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Synthesis of fatty acid methyl ester via transesterification of waste frying oil by a zinc-modified pumice catalyst: Taguchi approach to parametric optimization

机译:锌改性浮石催化剂酯交换用盐酸酯化酯化的脂肪酸甲酯的合成:TAGUCHI对参数优化的方法

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摘要

Methanolysis of waste frying oil (WFO) was conducted to synthesize fatty acid methyl esters (FAME) using zinc-modified pumice (ZMP) as a heterogeneous catalyst. The ZMP catalyst was prepared via incipient wetness impregnation method and characterized by various spectroscopic techniques such as Brunauer-Emmett-Teller (BET) surface area, scanning electron microscopy (SEM), energy dispersive X-ray (EDX), X-ray fluorescence (XRF), Fourier transform infrared (FTIR) spectroscopy and X-ray diffraction (XRD). Taguchi design approach was employed to optimize the transesterification process variables, which include reaction temperature (50-70 degrees C), reaction time (1-3 h), methanol/WFO molar ratio (6:1-12:1) and catalyst loading (1-3 wt%). The transesterification reaction kinetic and impact of reaction temperature on the reaction rate were investigated. The kinetic data obtained at different temperatures were evaluated using zero-order and pseudo-first-order models. Among the process variables studied, FAME yield was mostly affected by the reaction temperature, methanol/WFO molar ratio, and catalyst loading. The maximum FAME yield of 91.05 wt% was attained at the optimum reaction temperature of 60 degrees C, 3 wt% catalyst loading, and 12:1 methanol/WFO molar ratio. The better activity exhibited by the ZMP catalyst in the transesterification reaction was attributed to the interaction among several metal oxides present in the catalyst as confirmed by the EDX, XRF and XRD analyses. The catalyst stability study showed that the ZMP could be reused up to four times. The pseudo-first-order model gave the best fit with the catalytic reaction data, and the activation energy was 50.61 kJ mol(-1).
机译:通过作为非均相催化剂,对废物煎炸油(WFO)的甲醇分解合成脂肪酸甲酯(SAME)作为非均相催化剂。 ZMP催化剂通过初期湿润浸渍方法制备,其特征在于各种光谱技术,如Brunauer-Emmett-exerer(Bet)表面积,扫描电子显微镜(SEM),能量分散X射线(EDX),X射线荧光( XRF),傅里叶变换红外(FTIR)光谱和X射线衍射(XRD)。使用Taguchi设计方法来优化酯交换过程变量,包括反应温度(50-70℃),反应时间(1-3小时),甲醇/ WFO摩尔比(6:1-12:1)和催化剂负载(1-3wt%)。研究了酯交换反应动力学和反应温度对反应速率的影响。使用零阶和伪一阶模型评估在不同温度下获得的动力学数据。在研究的过程变量中,对反应温度,甲醇/ WFO摩尔比和催化剂负载影响的增生产量主要受影响。在60℃,3wt%催化剂负荷和12:1甲醇/ WFO摩尔比的最佳反应温度下获得91.05wt%的最大名称产率。 ZMP催化剂在酯交换反应中表现出的更好的活性归因于通过EDX,XRF和XRD分析证实的催化剂中存在的几种金属氧化物之间的相互作用。催化剂稳定性研究表明,ZMP可以重复达到四次。伪第一阶模型具有最佳拟合催化反应数据,活化能量为50.61 kJ摩尔(-1)。

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