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PROCESS AND PLANT FOR THE PRODUCTION OF ε-CAPROLACTAM AND AMMONIUM SULFATE ON INDUSTRIAL SCALE

机译:用于生产ε-己内酰胺和产业规模硫酸铵的过程和植物

摘要

The invention provides a process and a plant for the production of ε-caprolactam and crystalline ammonium sulfate in an industrial-scale plant, wherein the plant comprises a Beckmann rearrangement reaction section, an ammonium sulfate crystallization section, and one or more heat exchangers configured to transfer heat from the Beckmann rearrangement reaction section to the ammonium sulfate crystallization section and wherein the process comprises the steps of: a) feeding (i) cyclohexanone oxime and (ii) oleum and/or sulfuric acid to the Beckmann rearrangement reaction section b) reacting components (i) and (ii) in the Beckmann rearrangement reaction section to form a reaction mixture comprising ε-caprolactam, whereby heat of reaction is generated; c) discharging the reaction mixture comprising ε-caprolactam from the Beckmann rearrangement reaction section; d) removing partially or fully the heat of reaction generated in the Beckmann rearrangement reaction section by one or more heat exchangers configured to transfer heat from the Beckmann rearrangement reaction section; e) feeding an aqueous liquid comprising ammonium sulfate to the ammonium sulfate crystallization section; f) introducing heat into the ammonium sulfate crystallization section comprising the aqueous ammonium-sulfate-comprising liquid by one or more heat exchangers configured to transfer heat into the ammonium sulfate crystallization section; g) forming ammonium sulfate crystals by evaporative crystallization in the ammonium sulfate crystallization section; characterized in that h) the heat of reaction removed from the Beckmann rearrangement reaction section in step d) is at least partially or fully transferred to the ammonium sulfate crystallization section in step f).
机译:本发明提供了一种用于在工业规模植物中生产ε-己内酰胺和结晶硫酸铵的方法和植物,其中该植物包括Beckmann重排反应部分,硫酸铵结晶部分和配置为的一个或多个热交换器将热量从Beckmann重排反应部分转移到硫酸铵结晶部分,并且其中该方法包括以下步骤:a)饲料(i)环己酮肟和(ii)氧化物和/或硫酸对Beckmann重排反应部分B)反应Beckmann重排反应部分中的组分(I)和(II)以形成包含ε-己内酰胺的反应混合物,由此产生反应热量; c)将包含ε-己内酰胺的反应混合物从Beckmann重排反应部分排出; d)通过一个或多个热交换器部分地或完全地除去在Beckmann重排反应部分中产生的反应热,该热交换器被配置为从Beckmann重新排列反应部分转移热量; e)喂养包含硫酸铵的水性液体与硫酸铵结晶部分; f)将热量引入硫酸铵结晶部分,所述硫酸铵结晶部分包含一种或多种热交换器,所述硫酸铵 - 硫酸铵含液体,所述热交换器构造成将热量转移到硫酸铵结晶部分中; g)通过硫酸铵结晶部分中的蒸发结晶形成硫酸铵晶体;其特征在于H)在步骤d)中从Beckmann重排反应部分中除去的反应热至少部分地或完全转移到步骤f)中的硫酸铵结晶部分。

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