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Process for the continuous hydrogenation of fats, fatty acids and fatty acid derivatives in the presence of a heterogeneous catalyst

机译:在非均相催化剂存在下连续氢化脂肪,脂肪酸和脂肪酸衍生物的方法

摘要

For continuous heterogeneous hydrogenation, fats, fatty acids and/or fatty acid derivatives are brought into contact with hydrogen in the presence of a heterogeneous catalyst dispersed in a liquid phase in a tubular packed reactor, of which the length-to-diameter ratio is 10:1, under pressure of from 0.5 to 300 bar and at temperatures of from 60 to 260 C. The reactor is packed with a geometrically regularly arranged elements of a material inert to the components under the reaction conditions, and the hydrogen is passed through the reactor in parallel current or countercurrent to the fatty acid substrate under a gas velocity of from 0.5 to 30 cm/sec., based on the overall cross- section of the reactor. Preferably the catalyst is fixed on an insoluble support and suspended in small quantities of the particular reaction product before being added to the substrate and entering the reactor.
机译:对于连续的非均相氢化,在管式填充反应器中,在液相中分散的非均相催化剂存在下,使脂肪,脂肪酸和/或脂肪酸衍生物与氢接触,其长径比为10 1:1,压力为0.5至300 bar,温度为60至260C。反应器装有在反应条件下对成分呈惰性的材料的几何规则排列元素,氢气通过基于反应器的总横截面,在0.5-30cm / sec的气体速度下,与脂肪酸底物平行或逆流的反应器。优选地,将催化剂固定在不溶性载体上并悬浮在少量的特定反应产物中,然后将其添加至底物并进入反应器。

著录项

  • 公开/公告号US4847016A

    专利类型

  • 公开/公告日1989-07-11

    原文格式PDF

  • 申请/专利权人 HENKEL KOMMANDITGESELLSCHAFT AUF AKTIEN;

    申请/专利号US19870008706

  • 发明设计人 GERD GOBEL;

    申请日1987-01-29

  • 分类号C11C3/12;

  • 国家 US

  • 入库时间 2022-08-22 06:27:50

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