首页> 外国专利> Reductive roasting process for nickel-bearing laterite ores.

Reductive roasting process for nickel-bearing laterite ores.

机译:含镍红土矿石的还原焙烧工艺。

摘要

1392825 Reduction reacting nickeliferous laterite ore SHERRITT GORDON MINES Ltd 29 March 1972 [3 May 1971] 14897/72 Heading C1A Nickel values, leachable in aqueous solution, are recovered from nickeliferous laterite ore by H 2 reduction roasting the ore in a multiple hearth furnace heated by the partial combustion of fuel in which the H 2 concentration of the gases in the lower half of the reduction zone, supplied by H 2 gas introduced through the bottom of the reduction zone, is 25% (e.g. 30-45%), and the concentration in the gases exiting from the furnace is 3% (e.g. 6-8%), the rate of ore throughput being such that depth of ore on each furnace hearth is 0À05- 0À085 inch for each minute of ore residence time within the furnace; the reduced ore then being cooled (e.g. in a non-oxidizing atmosphere), and recovered, e.g. in aqueous ammoniacal (NH 4 ) 2 CO 3 solution. The ore may be pre-heated prior to reduction in the upper part of the furnace to a temperature of 1250‹ F. at a rate of 35-80‹ F./min. when the ore is a limonite (40% Fe) or to a temperature of 1350‹ F. at a rate of 35-70‹ F./min. when the ore is a serpentine or garnieritic ore (40% Fe) and then the ore maintained within Œ25‹ F. of this temperature in its passage down the furnace. The gas temperature across any hearth may #1450‹ F. Air may be injected through a series of nozzles around the periphery of the furnace into the preheat zone to burn the excess reductants contained in the partially combusted fuel gases and thereby control the per cent H 2 in the exit gases. The H 2 is preferably injected in at two points on opposite sides of the lowermost hearth. The hot combustion gases may be injected into the furnace through a plurality of vertically spaced conduits.
机译:1392825还原反应的含镍红土矿石SHERRITT GORDON MINES Ltd 1972年3月29日[1971年5月3日] 14897/72品目C1A在多炉膛加热的情况下,通过H 2还原焙烧矿石,从含镍红土矿石中回收可浸出的镍值。通过燃料的局部燃烧,其中通过还原区底部引入的H 2气体提供的还原区下半部分气体中的H 2浓度> 25%(例如30-45%),并且从熔炉中排出的气体中的浓度> 3%(例如6-8%),矿石通过量的变化应使每个熔炉炉床内每分钟的矿石停留时间为0-05--0-085英寸炉子;然后将还原的矿石冷却(例如在非氧化气氛中),并回收,例如将其还原。在氨水(NH 4)2 CO 3水溶液中。矿石可以在炉膛上部以35-80°F / min的速度还原到1250°F之前进行预热。当矿石是褐铁矿(铁含量> 40%)或以35-70?F / min的速度升至1350?F时。当矿石是蛇纹石或铁镍矿(<40%Fe),然后矿石在通过炉子时保持在该温度的25°F之内。跨任何炉床的气体温度可能为#1450 ‹F。可以通过围绕炉子外围的一系列喷嘴将空气注入预热区,以燃烧部分燃烧的燃料气体中所含的过量还原剂,从而控制H百分比2排出气体。优选在最低炉床的相对两侧的两个点处注入H 2。可以通过多个垂直间隔的导管将热的燃烧气体注入炉中。

著录项

  • 公开/公告号OA04006A

    专利类型

  • 公开/公告日1979-09-15

    原文格式PDF

  • 申请/专利权人 SHERRITT GORDON MINES LTD;

    申请/专利号OA19720054555

  • 发明设计人

    申请日1972-04-29

  • 分类号C22B23/00;

  • 国家 OA

  • 入库时间 2022-08-22 20:38:27

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