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Production of aluminum fluoride by thermal decomposition of aluminum double fluorides

机译:通过热分解双氟化铝生产氟化铝

摘要

In the production of aluminium fluoride, solid aluminium hydrate is intimately mixed with such an amount of a solid acid fluoride salt of ammonia that it contains at least six and preferably twelve atoms of fluorine for each molecule of alumina used, and the mixture heated at 100--200 DEG C., until a double aluminium ammonium fluoride is formed, after which the temperature is gradually raised to 500--600 DEG C., to decompose the double salt and yield anhydrous aluminium fluoride. If desired, the second heating step may be omitted and the double fluoride recovered as such. The initial materials may contain free or hygroscopic moisture. Vapours evolved in the second heating step are collected and reformed into ammonium acid fluoride for re-use by combination with hydrofluoric acid; for instance they may be first passed through aluminium hydrate to remove ammonium acid fluoride and then into aqueous hydrofluoric acid. The ammonium acid fluoride may be prepared in situ as by using normal ammonium fluoride in the initial mixture, or by mixing aluminium hydrate with an ammonium compound such as the carbonate, and heating the mixture in the presence of hydrofluoric acid gas. The process may be carried out continuously in an externally heated rotating tube having a temperature gradient of 150--600 DEG C., which contains initially a charge of ammonium acid fluoride. Hydrate of alumina is fed into the cool end of the tube and hydrofluoric acid at the hot end. In the furnace the double salt is first formed and then decomposed at higher temperatures, and the vapours evolved react with the hydrofluoric acid to form ammonium acid fluoride which condenses at the cool end of the tube and reacts with further supplies of aluminium hydrate. The process may be carried out in aluminium vessels, or in the case of the continuous process, also in vessels constructed of iron or steel.
机译:在生产氟化铝时,将固态水合铝与一定量的固态氨氟化氟盐紧密混合,以使所用的每个氧化铝分子均含有至少六个,优选十二个氟原子,并将混合物加热至100℃。在-200℃下,直到形成双氟化铝铵,然后将温度逐渐升高到500-600℃,以分解该双盐并得到无水氟化铝。如果需要,可以省略第二加热步骤,并照这样回收双氟化物。初始材料可能包含游离或吸湿的水分。收集在第二加热步骤中产生的蒸气,并与氢氟酸混合重整为氟酸铵,以重复使用。例如,可以先使它们通过水合铝以除去氟化铵,然后进入氢氟酸水溶液。可以通过在初始混合物中使用普通氟化铵,或通过将水合铝与铵化合物(例如碳酸盐)混合,然后在氢氟酸气体的存在下加热混合物,来原位制备氟化氟铵。该方法可以在温度梯度为150--600℃的外部加热的旋转管中连续进行,该管最初含有一定量的氟化铵。将氧化铝的水合物送入管的冷端,并在热端送入氢氟酸。在熔炉中,首先形成复盐,然后在较高的温度下分解,放出的蒸气与氢氟酸反应生成氟化铵,该氟化铵在管的冷端冷凝并与水合铝的进料反应。该过程可以在铝制容器中进行,或者在连续过程的情况下,也可以在由铁或钢制成的容器中进行。

著录项

  • 公开/公告号DE641230C

    专利类型

  • 公开/公告日1937-01-25

    原文格式PDF

  • 申请/专利权人 THE BRITISH ALUMINIUM COMPANY LIMITED;

    申请/专利号DE1934B166466D

  • 发明设计人

    申请日1934-08-10

  • 分类号C01F7/00;C01F7/50;C01F7/54;

  • 国家 DE

  • 入库时间 2022-08-24 05:48:52

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