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Process for the production of methyl esters of fatty acids or ethyl esters of fatty acids and glycerine by transesterification of oil or fat

机译:通过油或脂肪的酯交换反应生产脂肪酸甲酯或脂肪酸乙酯和甘油的方法

摘要

Liquid phase reaction of oil or fat with MeOH or EtOH and an alkaline catalyst (I) to give the fatty acid (m)ethyl ester and glycerol, which are recovered separately, is carried out in one or more stages. Each stage has a mixer and a separator for sepg. a light, ester-rich phase (II) and a heavy, glycerol-rich phase (III). The first stage is supplied with oil or fat, MeOH or EtOH and (I) and glycerol is sepd. from (III) from the first stage. The novelty is that the glycerol is mixed with alkali hydroxide to give an aq. alkaline soln. with a glycerol:alkali hydroxide molar ratio of 1:5 to 10:1; water is removed, giving mono-alkali glycerate; and the glycerate soln. is passed into mixing zone(s) to cover 50-100% of the total (I) requirement of the reaction.
机译:油或脂肪与MeOH或EtOH以及碱性催化剂(I)的液相反应生成脂肪酸(间)乙基酯和甘油(分别回收)是在一个或多个阶段中进行的。每个阶段都有一个混合器和一个用于分离的分离器。轻,富酯相(II)和重,富甘油相(III)。向第一阶段提供油或脂肪,MeOH或EtOH和(I),然后分离甘油。从第一阶段开始。新颖之处在于,将甘油与碱金属氢氧化物混合,得到水溶液。碱性溶液。甘油:氢氧化氢氧化物的摩尔比为1∶5至10∶1;除去水,得到单碱甘油酸酯;和甘油溶液。将其送入混合区以覆盖反应总需求的50-100%。

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