首页> 外国专利> Method of preparation of acetals of di - or sorting - chloroacetaldehyde or di - or sorting - chloroacetaldehyde of freedom.

Method of preparation of acetals of di - or sorting - chloroacetaldehyde or di - or sorting - chloroacetaldehyde of freedom.

机译:制备二-或分选-氯乙醛或二-或分选-氯乙醛的缩醛的方法。

摘要

A process for preparing chloral alcoholate or free chloral comprises contacting ethyl alcohol at a temperature not exceeding 35 DEG C. with part of the chlorine required, and subsequently treating the heated reaction liquid obtained continuously in countercurrent with the rest of the chlorine required, whereby a prolonged contact between the hydrogen chloride formed and the unconverted ethyl alcohol, sufficient for the formation of substantial proportions of ethyl chloride is prevented. The cold chlorination may be carried out batchwise or in counter-current. The chlorine supply may be adjusted in the hot process to produce chloral alcoholate or free chloral. Pressure may be normal or otherwise, e.g. hydrogen chloride is more easily removed from the hot reaction zone by operating at reduced pressure. A chlorination catalyst PICT:0644916/IV (b)/1 may be present, e.g. ferric chloride. In examples: (1) 96 per cent ethyl alcohol containing ferric chloride is passed into vessel 1 maintained at room temperature via tube 2 whilst chlorine is passed in through tube 3. The reaction mixture is then passed through tube 5 into the top of heated reactor 6, further chlorine being led in at the bottom via tube 10. Hydrogen chloride escapes through the reflux condenser 7 and the reaction product collects in vessel 8. Pure chloral is obtained from the latter by fractional distillation. Residual alcohol is collected in scrubber 12. (2) A similar chlorination is carried out using a third reactor operating at an intermediate temperature between the hot and cold reactions, both free chloral and the alcoholate being obtained. The Specification as open to inspection under Sect. 91 comprises also the production of dichloroacetaldehyde and acetals of di- and trichloroacetaldehyde. This subject-matter does not appear in the Specification as accepted.
机译:一种制备乙醇酸氯醛或游离氯醛的方法,包括使乙醇在不超过35℃的温度下与所需的一部分氯接触,然后与所需的其余氯气逆流连续处理加热的反应液,从而得到防止了所形成的氯化氢与未转化的乙醇之间长时间的接触,足以形成大量的氯乙烷。冷氯化可分批或逆流进行。可以在热过程中调节氯气的供应量,以生产乙醇醛或游离氯醛。压力可以是正常压力或其他压力,例如通过在减压下操作,更容易从热反应区中除去氯化氢。可以存在氯化催化剂,例如。氯化铁。在示例中:(1)将96%的含氯化铁的乙醇通过管2进入保持在室温下的容器1,同时将氯通过管3进入。然后将反应混合物通过管5进入加热的反应器顶部在图6中,另外的氯通过管10被引入底部。氯化氢通过回流冷凝器7逸出,反应产物收集在容器8中。通过分馏从后者获得纯的氯。残留的醇收集在洗涤器12中。(2)使用第三反应器进行类似的氯化反应,该反应器在热反应和冷反应之间的中间温度下操作,同时获得了游离氯醛和醇化物。该规范可供本节检查。 91还包括二氯乙醛和二-和三氯乙醛的缩醛的生产。该主题未在接受的规范中出现。

著录项

  • 公开/公告号FR949082A

    专利类型

  • 公开/公告日1949-08-19

    原文格式PDF

  • 申请/专利权人 N. V. DE BATAAFSCHE PETROLEUM MAATSCHAPPIJ;

    申请/专利号FRD949082

  • 发明设计人

    申请日1947-07-08

  • 分类号C07C45/30;

  • 国家 FR

  • 入库时间 2022-08-24 02:25:20

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