Glycerol acetylation into acetins over SnO2-based bimetallic oxide catalyst
Tin oxide-based bimetallic oxide catalysts, MOx (MOx = Al2O3, TiO2, Y2O3) with a molar ratio of MOx:SnO2 of 1:1 was prepared by the solid-state method. X-ray diffraction (XRD) analysis showed that tin oxide, SnO2, was present in all samples as a cassiterite phase with a tetragonal structure. The pr...
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| Main Authors: | , , , , , |
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| Format: | Article |
| Language: | English |
| Published: |
Malaysian Analytical Sciences Society
2024
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| Online Access: | http://psasir.upm.edu.my/id/eprint/112007/1/3_Glycerol%20acetylation%20into%20acetins.pdf http://psasir.upm.edu.my/id/eprint/112007/ https://mjas.analis.com.my/mjas/v28_n3/pdf/Azami_28_3_8.pdf |
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| Summary: | Tin oxide-based bimetallic oxide catalysts, MOx (MOx = Al2O3, TiO2, Y2O3) with a molar ratio of MOx:SnO2 of 1:1 was prepared
by the solid-state method. X-ray diffraction (XRD) analysis showed that tin oxide, SnO2, was present in all samples as a cassiterite phase with a tetragonal structure. The presence of other oxides, aluminum oxide (Al2O3), titanium oxide (TiO2), yttrium oxide (Y2O3) in the respective Al2O3/SnO2, TiO2/SnO2, Y2O3/SnO2 were also identified and confirmed by X-ray fluorescence (XRF) analysis. A small exothermic peak at 480 °C and 750 °C in the differential thermal gravimetric (DTG) analysis revealed the oxidation of sub-oxide defects, took place which are very common in SnO2-based samples. Further Fourier transform infrared spectroscopy (FTIR) analysis indicated the presence of Sn-O bonds, reflecting the abundance of tin-oxygen bonds in the materials. Acidity measurements by titration showed that both TiO2/ SnO2 and Y2O3/SnO2 have the same acidity value of 0.23 mmol/g whereas Al2O3/SnO2 and monoxide SnO2 at 0.20 mmol/g. These catalysts were tested for the acetylation of glycerol to monoacetin (MA), diacetin (DA) and triacetin (TA) in a batch reactor at a molar ratio of glycerol: acetic acid of 1:6 w/v, a temperature of 100°C, a reaction time of 2 h and a catalyst loading of 0.5 g. The tests showed complete conversion of glycerol by all catalysts, with the selective product being mainly MA, which was 64%, 62%, 57% and 43% for Al2O3/SnO2, Y2O3/SnO2, SnO2 and TiO2/SnO2, respectively. The percentage selectivity of the more valuable products, DA + TA, was produced in the following order, TiO2/SnO2 > SnO2 > Y2O3/SnO2 > Al2O3/SnO2 with 57%, 43%, 37%, and 35%, respectively. Further analysis of TiO2/SnO2 revealed that the
catalyst not only had a high acidity, but also an increased BET surface area of 9.8 m2/g compared to 8.6 m2/g for SnO2 when TiO2 was incorporated into SnO2. Analysis of the surface elements by energy dispersive X-ray spectroscopy (EDX) revealed a high surface oxygen content, which is consistent with the high acidity of the sample. |
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