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PROCESS FOR PRODUCING UNSATURATED ALDEHYDES AND ACIDS BY FIXED-BED CATALYTIC PARTIAL OXIDATION AND REACTOR THEREFOR

机译:固定床催化部分氧化反应器制备不饱和醛和酸的方法

摘要

Disclosed is a process for producing unsaturated aldehydes and/or unsaturated acids from olefins or alkanes in a fixed bed shell-and-tube heat exchanger-type reactor by catalytic vapor phase oxidation. A heat exchanger-type reactor for use in such a process is also disclosed. In the process, at least one of the first-step reaction zone and the second-step reaction zone is divided into two or more shell spaces by at least one partition; each of the divided shell spaces is independently heat-controlled; a heat transfer medium in the first shell space of the first-step reaction zone or the first shell space of the second-step reaction zone has a temperature ranging from the lowest active temperature of a catalyst layer packed in a reaction tube corresponding to the first shell space of the first-step reaction zone or the first shell space of the second-step reaction zone to [the lowest active temperature + 20 °C], when referring to the two or more shell spaces corresponding to the first-step reaction zone sequentially as the first shell space of the first-step reaction zone, the second shell space of the first-step reaction zone, ..., the nth shell space of the first-step reaction zone, and the two or more shell spaces corresponding to the second-step reaction zone sequentially as the first shell space of the second-step reaction zone, the second shell space of the second-step reaction zone, ... , the nth shell space of the second-step reaction zone; and the first shell space of the first-step reaction zone or the first shell space of the second-step reaction zone is controlled in such a manner that the first shell space provides a reactant conversion contribution per length as defined in Equation 1 or 2 of 1.2~2.5.
机译:公开了在固定床壳管式热交换器型反应器中通过催化气相氧化从烯烃或烷烃生产不饱和醛和/或不饱和酸的方法。还公开了用于这种方法的热交换器型反应器。在该方法中,第一步反应区和第二步反应区中的至少一个被至少一个隔板分成两个或多个壳空间。每个分开的壳体空间是独立受热控制的;第一步反应区的第一壳空间或第二步反应区的第一壳空间中的传热介质的温度范围为填充在对应于第一反应区的反应管中的催化剂层的最低活性温度。当涉及对应于第一步反应区的两个或多个壳空间时,第一步反应区的壳空间或第二步反应区的第一壳空间为[最低活性温度+ 20°C]依次作为第一步反应区的第一壳空间,第一步反应区的第二壳空间,...,第一步反应区的第n个壳空间以及两个或多个对应的壳空间依次进入第二步反应区,作为第二步反应区的第一壳空间,第二步反应区的第二壳空间,…,第二步反应区的第n壳空间;并以这样的方式控制第一步反应区的第一壳空间或第二步反应区的第一壳空间,使得第一壳空间按式(1)或(2)定义的每长度提供反应物转化贡献。 1.2〜2.5。

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