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首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Kinetics of transesterification of palm oil and dimethyl carbonate for biodiesel production at the catalysis of heterogeneous base catalyst
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Kinetics of transesterification of palm oil and dimethyl carbonate for biodiesel production at the catalysis of heterogeneous base catalyst

机译:棕榈油和碳酸二甲酯在异质基础催化剂催化下用于生物柴油生产的酯交换动力学

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摘要

The transesterification of palm oil with dimethyl carbonate (DMC) for preparing biodiesel has been studied in solvent-free system at the catalysis of potassium hydroxide (KOH) as heterogeneous catalyst. Fatty acid methyl esters (FAMEs) were analyzed by GC with internal standard method. The effects of reaction conditions (molar ratio of DMC and palm oil, catalyst amount and time) on FAMEs yield were investigated. The highest FAMEs yield could reach 96.2% at refluxing temperature for 8h with molar ratio of DMC and oil 9:1 and 8.5% KOH (based on oil weight). Kinetics of the KOH-catalyzed transesterification of palm oil and DMC was researched over a temperature range of 65-75°C. A pseudo first-order model was proposed. The activation energy (E_a) was 79.1kJmo1~(-1) and the pre-exponential factor (k_o) was 1.26×10~9min~(-1) from Arrhenius equation. Further, a plausible reaction mechanism for the catalytic process with DMC as acyl acceptor was proposed.
机译:在无溶剂体系中,以氢氧化钾(KOH)为多相催化剂,对棕榈油与碳酸二甲酯(DMC)的酯交换反应制备生物柴油进行了研究。用内标法通过GC分析脂肪酸甲酯(FAME)。研究了反应条件(DMC与棕榈油的摩尔比,催化剂用量和时间)对FAMEs收率的影响。 DMC和油的摩尔比为9:1和KOH(基于油的重量)为8:5时,在回流温度下连续8h,FAME的最高收率可以达到96.2%。在65-75°C的温度范围内研究了KOH催化棕榈油和DMC的酯交换反应的动力学。提出了伪一阶模型。根据Arrhenius方程,活化能(E_a)为79.1kJmo1〜(-1),指数前因子(k_o)为1.26×10〜9min〜(-1)。此外,提出了以DMC作为酰基受体催化过程的合理反应机理。

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