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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
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.
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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。
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