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Synthesis of biodiesel from soybean oil and methanol catalyzed by cationic ion-exchange resin in a ultrasonic reactor

机译:超声反应器中阳离子离子交换树脂催化的阳离子油和甲醇的合成生物柴油

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摘要

To improve the efficiency of the production of biodiesel (Fatty Acid Methyl Ester, FAME), a new production method for FAME is developed. The transesterification was carried out in a ultrasonic reactor using solid acid catalysts (cation-exchange resin or zeolite beta) under the atmospheric condition; the average pore size for these catalysts were determined by itrogen adsorption experiments, the FAME content in the reaction mixture were quantified by a potassium hydroxide aponification method, and the product was investigated by FTIR imaging for further structural analysis. Experimental results showed that cation-exchange resin NKC-9 exhibited higher catalytic activity than zeolite beta, which may be correlated to the larger pore size of the NKC-9 produced stronger cavitations effect. When the methanol/ soybean oil molar ratio was 20, reaction temperature at 333K, reaction time 6 hours and catalyst/soybean oil mass ratio of 1.08wt%, the conversion of triglyceride 68.1 wt% was obtained from this optimal reaction condition.
机译:为提高生物柴油生产的效率(脂肪酸甲酯,名称),开发了一种新的生产方法。在大气条件下使用固体酸催化剂(阳离子 - 交换树脂或沸石β)在超声反应器中进行酯交换;通过Itrogoger吸附实验测定这些催化剂的平均孔径,通过氢氧化钾呼吸方法定量反应混合物中的MAME含量,通过FTIR成像来研究产品进行进一步的结构分析。实验结果表明,阳离子交换树脂NKC-9表现出比沸石β更高的催化活性,这可能与NKC-9的较大孔径相关的沸石β产生的更强的空腔效应。当甲醇/大豆油摩尔比为20时,反应温度为333k,反应时间6小时和催化剂/大豆油质量比为1.08wt%,从而从该最佳反应条件下获得甘油三酯的转化率68.1wt%。

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