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A process for the enrichment of the iron and the iron is not difficult to metals from sulfur iron and iron oxide support strength material

机译:铁和铁的富集过程并不难从硫铁和氧化铁支持强度材料中提取金属

摘要

PICT:0800647/III/1 Ores or concentrates containing iron sulphide are mixed with material containing iron oxide and fed through pipes 3 to a closed furnace 1 of refractory material and melted electrically by carbon electrodes 2 which project downwards through the roof of the furnace, to form a slag including silica, gangue (if any), alkaline earth (if any) and a minor portion of the iron, and a matte, which contains the major portion of the iron partly as FeS and partly as FeO, most of the copper and cobalt content (if any) and part of the zinc content. The furnace has an upper outlet 4 for the slag 8 and a lower outlet 5 for the matte 7 and, if desired, a separate outlet 6 for drawing off material from the bottom of the furnace. Reactions between the iron sulphides, iron oxides and the carbon of the electrodes 2 also produce a gaseous mixture containing zinc vapour, sulphur vapour, carbon dioxide, carbon monoxide, carbonyl sulphide and carbon disulphide. This gaseous mixture at about 500 DEG C. passes through outlet 11 and conduit 13 provided with feeding screw 14 for transporting dust which may be deposited on the wall, to electric filter 12 where zinc is removed from the gases which then pass out of the top of the filter 12 at about 400 DEG C. via pipe 15 to condenser 16 in which they are cooled down to about 130 DEG C. so that the sulphur is condensed out and removed at S. The gases pass through circulation fan 9 back to the furnace 1 through pipe 10 fitted with valve 20 which is throttled to maintain a pressure above atmospheric in the system. The resulting matte may be crushed, leached, for example with sulphuric acid, and the ferrous sulphate solution obtained electrolysed to recover the iron by the method described in Specification 650,202.
机译:将含硫化铁的矿石或精矿与含氧化铁的材料混合,并通过管道3送入密闭耐火材料炉1,并通过碳电极2电熔化,碳电极2向下穿过炉顶。熔炉中形成的炉渣包括硅石,脉石(如果有的话),碱土(如果有的话)和一小部分的铁,以及一种冰沙,其中的大部分铁是FeS,部分是FeO,大部分铜和钴含量(如果有)以及部分锌含量。该炉具有用于炉渣8的上部出口4和用于毛面7的下部出口5,并且如果需要的话,具有用于从炉底部抽出材料的单独的出口6。硫化铁,氧化铁和电极2的碳之间的反应还产生包含锌蒸气,硫蒸气,二氧化碳,一氧化碳,羰基硫和二硫化碳的气态混合物。该大约500℃的气态混合物通过出口11和带有供料螺杆14的导管13,供料螺杆14用于将可能沉积在壁上的粉尘输送到电过滤器12,在那里从气体中除去锌,然后从顶部排出锌。过滤器12在约400℃下通过管道15到达冷凝器16,在其中冷凝器冷却至约130℃,从而使硫在S处冷凝并除去。气体通过循环风扇9返回到冷凝器16。通过装有阀20的管道10将炉1加热,该阀20被节流以保持系统中的大气压以上。可以例如用硫酸将所得的磨砂粉碎,浸出,并通过规格650,202中所述的方法电解获得的硫酸亚铁溶液被电解以回收铁。

著录项

  • 公开/公告号DE1029842B

    专利类型

  • 公开/公告日1958-05-14

    原文格式PDF

  • 申请/专利权人 PYROR LIMITED;

    申请/专利号DE1956A026289

  • 发明设计人 AANNERUD SIGURD ARTHUR;MOSTAD EIGIL;

    申请日1956-12-29

  • 分类号C01G49;C21B15;C22B1;C22B4;C22B9/18;C22B15;C22B19/02;C22B23/02;

  • 国家 DE

  • 入库时间 2022-08-23 20:53:00

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