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Production of Biodiesel by Esterification of Free Fatty Acid over Solid Catalyst from Biomass Waste

机译:通过生物质废物酯化在固体催化剂上的游离脂肪酸的生物柴油生产

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Recently,low cost feedstocks have been utilized to replace vegetable oils in order to improve the economic feasibility of biodiesel.The esterification of free fatty acid(FFA)on Palm Fatty Acid Distillate(PFAD)with methanol using solid catalyst generated from bagasse fly ash is a promising method to convert FFA into biodiesel.In this research,the esterification of FFA on PFAD using the sulfonated bagasse fly ash catalyst was studied.The performances of the catalysts were evaluated in terms of the reaction temperatures,the molar ratios of methanol to PFAD,and the catalyst loading.The effects of the mass ratio of catalyst to oil(1-10%),the molar ratio of methanol to oil(6:1-12:1),and the reaction temperature(40-60°C)were studied for the conversion of PFAD to optimize the reaction conditions.The results showed that the optimum conditions were methanol to PFAD molar ratio of 12:1,the amount of catalyst of 10%wt.of PFAD,and reaction temperature of 60°C.The reusability of the solid acid carbon catalysts was also studied in this work.The catalytic activity decreased up to 38% after third cycle.The significant decline in catalyst esterification activity was due to acid site leaching.The physico-characteristics and acid site densities were analyzed by Nitrogen gas adsorption,surface functional groups by Fourier transform infrared spectroscopy(FT-IR),elemental analysis using X-ray fluorescent(XRF),and acid-base back titration methods for determination of acid density.
机译:最近,低成本原料已被利用以提高植物油以提高生物柴油的经济可行性。使用从甘蔗渣产生的固体催化剂,用甲醇的棕榈脂肪酸馏分(PFAD)对游离脂肪酸(FFA)的酯化将FFA转化为生物柴油的有希望的方法。研究了使用磺化甘蔗粉粉催化剂对PFAD对PFAD的酯化。就反应温度评价催化剂的性能,甲醇对PFAD的摩尔比。和催化剂负载。催化剂与油(1-10%)的质量比的影响,甲醇与油的摩尔比(6:1-12:1)和反应温度(40-60℃研究了PFAD的转化为优化反应条件。结果表明,最佳条件为甲醇至PFAD摩尔比为12:1,催化剂的10%重量的催化剂,反应温度为60° C.固体酸性碳水化合物的可重用性在这项工作中也研究了N催化剂。第三个循环后催化活性降低至38%。催化剂酯化活性的显着下降是由于酸部位浸出。通过氮气吸附分析了物理特性和酸部位密度,表面官能团通过傅里叶变换红外光谱(FT-IR),使用X射线荧光(XRF)的元素分析,以及用于测定酸密度的酸碱后滴定方法。

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