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锌焙砂的选择性还原焙烧硫酸浸出工艺研究

侯栋科 彭兵 柴立元 彭宁 闫缓 胡明

有色金属科学与工程Issue(1):1-8,8.
有色金属科学与工程Issue(1):1-8,8.DOI:10.13264/j.cnki.ysjskx.2014.01.001

锌焙砂的选择性还原焙烧硫酸浸出工艺研究

Zinc recovery from zinc calcine by selective reduction roasting and acid leaching

侯栋科 1彭兵 1柴立元 2彭宁 1闫缓 2胡明1

作者信息

  • 1. 中南大学冶金与环境学院环境工程研究所,长沙 410083
  • 2. 国家重金属污染防治工程技术研究中心,长沙 410083
  • 折叠

摘要

Abstract

Zinc recovery from zinc calcine containing high content of iron by selective reduction roasting and acid leaching was investigated. Zinc ferrite in zinc calcine was selectively transformed to zinc oxide and magnetite under CO and CO2 atmosphere. The reduced zinc calcine was then leached with sulfuric acid for dissolving the soluble zinc in the leaching solution and leaving the iron in the residue as magnetite. The effects of reaction parameters of reduction roasting and sulfuric acid leaching on the recovery of zinc were studied and the reduced sample was analyzed by chemical analysis, XRD and SEM-EDS. Using the content of soluble zinc and ferrous iron as the evaluation index of the reduction roasting, the optimum conditions were obtained as follows: roasting temperature (750 ℃), roasting time (60 min), CO concentration (8 %) and CO/(CO+CO2) ratio (20 %). Under the optimum conditions, the content of soluble zinc in zinc calcine increased from 79.64 % to 91.75 %. With the leaching efficiency of zinc and iron as the evaluation index of the acid leaching, the best leaching conditions were obtained as follows:leaching temperature (normal temperature), leaching time (30 min), sulfuric acid concentration (90 g/L) and liquid to solid ratio (10∶1). The leaching efficiency of zinc and iron under this condition is 91.8%and 7.17%, respectively.

关键词

锌焙砂/铁酸锌/还原焙烧/浸出分离

Key words

zinc calcine/zinc ferrite/reduction roasting/leaching separation

分类

矿业与冶金

引用本文复制引用

侯栋科,彭兵,柴立元,彭宁,闫缓,胡明..锌焙砂的选择性还原焙烧硫酸浸出工艺研究[J].有色金属科学与工程,2014,(1):1-8,8.

基金项目

国家高技术研究发展计划(863计划)主题项目 ()

有色金属科学与工程

OACSTPCD

1674-9669

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