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Synthesis of Methyl Palmitate Catalyzed by Solid Acid Zr(SO_4)_2/TiO_2

Hao Xiang-ying

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Abstract

The biodiesel was synthesized by industrial palmitic acid and methanol,using solid acid Zr(SO4)2/TiO2 as catalyst.Effects of the mass fraction of Zr(SO4)2 in the catalyst,calcination temperature and time of catalyst,mass ratio of methanol to industrial palmitic acid,catalyst dosage and reaction time on the esterification rate were investigated.The catalyst and ester product were analysed by GC-MS,FTIR and DTG/DTA methods.Assessment experiments show that the catalytic activity of the supported Zr(SO4)2/TiO2 catalyst was higher than that of the unsupported Zr(SO4)2 catalyst.The esterification rate can reach 98.9% under the following conditions: calcination temperature of catalyst 400 ℃,loading amount of Zr(SO4)2(based on total mass of catalyst) 65%,mass ratio of methanol to industrial palmitic acid 12∶25,mass fraction of Zr(SO4)2/TiO2 in palmitic acid 8.0% and reaction time 5 h.The analysis result of GC-MS showed that the ester products were mainly hexadecanoic acid methyl ester and 10-octadecenoic acid methyl ester.

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What this paper is about

The biodiesel was synthesized by industrial palmitic acid and methanol,using solid acid Zr(SO4)2/TiO2 as catalyst.Effects of the mass fraction of Zr(SO4)2 in the catalyst,calcination temperature and time of catalyst,mass ratio of methanol to industrial palmitic acid,catalyst dosage and reaction time on the esterification rate were investigated.The catalyst and ester product were analysed by GC-MS,FTIR and DTG/DTA methods.Assessment experiments show that the catalytic activity of the supported Zr(SO4)2/TiO2 catalyst was higher than that of the unsupported Zr(SO4)2 catalyst.The esterification rate can reach 98.9% under the following conditions: calcination temperature of catalyst 400 ℃,loading amount of Zr(SO4)2(based on total mass of catalyst) 65%,mass ratio of methanol to industrial palmitic acid 12∶25,mass fraction of Zr(SO4)2/TiO2 in palmitic acid 8.0% and reaction time 5 h.The analysis result of GC-MS showed that the ester products were mainly hexadecanoic acid methyl ester and 10-octadecenoic acid methyl ester.

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Available abstract

The biodiesel was synthesized by industrial palmitic acid and methanol,using solid acid Zr(SO4)2/TiO2 as catalyst.Effects of the mass fraction of Zr(SO4)2 in the catalyst,calcination temperature and time of catalyst,mass ratio of methanol to industrial palmitic acid,catalyst dosage and reaction time on the esterification rate were investigated.The catalyst and ester product were analysed by GC-MS,FTIR and DTG/DTA methods.Assessment experiments show that the catalytic activity of the supported Zr(SO4)2/TiO2 catalyst was higher than that of the unsupported Zr(SO4)2 catalyst.The esterification rate can reach 98.9% under the following conditions: calcination temperature of catalyst 400 ℃,loading amount of Zr(SO4)2(based on total mass of catalyst) 65%,mass ratio of methanol to industrial palmitic acid 12∶25,mass fraction of Zr(SO4)2/TiO2 in palmitic acid 8.0% and reaction time 5 h.The analysis result of GC-MS showed that the ester products were mainly hexadecanoic acid methyl ester and 10-octadecenoic acid methyl ester.

Key concepts: Catalysis, Palmitic acid, Methanol, Calcination, Chemistry, Mass fraction, Nuclear chemistry, Biodiesel

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