首页> 外国专利> The preparation process of copper catalysts supported on hydroxyapatite, and its application in the direct synthesis of crotonaldehyde from ethanol.

The preparation process of copper catalysts supported on hydroxyapatite, and its application in the direct synthesis of crotonaldehyde from ethanol.

机译:羟基磷灰石负载铜催化剂的制备方法及其在乙醇直接合成巴豆醛中的应用。

摘要

The preparation process of copper catalysts supported on hydroxyapatite, and its application in the direct synthesis of crotonaldehyde from ethanol.It is described a process for preparing catalysts based on copper supported on hydroxyapatite, useful for the production of crotonaldehyde from ethanol.The process of obtaining crotonaldehyde comprises directing a stream (2) of ethanol fresh for a reactor (7) loaded with the catalyst of the invention.Under the reaction conditions at temperatures between 180 and 360 C 198 198 C, the pressure between 1 and 2 atmospheres and factor of residence time 50 to 250 kg ~ cat ~ min kg ^ - 1 ^ ~ EtOH.Obtaining a stream (8) of the product at the outlet of the reactor (7) which is cooled in a heat exchanger system (9), where it is separated the liquid product, and the product gas stream (17), the current (10).The heat exchanger (11) separates mainly acetaldehyde, the current (16) which can be recycled to the reactor (7), and a hydrogen stream (13).You can feed the reactor (24) for the reactions of hydrogenation of crotonaldeido in products such as alcohol crotu00edlico, butanol and butiraldeido.Hydrogen can alternatively be stored in the tank (14).The liquid stream (17) containing the liquid product is refined in (18) and the crotonaldehyde product is stored in the tank (20).Or is fed to the reactor (23) for the integrated production of oxidation products of crotonaldeido and / or the reactor (24) for the integrated production of products of hydrogenation of crotonaldehyde and u00e1lco are:Ol crotilico, butanol and butyraldehyde.
机译:羟基磷灰石负载的铜催化剂的制备方法及其在乙醇直接合成巴豆醛中的应用。描述了一种基于羟基磷灰石负载的铜催化剂的制备方法,该方法可用于由乙醇生产巴豆醛。巴豆醛包括将新鲜的乙醇料流(2)引导至装有本发明催化剂的反应器(7)。在温度为180至360℃> 198 <198198℃的反应条件下,压力为1至2℃。大气和停留时间的因素50至250 kg〜cat〜min kg ^-1 ^〜EtOH在反应器(7)的出口处获得产物流(8),该产物流在热交换器系统(9)中冷却),其中将液体产物和产物气流(17)分离为气流(10)。换热器(11)主要分离乙醛,将气流(16)再循环至反应器(7)和氢气流(13 )。您可以将反应器(24)进料到巴豆醛基在诸如乙醇c,丁醇,丁醇和丁醛等产品中的氢化反应,也可以将氢气存储在罐(14)中。液体产物在(18)中进行精制,巴豆醛产物存储在罐(20)中,或进料到反应器(23)中以综合生产巴豆醛和/的氧化产物,或巴豆醛的反应器(24)巴豆醛和 col加氢的氢化产物的综合生产是:o crotilico,丁醇和丁醛。

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