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Preparation of C10-C30-alkenes by partial hydrogenation of alkynes over fixed-bed supported palladium catalysts

机译:在固定床负载的钯催化剂上通过炔烃的部分加氢制备C10-C30烯烃

摘要

Alkenes are prepared by partial hydrogenation of alkynes in the liquid phase at from 20 to 250° C. and hydrogen partial pressures of from 0.3 to 200 bar over fixed-bed supported palladium catalysts which are obtainable by heating the support material in the air, cooling, applying a palladium compound and, if required, additionally other metal ions for doping purposes, molding and processing to give monolithic catalyst elements, by a process in which ;A) alkynes of 10 to 30 carbon atoms are used as starting compounds, ;B) the palladium compound and, if required, the other metal ions are applied to the support material by impregnation of the heated and cooled support material with a solution containing palladium salts and, if required, other metal ions and subsequent drying, and ;C) from 10 to 2000 ppm of carbon monoxide (CO) are added to the hydrogenation gas or a corresponding amount of CO is allowed to form in the liquid phase by slight decomposition of a compound which is added to the reaction mixture and eliminates CO under the reaction conditions. ;The process is particularly advantageous if the partial hydrogenation is carried out in a tube reactor by the trickle-bed or liquid phase procedure with product recycling at cross-sectional loadings of from 20 to 500 m3 /m2 *h. The process is particularly suitable for the preparation of 3,7,11,15-tetramethyl-1-hexadecen-3-ol (isophytol), 3,7,11-trimethyl-1-dodecen-3-ol (tetrahydronerolidol), 3,7,11-trimethyl-1,4-dodecadien-3-ol, 3,7,11-trimethyl-1,6-dodecadien-3-ol (dihydronerolidol), 3,7-dimethyloct-1,6-dien-3-ol or 3,7-dimethyloct-1-en-3-ol from the corresponding alkynes.
机译:通过在20-250℃下在液相中炔烃的部分氢化制备烯烃。固定床负载钯催化剂上的C.和氢分压为0.3至200 bar,这可以通过在空气中加热载体材料,冷却,施加钯化合物以及(如果需要)其他用于掺杂目的的金属离子获得,通过以下方法成型和加工,以得到整体式催化剂元素;其中:A)将10至30个碳原子的炔烃用作起始化合物;; B)钯化合物;如果需要,将其他金属离子施加到载体上通过用含钯盐和其他金属离子(如有需要)的溶液浸渍加热和冷却的载体材料,然后干燥,以及将10-2000 ppm一氧化碳(CO)中的; C)添加到氢化气体或通过稍微分解加入到反应混合物中的化合物并在反应条件下消除CO,可以在液相中形成相应量的CO。 ;如果在管式反应器中通过滴流床或液相方法进行部分氢化,且产品循环利用的截面负荷为20至500 m 3 / m ,则该方法特别有利 2 * h。该方法特别适合于制备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(四氢神经寡糖),3 ,7,11-三甲基-1,4-dodecadien-3-ol,3,7,11-三甲基-1,6-dodecadien-3-ol(dihydronerolidol),3,7-二甲基辛基-1,6-dien-来自相应炔烃的3-ol或3,7-二甲基辛-1-烯-3-醇。

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