首页> 外国专利> Guerbet alcohol(s) prodn. - by condensn. of prim. linear alkanol(s) in presence of alkali and catalyst mixt. of iron-III sulphate, basic copper carbonate and nickel

Guerbet alcohol(s) prodn. - by condensn. of prim. linear alkanol(s) in presence of alkali and catalyst mixt. of iron-III sulphate, basic copper carbonate and nickel

机译:格尔伯特酒精产品。 -通过压缩。素数在碱和催化剂混合物存在下的直链烷醇。硫酸铁Ⅲ,碱式碳酸铜和镍

摘要

Guerbet alcohols (I) are produced by condensation of linear prim. aliphatic alcohols (II) in the presence of an alkali or alkaline earth metal hydroxide (III) and a catalyst mixt. contg. Fe(III) sulphate (A), basic Cu carbonate (B) and Ni (C). More specifically, (II) are 6-22C linear prim. aliphatic alcohols, and amt. of (II) is 2-10 wt.% (pref. KOH) w.r.t. (II); wt. ratio A:B:C in the catalyst mixt. is (0.25:0.25:1)-(1:1:1), and catalyst concn. is 0.05-1 wt.% w.r.t. (II); pref. condensation is carried out at 180-250 deg.C. in a cascade appts.. USE/ADVANTAGE - The process is useful for the prodn. of alpha-branched alcohols (I) which are used e.g. in the mfr. of superfatting agents, lubricants, detergents, etc.. The process can be operated as a batch or (pref.) continuous process (contrast prior-art processes); reaction times are also reduced. In an example, octanol was subjected to continuous Guerbet condenstion in a vertical 3-stage cascade appts. in the presence of 4 wt.% KOH and 0.4 wt.% catalyst (Fe2(SO4)3.5H2O/CuCO3.Cu(OH)2/Ni = 1:1:2,; Ni as 17 wt.% slurry in fatty alcohol or fish oil); stages 1, 2 and 3 were operated at 187, 217 and 244 deg.C. respectively, and the reactants were mixed by means of a stream of nitrogen at 800 ml./hr; alcohol (I) was run off at 475 ml/hr. and water at 25 ml/hr.. The alcohol fraction contained 4.5 wt.% 8C, 66.0 wt.% iso-16C and 11.0 wt.% 24C alcohols, and 18.5 wt.% distn. residue.
机译:Guerbet醇(I)是通过线性底漆的缩合生成的。在碱金属或碱土金属氢氧化物(III)和催化剂混合物存在下的脂肪醇(II)。续硫酸铁(III)(A),碱式碳酸铜(B)和镍(C)。更具体地说,(II)是6-22C线性底漆。脂肪族醇,和amt。 (II)的重量为2-10重量%(优选KOH)。 (II);重量催化剂混合物中的比例A:B:C。为(0.25:0.25:1)-(1:1:1),催化剂浓度为w.r.t为0.05-1 wt。% (II);偏好冷凝在180-250℃下进行。在级联应用程序中。使用/优势-该过程对产品很有用。的α-支链醇(I)的使用例如在mfr。该方法可以分批或(优选)连续过程(与现有技术相反)进行。反应时间也减少了。在一个实例中,使辛醇在垂直的三阶段级联装置中进行连续的Guerbet冷凝。在4 wt。%的KOH和0.4 wt。%的催化剂(Fe2(SO4)3.5H2O / CuCO3.Cu(OH)2 / Ni = 1:1:2 ;;镍在脂肪醇中为17 wt。或鱼油);阶段1、2和3在187、217和244℃下运行。分别用800毫升/小时的氮气流混合反应物。乙醇(I)以475 ml / hr的速度流失。醇级分包含4.5wt。%的8C,66.0wt。%的iso-16C和11.0wt。%的24C醇,和蒸馏水为18.5wt。%。残留物。

著录项

  • 公开/公告号DE4014736A1

    专利类型

  • 公开/公告日1991-11-14

    原文格式PDF

  • 申请/专利权人 HENKEL KGAA 4000 DUESSELDORF DE;

    申请/专利号DE19904014736

  • 发明设计人 REINHOLD KARL 5650 SOLINGEN DE;

    申请日1990-05-08

  • 分类号C07C29/34;C07C31/02;C07C31/125;

  • 国家 DE

  • 入库时间 2022-08-22 05:26:01

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