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首页> 外文期刊>Angewandte Chemie >A New Route to Lactam Precursors from Cycloalkanes: Direct Production of Nitrosocycloalkanes or Cycloalkanone Oximes by Using tert-Butyl Nitrite and N-Hydroxyphthalimide
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A New Route to Lactam Precursors from Cycloalkanes: Direct Production of Nitrosocycloalkanes or Cycloalkanone Oximes by Using tert-Butyl Nitrite and N-Hydroxyphthalimide

机译:从环烷烃到内酰胺前体的新途径:使用亚硝酸叔丁酯和N-羟基邻苯二甲酰亚胺直接生产亚硝基环烷烃或环烷酮肟

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摘要

The development of an innovative methodology for the production of bulk and commodity chemicals, in particular one that takes account of effects on the environment, becomes more and more important in industrial chemistry worldwide. ε-Caprolactam is one of the monomers most widely used for the production of nylon 6; the world production capacity of ε-caprolactam in 1998 was about 4.2 million tons. Currently, ε-caprolactam is produced by the following methods (Scheme 1): 1) Beckmann rearrangement of cyclohexanone oxime derived from cyclohexanone and hydroxylamine (Route A) or from cyclohexane and NOCl by the photonitrosation of cyclohexane (PNC) process (Route B), or 2) nitrosation of cyclohexane carboxylic acid with NOHSO_4 (Route C). Of these approaches, Route A is most often employed and accounts for about 70 % of the total production of ε-caprolactam worldwide. However, this method has several drawbacks. Cyclohexanone is supplied by the aerobic oxidation of cyclohexane, which leads to a mixture of cyclohexanone and cyclohexanol (K/A oil), but the conversion of cyclohexane must be kept at only 3-6 % to avoid the formation of further oxidation products such as adipic acid and glutaric acid. Another serious drawback of this method is the coproduction of a large amount of ammonium sulfate waste in both the hydroxylamine production and the Beckmann rearrangement processes.
机译:开发一种用于生产大宗和商品化学品的创新方法,尤其是考虑到对环境影响的一种创新方法,在全球工业化学中变得越来越重要。 ε-己内酰胺是最广泛用于生产尼龙6的单体之一; 1998年全世界ε-己内酰胺的生产能力约为420万吨。目前,ε-己内酰胺是通过以下方法生产的(方案1):1)通过环己烷的光亚硝化(PNC)方法(路线B),对由环己酮和羟胺(路线A)或从环己烷和NOCl衍生的环己酮肟进行贝克曼重排,或2)用NOHSO_4(路线C)亚硝化环己烷羧酸。在这些方法中,路线A最常用,占全世界ε-己内酰胺总产量的70%。但是,这种方法有几个缺点。环己酮通过环己烷的有氧氧化来提供,这会导致环己酮和环己醇(K / A油)的混合物,但必须将环己烷的转化率保持在3-6%,以避免形成进一步的氧化产物,例如己二酸和戊二酸。该方法的另一个严重缺陷是在羟胺生产和贝克曼重排过程中共同生产大量硫酸铵废料。

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