首页> 外国专利> THE MANUFACTURE OF SODIUM FLUORIDE AND SILICA GEL AS SOLID MATERIALS BY THE DECOMPOSITION OF SODIUM SILICO-FLUORIDE

THE MANUFACTURE OF SODIUM FLUORIDE AND SILICA GEL AS SOLID MATERIALS BY THE DECOMPOSITION OF SODIUM SILICO-FLUORIDE

机译:分解氟硅酸钠制得氟化钠和硅凝胶作为固体材料

摘要

1295760 Sodium flouride and silica gel ONODA CHEMICAL INDUSTRY CO Ltd 29 May 1970 [29 May 1969] 26108/70 Heading C1A Sodium fluoride and silica gel are produced by treating sodium fluorosilicate with an aqueous solution of ammonium hydroxide with vigorous agitation, the concentration of ammonium hydroxide in the reaction medium during the reaction being not greater than 5 wt. per cent and the total concentration of NH 4 SP+/SP after completion of the reaction being more than 7À5% calculated as NH 3 . In an embodiment of the invention, as illustrated by Fig. I, sodium fluosilicate, either in aqueous solution or as a fine powder, is introduced into a reactive vessel simultaneously with an aqueous solution of ammonium hydroxide and the mixture in the vessel is stirred vigorously at an elevated temperature for about one hour. The slurry discharged from the reactor, after settling is separated in a levigation apparatus and the separated slurries of SiO 2 and NaF filtered, washed, and dried. The filtrate in each case is a solution of ammonium fluoride. The ammonium hydroxide cone. is selected to give a final conc. of NH 4 SP+/SP after reaction greater than 7À5% and the conc. of free NH 3 during reaction is kept as low as possible. The slurry obtained from the process as described may be subsequently reacted with aqueous NaOH, Na 2 SO 4 , or NaCl to increase the yield of NaF and form an aqueous solution of NH 4 Cl, NH 4 OH or (NH 4 ) 2 SO 4 .
机译:1295760氟化钠和硅胶小野化学工业株式会社1970年5月29日[1969年5月29日] 26108/70标题C1A氟化钠和硅胶是通过在剧烈搅拌下(浓度为铵)的氢氧化铵水溶液处理氟硅酸钠制成的。反应期间反应介质中的氢氧化物含量不大于5重量%。反应结束后,NH 4 + 的总浓度大于7%,按NH 3计算,则总浓度大于7%。在本发明的一个实施方案中,如图1所示,将水溶液或细粉形式的氟硅酸钠与氢氧化铵水溶液同时引入反应容器中,并剧烈搅拌容器中的混合物。在高温下约一小时。沉降后,将从反应器中排出的浆料在悬浮设备中分离,并将分离的SiO 2和NaF的浆料过滤,洗涤并干燥。在每种情况下,滤液均为氟化铵溶液。氢氧化铵锥。选择给出最终浓度。反应后NH 4 + 的浓度大于75%且浓反应期间游离NH 3的含量保持尽可能低。从所述方法获得的浆料可以随后与NaOH,Na 2 SO 4或NaCl水溶液反应以增加NaF的产率并形成NH 4 Cl,NH 4 OH或(NH 4)2 SO 4的水溶液。 。

著录项

  • 公开/公告号IL34592D0

    专利类型

  • 公开/公告日1970-07-19

    原文格式PDF

  • 申请/专利权人 ONODA CHEM IND CO LTD;

    申请/专利号IL19700034592

  • 发明设计人

    申请日1970-05-25

  • 分类号C01B33/152;C01C1/16;C01D1/24;C01D3/02;

  • 国家 IL

  • 入库时间 2022-08-23 11:34:13

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