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Process for the production of carbides such as titanium carbide, boron carbide or zirconium carbide

机译:生产碳化物如碳化钛,碳化硼或碳化锆的方法

摘要

PICT:0777013/III/1 Hard carbides are produced from a mixture of carbon and the oxide of the element the carbide of which is to be produced, by electric arc heating in an electric furnace comprising two electrodes capable of up and down movement and a carbon or graphite bridge, each electrode making arcing contact initially with the carbon bridge and then with carbide which builds up on the bridge in the form of two ingots, with little or no formation of liquid, as the reaction proceeds. The ratio of the cross sectional area of the bridge to the diameter or equivalent diameter of the electrodes may be 2:12. The applied voltage may be 50-160 volts. The production of titanium, zirconium and boron carbide, and proportions of carbon to oxide of 1-2 to 1, 0.7-1.5 to 1, and 0.6-1 to 1 respectively are specified. The oxide may be in the form of ore, e.g. rutile, zircon or baddeleyite. Unconverted or partially converted oxide from a previous operation may be mixed with fresh oxide. As shown, the furnace comprises two electrodes 80 and an oval-shaped shell 20 supported on a base 66 around an inner container 67 and cooled by sprays of water supplied at inlets 57-60. A concave layer of fine carbon and pitch is formed in the inner container 67 and refrectory non-electrically conducting oxide material is packed between the container 67 and the shell 20. A layer of oxide material is then added to a height of ca. 4 inches above the top of container 67. The oxide material may be the same as is used in the reduction process, unconverted or partly converted material from a previous operation or other oxide material, e.g. alumina (in the production of boron carbide). In a trough in the oxide material is then placed a bridge of graphite or carbon of length equal to the distance between the electrodes. The furnace is wheeled beneath the electrodes which are then lowered into position. A layer of mixture to be heated is then placed in the furnace to a depth of 1-3 inches and a current passed through the electrodes. In operation automatic control mechanism raises and lowers the electrodes, maintaining arcs with a current flow of ca. 8,000 amps., and additional mixture is introduced as carbide is formed. The layer of mixture may be maintained 1-3 inches deep in the area of the electrodes, measured from the bottom of the electrodes. After completion of a run the electrodes are raised, the furnace wheeled away, allowed to cool while the water spray is maintained, and the shell lifted. Three phase power may be used instead of single phase power, using three electrodes and a round or trilobed furnace shell. Specification 747,834 [Group XXXVI] is referred to.
机译:硬质碳化物是由碳和将要生成碳化物的元素的氧化物的混合物制成的,方法是在包括两个能够上下移动的电极的电炉中通过电弧加热进行电弧加热碳和石墨桥,每个电极起弧时先与碳桥接触,然后与碳化物接触,随着反应的进行,碳化物以两个铸锭的形式堆积在桥上,很少或没有形成液体。桥的横截面积与电极的直径或等效直径的比可以为2:12。施加的电压可以是50-160伏。规定了钛,锆和碳化硼的生产,碳与氧化物的比例分别为1-2比1、0.7-1.5比1和0.6-1比1。氧化物可以是矿石的形式,例如铁矿石。金红石,锆石或baddeleyite。来自先前操作的未转化或部分转化的氧化物可以与新鲜氧化物混合。如图所示,该熔炉包括两个电极80和椭圆形的壳20,该椭圆形的壳20支撑在内部容器67周围的基座66上,并由在入口57-60处供应的水喷雾冷却。在内部容器67中形成有细碳和沥青的凹层,并且在容器67和壳体20之间填充了非导电性的氧化物导电材料。然后,将氧化物材料的层添加至大约200埃的高度。氧化物材料可以在容器67的顶部上方4英寸处。氧化物材料可以与还原过程中所使用的材料相同,可以是来自先前操作的未转化的或部分转化的材料,或者可以是其他氧化物材料。氧化铝(在碳化硼生产中)。然后在氧化物材料的槽中放置长度等于电极之间距离的石墨或碳桥。炉子在电极下方旋转,然后放下到位。然后将待加热的混合物层放置在炉中至1-3英寸的深度,电流通过电极。在操作中,自动控制机构会升高和降低电极,并以约200毫安的电流保持电弧。 8,000安培,并在形成碳化物时引入其他混合物。从电极底部开始测量,混合物层可以在电极区域中保持1-3英寸深。运行结束后,将电极举起,将炉子转开,使其冷却,同时保持水喷雾,并提起炉壳。使用三个电极和圆形或三叶形炉壳,可以使用三相电源代替单相电源。参见规格747,834 [XXXVI组]。

著录项

  • 公开/公告号GB777013A

    专利类型

  • 公开/公告日1957-06-12

    原文格式PDF

  • 申请/专利权人 NORTON GRINDING WHEEL COMPANY LIMITED;

    申请/专利号GB19550024816

  • 发明设计人

    申请日1955-08-30

  • 分类号B23Q11/06;C01B31/30;

  • 国家 GB

  • 入库时间 2022-08-23 22:11:02

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