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PRODUCTION OF 1,1,1,3,3,3-HEXAFLUORO-2-PROPANOL

机译:1,1,1,3,3,3-六氟-2-丙醇的生产

摘要

PURPOSE:The hydrogenation of hexafluoroacetone is carried out in the presence of a rhodium catalyst to produce in high yield the titled substance that is used as a surface active agent, emulsifier, polymer solvent, synthetic intermediate of fluorine-containing compounds and intermediate of inhalation anesthetic. CONSTITUTION:The titled substance is obtained by hydrogenation of hexafluoroacetone in the presence of a rhodium catalyst such as reduced rhodium, rhodium oxide, rhodium hydroxide, or rhodium chloride. As a catalyst, 0-valent rhodium is effective and reduced rhodium is preferred. The catalyst is generally in the form of rhodium on a support (such as activated carbon or alumina)[the content of rhodium is 0.5-10wt% based on the support (calculated as metallic rhodium)] and the reaction is preferably carried out in a gaseous or liquid system. The amount of the catalyst ued is 0.001-0.1wt% based on the starting material calculated as metallic rhodium and reaction conditions are 20-100 deg.C, 0.5- 30 atmospheric pressure in the hydrogen partial pressure and 1min to 500hr in reaction time.
机译:用途:六氟丙酮在铑催化剂的存在下进行氢化,以高产率生产用作表面活性剂,乳化剂,聚合物溶剂,含氟化合物的合成中间体和吸入麻醉剂中间体的标题物质。组成:该标题物质是通过在铑催化剂如还原铑,氧化铑,氢氧化铑或氯化铑的存在下六氟丙酮的氢化而获得的。作为催化剂,0价铑是有效的,还原铑是优选的。催化剂通常为在载体(例如活性炭或氧化铝)上的铑形式[铑的含量相对于载体(以金属铑计)为0.5-10wt%],并且该反应优选在甲醇中进行。气体或液体系统。基于以金属铑计算的起始原料计,催化剂的用量为0.001-0.1wt%,反应条件为20-100℃,氢气分压为0.5-30大气压,反应时间为1min至500hr。

著录项

  • 公开/公告号JPS6054931B2

    专利类型

  • 公开/公告日1985-12-03

    原文格式PDF

  • 申请/专利权人 ASAHI GLASS CO LTD;

    申请/专利号JP19810186826

  • 发明设计人 YASUDA ARATA;ARAI YOSHIMASA;ODA YOSHIO;

    申请日1981-11-24

  • 分类号C07C29/136;B01J23/00;B01J23/46;C07B61/00;C07C27/00;C07C29/145;C07C31/38;C07C67/00;

  • 国家 JP

  • 入库时间 2022-08-22 07:43:11

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