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Method of preparation of very pure chemical elements, in particular, the silicon from their halides

机译:从其卤化物制备非常纯净的化学元素,特别是硅的方法

摘要

PICT:0799876/III/1 A mixture of silicon tetrachloride and hydrogen is passed through a high-temperature reaction zone so as to cause the production of silicon and hydrogen chloride to a substantial extent, the silicon is allowed to deposit in said zone the gaseous reaction product, which consists of a mixture of hydrogen chloride and unreacted silicon tetrachloride and hydrogen, is removed from the reaction zone, the hydrogen chloride is removed from said mixture and further silicon tetrachloride and hydrogen added thereto to replace that used in the reaction, and the resulting mixture of silicon tetrachloride and hydrogen is recycled to the high temperature reaction zone. The silicon may be produced at a temperature of 1100-1300 DEG C., preferably 1200 DEG C. Removal of hydrogen chloride and addition of hydrogen may be effected simultaneously by reaction of the hydrogen chloride with vaporized zinc at a temperature of 600-800 DEG C., preferably 650 DEG C. As illustrated, silicon tetrachloride is introduced from reservoir 30 into the cyclic system after the high temperature reaction zone 31. Zinc vapour is then introduced into the system from zinc boiler 33. The zinc chloride thereby produced is removed by means of a cooling and settling chamber 34 and filter 35 of glass wool. The remaining hydrogen and silicon tetrachloride pass via pump 36 to reaction zone 31. Before passing to zone 31, a portion of the gases may pass continuously or intermittently through an analyser 37 consisting of an infra-red analysis unit or a thermal conductivity cell. Hydrogen for commencing the reaction, and for subsequent supplementary addition, if necessary, may be added via reaction tube 32. Silicon tetra chloride for use in the process may be purified by admixing with a solvent, e.g. dichloromethane, trichloromonofluoromethane, or trichlorotriflorethane, passing through activated alumina boiling off, condensing, and recycling the solvent (Fig. 2, not shown).
机译:使四氯化硅和氢的混合物通过高温反应区,以使硅和氯化氢的产生量大大增加,使硅沉积在所述区中从反应区中除去由氯化氢和未反应的四氯化硅与氢的混合物组成的气态反应产物,从所述混合物中除去氯化氢,再向其中加入四氯化硅和氢以代替反应中所用的产物。 ,然后将所得的四氯化硅和氢气的混合物再循环至高温反应区。硅可以在1100-1300℃,优选1200℃的温度下生产。脱氯化氢和添加氢可以通过使氯化氢与汽化锌在600-800℃的温度下反应同时进行。最好是650℃。如图所示,在高温反应区31之后,将四氯化硅从储罐30中引入循环系统中。然后从锌锅炉33中将锌蒸气引入该系统中。由此产生的氯化锌被除去。通过冷却和沉降室34和玻璃棉过滤器35。剩余的氢和四氯化硅通过泵36到达反应区31。在进入区31之前,一部分气体可以连续或间歇地通过由红外分析单元或导热池组成的分析仪37。可以通过反应管32加入用于开始反应以及随后必要时进行补充添加的氢。用于该方法的四氯化硅可以通过与溶剂例如二氯甲烷混合而纯化。二氯甲烷,三氯一氟甲烷或三氯三氟乙烷通过沸腾的活性氧化铝沸腾,冷凝并回收溶剂(图2,未显示)。

著录项

  • 公开/公告号FR1229718A

    专利类型

  • 公开/公告日1960-09-09

    原文格式PDF

  • 申请/专利号FR19580783066

  • 发明设计人

    申请日1958-12-31

  • 分类号C01B25/06;C01B33/02;C01B33/08;C01B35/02;C22B5;C22B5/16;C23C16/08;H01G9/04;H01G9/048;

  • 国家 FR

  • 入库时间 2022-08-23 19:09:42

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