Abstract

The purpose of this work is to study the synthesis, characterization, and catalytic performance of two types of solid heteropoly acid catalysts, namely, silicotungstic acid bulk (STAB) and STA-silica sol-gel (STA-SG) compared with sulfuric acid. From the XPS analyses, there was a significant formation of W-O-Si, W-O-W, and Si-O-Si bonding in STA-SG compared to that in STAB. The main spectra of O1s (90.74%, 531.5 eV) followed by other O1s peak (9.26%, 532.8 eV) were due to the presence of W-O-W and W-O-Si bonds, respectively. The STA-SG catalyst was found to be the more environmentally benign solid acid catalyst for the esterification reaction between oleic acid and glycerol due to its lower toxicity supported by silica via sol-gel technique. In addition, the ease of separation for STA-SG catalyst was attributed to its insoluble state in the product phase. The esterification products were then analysed by FTIR and HPLC. Both the H2SO4and the STAB gave high conversion of 100% and 98% but at a lower selectivity of GME with 81.6% and 89.9%, respectively. On the contrary, the STA-SG enabled a conversion of 94% but with a significantly higher GME selectivity of 95%, rendering it the more efficient solid acid catalyst.

Highlights

  • IntroductionGlycerol has been used as combustion materials around the world

  • During the recent years, glycerol has been used as combustion materials around the world

  • It clearly demonstrated that Si-O-Si bend with higher composition in STA-SG affected Si and O from TEOS and that silicotungstic acid bulk (STAB) was chemically bonded with each other

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Summary

Introduction

Glycerol has been used as combustion materials around the world. The GME is synthesized at present by acid catalyzed esterification of glycerol and fatty acids [2, 3]. List of studies involving alternative heterogeneous catalytic routes have been reported such as the glycerol esterification with lauric acid (LA) and oleic acid (OA) by using functionalized mesoporous materials [4], zeolitic molecular sieves [5, 6], and solid cationic resins [7, 8] as catalysts. The beta-zeolite catalyst gave the conversion of fatty acids above 20% at optimum condition of glycerol : LA molar ratio of 1 : 1 at 100◦C for 24 hours [9]

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