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Improved process for the electrolytic decomposition of anhydrous magnesium chloride and the production of magnesium and chlorine

机译:改进的无水氯化镁电解分解工艺及镁和氯的生产

摘要

152,402. Ashcroft, E. A. July 9, 1919. Electrolytic furnaces. - Fused anhydrous magnesium chloride, free or practically so from other substances, is used as electrolyte in both a primary and a secondary cell. A body of lead-magnesium. alloy may form one electrode of each cell. The cells 1, 2, Fig. 1, may be connected in series by conductors x.All their upper parts the cast-iron or other cells may be protected from the electrolyte and chlorine by a lining 13 of fire-clay or magnesite brick. Each cell supports an insulated cover 11 carrying the upper electrodes and provided with charging holes for crystalline magnesium chloride, which may be prepared as described in Specification 152,401, [Class 1 (ii), Inorganic compounds other than &c.]. For a current of 5000 amperes there may be 20 graphite anodes 9, of about 3 in. diameter, immersed 3 in. in the electrolyte and 1 in. from the surface of the alloy. Connexion may be made by conductors 14, dipping into molten lead in holes in the cover and in the anodes. In the secondary cell, the cathodes may be carried by four separate subsidiary covers 15. For each cover there may be 70 iron or steel cathode rods, 10 of # in. diameter immersed ¢ in. in the electrolyte and ¥ in. distant from the alloy. Each subsidiary cover is connected to the main cover by a flexible conductor 16. On opposite sides of each cell are inlet and outlet walls 6, 7, Fig. 3, opening into the body of the cell through passages 4, 5. A weir 8 also interposed between the main bodv of the cell and the outlet well maintains the required level of the alloy. Preferably, electrolysis is carried on for, say, six hours without disturbance of the alloy. The small covers of the secondary cell are then removed successively, and the floating masses of molten magnesium ladled out, without interrupting the current. At intervals, preferably immediately after the removal of the metal, the alloy is transferred from one cell to the other, by ladling, or by communicating passages, or otherwise. A temperature of 750‹ C. is suitable for electrolysis; preferably there is used sufficient current to maintain this temperature. Specification 26813/05 also is referred to.
机译:152,402。 Ashcroft,E. A.,1919年7月9日。电解炉。 -无水或几乎不含其他物质的熔融无水氯化镁在一次电池和二次电池中均用作电解质。铅镁合金。合金可以形成每个电池的一个电极。电池1、2(图1)可以通过导体x串联连接。铸铁或其他电池的所有上部都可以通过耐火粘土或菱镁矿砖的衬里13加以保护,以免受电解质和氯的影响。每个电池支撑绝缘的盖11,该盖带有上部电极并设有用于结晶氯化镁的充电孔,其可以按照规范152,401 [1(ii)类,&c以外的无机化合物]中所述制备。对于5000安培的电流,可以有20个直径约3英寸的石墨阳极9,浸入电解质中3英寸,并浸入合金表面1英寸。可以通过将导体14浸入盖中和阳极中的孔中的熔融铅中来进行连接。在二次电池中,阴极可以由四个单独的辅助覆盖层15承载。每个覆盖层可以有70条铁或钢阴极棒,其中10条直径#英寸的直径浸入¢英寸,并且¥英寸与电解液隔开。合金。每个辅助盖通过挠性导体16连接到主盖。在每个电池的相对侧,分别是入口和出口壁6、7(图3),它们通过通道4、5进入电池的主体。堰8插在电解槽的主要部分和出口之间的孔也可保持所需的合金水平。优选地,电解进行例如六个小时而不会干扰合金。然后,依次取下二次电池的小盖子,并在不中断电流的情况下将熔融镁的漂浮物拉出。每隔一段时间,最好是在去除金属后立即,通过浇包或通过连通通道,或其他方式,将合金从一个孔转移到另一个孔。 750℃的温度适合于电解。优选地,使用足够的电流来维持该温度。也参考规范26813/05。

著录项

  • 公开/公告号GB152402A

    专利类型

  • 公开/公告日1920-10-11

    原文格式PDF

  • 申请/专利权人 EDGAR ARTHUR ASHCROFT;

    申请/专利号GB19190017247

  • 发明设计人

    申请日1919-07-09

  • 分类号C25C3/04;

  • 国家 GB

  • 入库时间 2022-08-24 12:55:27

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