无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ

无机盐工业 ›› 2020, Vol. 52 ›› Issue (11): 69-74.doi: 10.11962/1006-4990.2019-0643

• 环境·健康·安全 • 上一篇    下一篇

氨法浸出锌冶金渣尘提锌工艺及动力学研究

马爱元(),郑雪梅(),李松   

  1. 六盘水师范学院化学与材料工程学院,贵州六盘水 553004
  • 收稿日期:2020-05-17 出版日期:2020-11-10 发布日期:2020-12-01
  • 通讯作者: 郑雪梅
  • 作者简介:马爱元(1988— ),男,博士,副教授,主要研究方向为冶金固体废弃物资源综合利用;E-mail: may_kmust11@163.com
  • 基金资助:
    贵州省教育厅科技拔尖人才支持项目(黔教合KY字[2018]066);贵州省科技厅技术基金项目(黔科合基础[2019]1444);六盘水市科技计划项目(52020-2018-0304);六盘水市科技计划项目(52020-2019-05-08);六盘水市科技计划项目(52020-2019-05-09);六盘水师范学院科技创新团队(LPSSYKJTD201801);六盘水师范学院科技创新团队(LPSSYKJTD201905);六盘水师范学院重点学科建设项目(LPSSYZDPYXK201708);卓越工程师培养计划项目(LPSSYzyjypyjh201801)

Study on leaching process and kinetics of zinc extraction from metallurgical slag and dust with ammonia

Ma Aiyuan(),Zheng Xuemei(),Li Song   

  1. School of Chemistry and Materials Engineering,Liupanshui Normal University,Liupanshui 553004,China
  • Received:2020-05-17 Online:2020-11-10 Published:2020-12-01
  • Contact: Zheng Xuemei

摘要:

锌冶金渣尘作为一种重要的锌二次资源,来源广、储量大、具有较高的综合回收利用价值。以NH3-CH3COONH4-H2O为浸出体系,考察粒度、反应时间、搅拌速度、液固比、总氨浓度、NH3与NH4+物质的量比和温度对锌浸出率的影响,结果表明:控制浸出温度为25 ℃、总氨浓度为5 mol/L、液固体积质量比为5 mL/g、n(NH3)/n(NH4+)=1:1、搅拌速度为300 r/min、浸出时间为60 min,在此条件下锌的浸出率可达84%。含锌冶金渣尘浸出动力学分析显示,浸出反应表观活化能为22.66 kJ/mol,锌浸出过程的浸出速率受固体膜层扩散及界面化学反应共同控制,并获得了浸出锌的动力学速率方程。

关键词: 锌, 冶金渣尘, 氨法浸出

Abstract:

Zinc metallurgical slag and dust is an important secondary resource,it has the advantages of wide source,large re-serves and high comprehensive recycling value.The influence of particle size,reaction time,stirring speed,liquid-solid ratio,total ammonia concentration,amount-of-substance ratio of NH3 to NH4+ and temperature on the zinc leaching rate were investi-gated in NH3-CH3COONH4-H2O system.The results showed that the control leaching temperature of 25 ℃,total ammonia co-ncentration of 5 mol/L,liquid-solid volume-mass ratio of 5 mL/g,amount-of-substance ratio of n(NH3)/n(NH4+)=1:1,stirring speed of 300 r/min and leaching time for 60 min,then the zinc leaching rate reached 84%.The leaching kinetic analysis of metallurgical slag and dust indicated that the apparent activation energy of the reaction was 22.66 kJ/mol.The leaching rate of zinc was controlled by both solid film diffusion and interfacial chemical reaction,and the kinetic rate equation of zinc leaching was obtained.

Key words: zinc, metallurgical slag and dust, ammonia leaching

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