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Free Fatty Acid Reduction for Biodiesel Production in Reactive Distillation Column

机译:反应蒸馏塔中生物柴油生产的游离脂肪酸还原

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To treat high free fatty acid feedstock in biodiesel production, the reduction of free fatty acid by esterification in continuous reactive distillation column was investigated. In this work, ethanol and crude palm oil (CPO) which the molar ratio of ethanol to oil was 8:1 were selected as reactants with Amberlyst-15 catalyst and the reaction temperature was 80±5°C. The effects of type of reactor, feed location and amount of catalyst were examined experimentally. The result showed that either high amount of catalyst in reactive distillation column increased the efficiency of free fatty acid reduction. Finally, at the same amount of catalyst, feed location at upper part of column yield better reduction free fatty acid than lower part of column.
机译:为了在生物柴油生产中处理高脂肪酸原料,研究了通过连续反应蒸馏塔中酯化的游离脂肪酸的减少。在这项工作中,乙醇和粗棕榈油(CPO)将乙醇与油的摩尔比为8:1作为反应物,催化剂 - 15催化剂,反应温度为80±5℃。实验检查反应器类型,饲料位置和催化剂的量的影响。结果表明,反应蒸馏塔中的任一催化剂增加了游离脂肪酸还原的效率。最后,在相同量的催化剂中,柱上部的饲料位置产生比柱下部的无游离脂肪酸更好。

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