首页> 外国专利> method for the continuous recovery of useful components from the mixture.in the catalytic preparation of chloorcyaan from acid and chlorine or in the subsequent trimerisering of chloorcyaan to cyanuurchloride in the vapour phase is obtained.

method for the continuous recovery of useful components from the mixture.in the catalytic preparation of chloorcyaan from acid and chlorine or in the subsequent trimerisering of chloorcyaan to cyanuurchloride in the vapour phase is obtained.

机译:一种从混合物中连续回收有用成分的方法,该方法包括从酸和氯催化制备氯氰菊酯,或随后在气相中将氯氰菊酯三聚化为氰尿酰氯。

摘要

1,268,673. Separating chlorine and cyanogen chloride from mixtures with hydrogen chloride. AGRIPAT S.A. 9 July, 1969 [10 July, 1968], No. 34482/69. Heading B1L. [Also in Divisions Cl and C2] Hydrogen chloride is separated from chlorine and cyanogen chloride by passing the mixture (which has originated from the catalytic production of cyanogen chloride from hydrocyanic acid and chlorine, or from the trimerization of cyanogen chloride to cyanuric chloride) by line 9 to jacketed absorber 1 where pentachloroethane is agitated in contact with the gas stream. The pentachloroethane preferably contains a small proportion of iodine to prevent undue chlorination by the chlorine in the gas stream. The bulk of the hydrogen chloride, which is not absorbed, rises through condenser 2 and leaves by line 10. Solvent containing cyanogen chloride and chlorine passes by line 3 to evaporator 4, and thence in gaseous form up through distillation column 5 to condenser 6. Solvent condensate therefrom is returned by line 13 to absorber 1, while cyanogen chloride and chlorine pass to reactor 7 which is irradiated with u.v. light. This causes any entrained solvent to be converted to hexachloroethane, which is condensed in liquid air trap 8. Residual gases pass by line 11 back to a cyanogen chloride or cyanuric chloride reactor.
机译:1,268,673。从与氯化氢的混合物中分离氯气和氯化氰。 AGRIPAT S.A.,1969年7月9日[1968年7月10日],第34482/69号。标题B1L。 [也在C1和C2区中]通过使混合物(源自氢氰酸和氯催化生产氯化氰,或源自氯化氰三聚为氰尿酰氯)而将氯化氢与氯和氯化氰分离。管线9到达带夹套的吸收器1,在其中搅拌五氯乙烷与气流接触。五氯乙烷优选包含少量的碘,以防止气流中的氯过度氯化。未被吸收的大部分氯化氢通过冷凝器2上升并通过管线10离开。含有氯化氰和氯的溶剂通过管线3到达蒸发器4,然后以气态形式通过蒸馏塔5到达冷凝器6。溶剂冷凝液通过管线13返回到吸收器1,氯化氰和氯气进入反应器7,并用uv照射光。这导致任何夹带的溶剂转化为六氯乙烷,该六氯乙烷在液体空气收集器8中冷凝。残留气体通过管线11返回氯化氰或氰尿酰氯反应器。

著录项

  • 公开/公告号NL6910547A

    专利类型

  • 公开/公告日1970-01-13

    原文格式PDF

  • 申请/专利权人

    申请/专利号NL19690010547

  • 发明设计人

    申请日1969-07-09

  • 分类号C01C3/16;C01B7/08;

  • 国家 NL

  • 入库时间 2022-08-23 11:33:49

相似文献

  • 专利
  • 外文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号