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Process for the preparation of C10-C30-alkenes by partial hydrogenation of alkynes on fixed-bed palladium-supported catalysts

机译:在固定床钯负载的催化剂上通过炔烃的部分加氢制备C10-C30烯烃的方法

摘要

A process for the preparation of alkenes by partial hydrogenation of alkynes in the liquid phase at temperatures of 20 to 250 ° C and hydrogen pressures from 0.3 to 200 bar on palladium-fixed-bed support catalysts obtained by heat treatment of the support material in the air, cooling, applying a palladium compound and optionally additionally for doping purposes other metal ions, molding and processing to monolithic catalyst elements are available, which is characterized in that A) alkynes employing having 10 to 30 carbon atoms, as starting compounds, B) applying the palladium compound and optionally the other metal ions by impregnating the annealed and cooled support material with a palladium salts and optionally other metal ion-containing solution and subsequent drying on the support material and C) that is added to the hydrogenation 10 to 2000 ppm Kohlenmomoxid (CO) or can be a corresponding amount of CO in the liquid phase, resulting from slight decomposition of an added to the reaction mixture compound which eliminates CO under the reaction conditions.; Particularly advantageously, the process is designed, if one carries out the partial hydrogenation in a tubular reactor in a downflow or upflow mode with product recycling at cross-sectional loadings of from 20 to 500 m 3 / m 2 * h. Particularly suitable method for the preparation of 3,7,11,15-tetramethyl-1-hexadecen-3-ol (isophytol), 3,7,11-trimethyl-1-dodecen-3-ol is (tetrahydronerolidol), 3 , 7,11-trimethyl-1,4-dodekadien-3-ol, 3,7,11-trimethyl-1,6-dodekadien-3-ol (dihydronerolidol), 3,7-dimethyl-oct-1,6- dien-3-ol or 3,7-dimethyl-oct-1-en-3-ol from the corresponding alkynes.
机译:一种通过在20-250°C的温度和0.3-200 bar的氢气压力下在液相中将炔烃在液相中进行部分加氢的方法制得的烯烃,该钯固定床载体催化剂是通过在空气,冷却,施加钯化合物以及可选地另外用于掺杂的目的,还可以将其他金属离子,模制和加工成整体催化剂元件,其特征在于 A)炔烃采用10至30个碳原子,作为起始化合物, B)通过将退火并冷却的载体材料浸入钯盐和任选的其他含金属离子的溶液中,然后在载体材料上干燥,来施加钯化合物和任选的其他金属离子和 C)添加到加氢10至2000 ppm Kohlenmomoxid(CO)或可以是液体中相应数量的CO ;由于在反应条件下添加到反应混合物中的化合物发生轻微分解,从而消除了CO。如果在管式反应器中以向下或向上流动的方式进行部分氢化,并以横截面负荷为20至500 m 3 / m < Sup> 2 * h。制备3,7,11,15-四甲基-1-十六烯-3-醇(异植醇),3,7,11-三甲基-1-十二烯-3-醇的特别合适的方法是(四氢神经寡糖),3, 7,11-三甲基-1,4-十二烷基三醇,3,7,11-三甲基-1,6-十二烷基三醇(二氢神经醇),3,7-二甲基-辛基-1,6-二烯来自相应炔烃的-3-ol或3,7-二甲基-oct-1-en-3-ol。

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