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Recovery of zinc from ore or concentrate - involves thermal treatment in fluidised bed before forming soln. for further treatment

机译:从矿石或精矿中回收锌-涉及在形成锡之前在流化床中进行热处理。进一步治疗

摘要

Zinc is recovered from ores and sulphated concentrates contg. iron sulphate by (a) calcining in a fluidised bed at 620-700 deg.C with 20-60% stoichiometric excess of air, mean retention time over 1 hr. and gas velocity 25-150 cm/sec. to obtain a calcined prod. contg. zinc mainly as sulphate and oxy-sulphate, and iron mainly as haemalite, (b) lixiviating with water or dil. sulphuric acid at below 80 deg.C to partially extract the zinc cpds., (c) separating the liq. for recovery and purification of the zinc, (d) lixiviating the residue with hot conc. sulphuric acid soln. at above 80 deg.C so that most of the zinc ferrite and sulphide are converted to zinc sulphate and iron sulphate which dissolve, (e) separating the soln. and (f) recycling this to the fluidised bed, (g) washing the solid residue from (e) with water, (h) separating the soln. and (i) recycling this partially to stage (b) and/or the fluidised bed.
机译:从矿石和硫酸精矿中回收锌。 (a)在流化床中于620-700℃下煅烧,化学计量过量的空气为20-60%,平均保留时间超过1小时。气体速度为25-150厘米/秒。获得煅烧的产品。续锌主要为硫酸盐和硫酸硫酸盐,铁主要为赤铁矿,(b)用水或稀水溶解。在低于80摄氏度的温度下用硫酸将锌cpds部分萃取出来。(c)分离液用于回收和纯化锌,(d)用热浓溶液浸提残留物。硫酸溶液。在高于80℃的温度下,使大部分的铁氧体锌和硫化物转化为溶解的硫酸锌和硫酸铁,(e)分离出溶液。 (f)将其循环到流化床中,(g)用水将(e)中的固体残留物洗净,(h)分离溶液。 (i)将其部分再循环至阶段(b)和/或流化床。

著录项

  • 公开/公告号ES8504950A1

    专利类型

  • 公开/公告日1985-07-16

    原文格式PDF

  • 申请/专利权人 PROVINCIAL HOLDINGS LTD.;

    申请/专利号ES19830527405

  • 发明设计人

    申请日1983-11-19

  • 分类号C22B3/00;

  • 国家 ES

  • 入库时间 2022-08-22 08:06:02

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