Published: MDPI AG 2022-10-01
Series:Molecules
Subjects:
Online Access:https://www.mdpi.com/1420-3049/27/19/6573
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author Diana Julião
Fatima Mirante
Salete S. Balula
author_facet Diana Julião
Fatima Mirante
Salete S. Balula
author_sort Diana Julião
collection DOAJ
description This work presents an effective and fast procedure to valorize the main waste produced from the biodiesel industry, i.e., the glycerol. The acetalization of glycerol with acetone represents an effective strategy to produce the valuable solketal, a fuel additive component. In this work, the catalytic efficiency of different commercial heteropolyacids (HPAas) was compared under a solvent-free system. The HPAs used were H<sub>3</sub>[PW<sub>12</sub>O<sub>40</sub>] (PW<sub>12</sub>), H<sub>3</sub>[PMo<sub>12</sub>O<sub>40</sub>] (PMo<sub>12</sub>) and H<sub>4</sub>[SiW<sub>12</sub>O<sub>40</sub>] (SiW<sub>12</sub>). The influence of reactional parameters such as reactants stoichiometry, catalyst concentration and reaction temperature were investigated in order to optimize experimental conditions to increase cost-efficiency and sustainability. HPAs demonstrated to be highly efficient for this type of reaction, presenting a high and fast glycerol conversion, with high selectivity to solketal under sustainable conditions (solvent-free system and room temperature medium). The activity of HPAs using 3% to glycerol weight and a glycerol/acetone ratio of 1:15 followed the order: PW<sub>12</sub> (99.2%) > PMo<sub>12</sub> (91.4%) > SiW<sub>12</sub> (90.7%) as a result of the strong acidic sites after 5 min. In fact, only 5 min of reaction were needed to achieve 97% of solketal product in the presence of the PW<sub>12</sub> as a catalyst. This last system presents an effective, selective and sustainable catalytic system to valorize glycerol.
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spelling doaj.art-adf1e7fc44e84eb58f1459612a0c365f2023-11-23T21:13:38ZengMDPI AGMolecules1420-30492022-10-012719657310.3390/molecules27196573Easy and Fast Production of Solketal from Glycerol Acetalization via HeteropolyacidsDiana Julião0Fatima Mirante1Salete S. Balula2LAQV/REQUIMTE & Department of Chemistry and Biochemistry, Faculty of Sciences, University of Porto, 4169-007 Porto, PortugalLAQV/REQUIMTE & Department of Chemistry and Biochemistry, Faculty of Sciences, University of Porto, 4169-007 Porto, PortugalLAQV/REQUIMTE & Department of Chemistry and Biochemistry, Faculty of Sciences, University of Porto, 4169-007 Porto, PortugalThis work presents an effective and fast procedure to valorize the main waste produced from the biodiesel industry, i.e., the glycerol. The acetalization of glycerol with acetone represents an effective strategy to produce the valuable solketal, a fuel additive component. In this work, the catalytic efficiency of different commercial heteropolyacids (HPAas) was compared under a solvent-free system. The HPAs used were H<sub>3</sub>[PW<sub>12</sub>O<sub>40</sub>] (PW<sub>12</sub>), H<sub>3</sub>[PMo<sub>12</sub>O<sub>40</sub>] (PMo<sub>12</sub>) and H<sub>4</sub>[SiW<sub>12</sub>O<sub>40</sub>] (SiW<sub>12</sub>). The influence of reactional parameters such as reactants stoichiometry, catalyst concentration and reaction temperature were investigated in order to optimize experimental conditions to increase cost-efficiency and sustainability. HPAs demonstrated to be highly efficient for this type of reaction, presenting a high and fast glycerol conversion, with high selectivity to solketal under sustainable conditions (solvent-free system and room temperature medium). The activity of HPAs using 3% to glycerol weight and a glycerol/acetone ratio of 1:15 followed the order: PW<sub>12</sub> (99.2%) > PMo<sub>12</sub> (91.4%) > SiW<sub>12</sub> (90.7%) as a result of the strong acidic sites after 5 min. In fact, only 5 min of reaction were needed to achieve 97% of solketal product in the presence of the PW<sub>12</sub> as a catalyst. This last system presents an effective, selective and sustainable catalytic system to valorize glycerol.https://www.mdpi.com/1420-3049/27/19/6573glycerolacetalizationsolketalheteropoly acids
spellingShingle Diana Julião
Fatima Mirante
Salete S. Balula
Easy and Fast Production of Solketal from Glycerol Acetalization via Heteropolyacids
Molecules
glycerol
acetalization
solketal
heteropoly acids
title Easy and Fast Production of Solketal from Glycerol Acetalization via Heteropolyacids
title_full Easy and Fast Production of Solketal from Glycerol Acetalization via Heteropolyacids
title_fullStr Easy and Fast Production of Solketal from Glycerol Acetalization via Heteropolyacids
title_full_unstemmed Easy and Fast Production of Solketal from Glycerol Acetalization via Heteropolyacids
title_short Easy and Fast Production of Solketal from Glycerol Acetalization via Heteropolyacids
title_sort easy and fast production of solketal from glycerol acetalization via heteropolyacids
topic glycerol
acetalization
solketal
heteropoly acids
url https://www.mdpi.com/1420-3049/27/19/6573
work_keys_str_mv AT dianajuliao easyandfastproductionofsolketalfromglycerolacetalizationviaheteropolyacids
AT fatimamirante easyandfastproductionofsolketalfromglycerolacetalizationviaheteropolyacids
AT saletesbalula easyandfastproductionofsolketalfromglycerolacetalizationviaheteropolyacids