首页> 外国专利> PROCESS FOR THE CO-PRODUCTION OF A STREAM OF A FATTY ALCOHOL HAVING A FIRST CARBON CHAIN LENGTH AND A STREAM OF A FATTY ALCOHOL HAVING A SECOND CARBON CHAIN LENGTH

PROCESS FOR THE CO-PRODUCTION OF A STREAM OF A FATTY ALCOHOL HAVING A FIRST CARBON CHAIN LENGTH AND A STREAM OF A FATTY ALCOHOL HAVING A SECOND CARBON CHAIN LENGTH

机译:具有第一碳链长度的脂肪醇的流和具有第二碳链长度的脂肪醇的流的联产工艺

摘要

A process for the co-production of a stream of a fatty alcohol having first carbon chain lengths and a stream of a fatty alcohol having a second carbon chain lengths, said second carbon chain lengths being longer than said first carbon chain lengths, said process comprising the steps of: (a) supplying a stream comprising lower alkyl esters of fatty acids having chain lengths comprising the first and second chain lengths to a first vaporization zone and contacting said stream with an amount of hydrogen recycled from step (i) which is sufficient to vaporize the lower alkyl esters of the fatty acids having the first carbon chain lengths into the hydrogen; (b) supplying the hydrogen and the vaporized lower alkyl esters of fatty acids having the first carbon chain lengths to a first reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired alcohol having first carbon chain lengths; (c) recovering from the first reaction zone an alcohol product stream having first carbon chain lengths and the hydrogen; (d) supplying the unvaporized lower alkyl esters of the fatty acids having second carbon chain lengths remaining from step (a) to a second vaporization zone; (e) contacting the unvaporized lower alkyl esters having second carbon chain lengths in the second vaporization zone with an amount of hydrogen sufficient to vaporize the lower alkyl esters having fatty acids of the second carbon chain lengths into the hydrogen; (f) supplying the hydrogen and the vaporized lower alkyl esters of fatty acids having second carbon chain lengths to a second reaction zone comprising catalyst and operating under reaction conditions to allow hydrogenation to the desired alcohol having second carbon chain lengths; (g) recovering from the second reaction zone an alcohol product stream having second carbon chain lengths and hydrogen; (h) separating the stream of fatty acid alcohol having the second carbon chain length from hydrogen; and (i) recycling a portion of the hydrogen recovered in step (h) to the first vaporization zone and a portion to the second vaporization zone.
机译:共生产具有第一碳链长度的脂肪醇流和具有第二碳链长度的脂肪醇流的方法,所述第二碳链长度长于所述第一碳链长度,所述方法包括步骤:(a)将包含链长包括第一和第二链长的脂肪酸的低级烷基酯的料流提供到第一汽化区,并使所述料流与从步骤(i)回收的足够量的氢气接触将具有第一碳链长度的脂肪酸的低级烷基酯蒸发成氢; (b)将具有第一碳链长的脂肪酸的氢和汽化的低级烷基酯供应到包含催化剂并在反应条件下操作以允许氢化为具有第一碳链长的所需醇的第一反应区; (c)从第一反应区中回收具有第一碳链长度和氢的醇产物流; (d)将步骤(a)中剩余的具有第二碳链长度的脂肪酸的未蒸发的低级烷基酯供应至第二蒸发区; (e)使在第二汽化区中具有第二碳链长的未汽化的低级烷基酯与足以使具有第二碳链长的脂肪酸的低级烷基酯汽化为氢的氢量接触; (f)将具有第二碳链长的脂肪酸的氢和汽化的低级烷基酯供应到包含催化剂并在反应条件下操作的第二反应区,以允许氢化为具有第二碳链长的期望的醇; (g)从第二反应区中回收具有第二碳链长度和氢的醇产物流; (h)将具有第二碳链长度的脂肪酸醇流与氢分离; (i)将在步骤(h)中回收的一部分氢气再循环到第一汽化区,并将一部分氢气再循环到第二汽化区。

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