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Kinetics of transesterification in rapeseed oil to biodiesel fuel as treated in supercritical methanol

机译:在超临界甲醇中处理的菜籽油到生物柴油燃料的酯交换反应动力学

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A kinetic study in free catalyst transesterification of rapeseed oil was made in subcritical and supercritical methanol under different reaction conditions of temperatures and reaction times. Runs were made in a bath-type reaction vessel ranging from 200deg.C in subcritical temperaturee to 500deg.C at supercritical state with different molar ratios of methanol to rapeseed oil to determine rate constants by employing a simple method. As a result, the conversion rate of rapeseed oil to its methyl esters was found to increase dramatically in the supercritical state, and reaction temperature of 350deg.C was considered as the best condition, with the molar ratio of methanol in rapeseed oil being 42.
机译:在不同温度和反应时间的反应条件下,在亚临界和超临界甲醇中进行菜籽油的游离催化剂酯交换反应的动力学研究。在浴式反应器中,在亚临界温度至200℃,超临界状态至500℃的浴式反应器中,以不同的甲醇与菜籽油摩尔比进行操作,以通过简单的方法确定速率常数。结果,发现菜籽油在其超临界状态下向其甲酯的转化率急剧增加,并且认为350℃的反应温度是最佳条件,菜籽油中甲醇的摩尔比为42。

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