缓释硫化剂ZnS去除冶炼污酸中As(Ⅲ)的试验及动力学研究
CSTR:
作者:
作者单位:

1.昆明理工大学 冶金与能源工程学院, 云南 昆明 650093 ;2.微波能源与装备技术工程应用国家地方联合实验室, 云南 昆明 650093 ;3.昆明市特种冶金重点实验室, 云南 昆明 650093

作者简介:

张萌萌(1995—),女,河南开封人,硕士研究生,主要从事冶金新技术研究。

通讯作者:

中图分类号:

TF813;X758

基金项目:

云南省科技厅重点研发计划(202403AA080004); 云南省科技厅基础研究专项(202201AS070031); 云南省科技厅重大科技专项计划(202302AG050008)


Experimental and kinetic study on the removal of As(Ⅲ) from smelting waste acid by slow-release sulfiding agent ZnS
Author:
Affiliation:

1.Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, Kunming 650093 , China ; 2.National Local Joint Laboratory of Engineering Application of Microwave Energy and Equipment Technology, Kunming 650093 , China ;3.Kunming Key Laboratory of Special Metallurgy, Kunming University of Science and Technology, Kunming 650093 , China

Fund Project:

  • 摘要
  • |
  • 图/表
  • |
  • 访问统计
  • |
  • 参考文献
  • |
  • 相似文献
  • |
  • 引证文献
  • |
  • 资源附件
  • |
  • 文章评论
    摘要:

    冶炼污酸中含有大量砷,目前一般采用硫化-石灰中和铁盐法除砷,存在成本高、环境风险大、体系负担重等问题,问题出现的主要原因是硫化药剂在污酸中溶解度极高,难以与除砷速率形成完美匹配。本文提出了硫化锌缓释除砷技术,研究在E-pH分析的基础上进行了条件试验,并对ZnS除砷动力学进行研究,还根据反应产物的表征深度探究ZnS除砷机理,得到以下主要结论。在As-S-H2O体系中,当pH值小于2时,砷离子处于As2S3稳定存在区域;ZnS缓释剂除砷的优化工艺条件为S/As物质的量比7.5、反应温度80℃、反应时间240min,该条件下砷去除率达到98.42%,污酸砷含量由1017mg/L降低至16.04mg/L;ZnS去除污酸中砷的反应速率受混合扩散模型控制,反应表观活化能为28.29kJ/mol;ZnS为表面粗糙的球形颗粒,拥有较大比表面积,反应后污酸中的砷以As2S3沉淀的形式附着在ZnS表面。该工艺利用硫化锌溶解特性,在污酸中缓慢释放S2-除砷,既避免了钠离子的引入,降低体系负担,同时减少环境风险,而且有效实现了污酸中砷的去除,为污酸处理提供了新思路。

    Abstract:

    The smelting waste acid contains a large amount of arsenic. Currently, the conventional approach to arsenic removal involves the use of a sulfide-lime neutralization method for iron salts. However, this method is associated with high costs, environmental concerns, and a substantial burden on the system. The primary cause of these issues is the high solubility of the sulfide agent in the waste acid, which hinders its effectiveness in arsenic removal. This paper presents a slow-release arsenic removal technique using zinc sulfide (ZnS). The study is based on E-pH analysis of the test conditions, ZnS arsenic removal kinetics, and in-depth characterization of the reaction products to explore the ZnS arsenic removal mechanism. The main conclusions are as follows: In the As-S-H2O system, when the pH value is less than 2, arsenic ions are found to be in the stable existence region of As2S3. The most effective process conditions for arsenic removal by ZnS retardant are determined to be a S/As substance amount ratio of 7.5, a reaction temperature of 80℃, and a reaction time of 240 minutes. Under these conditions, the arsenic removal rate reaches 98.42%, and the arsenic content in the waste acid is reduced from 1017mg/L to 16.04mg/L. The reaction rate of ZnS in removing arsenic from waste acid follows a mixed diffusion model, with an apparent activation energy of 28.29kJ/mol. ZnS is a spherical particle with a rough surface and a large specific surface area, and arsenic in the waste acid adheres to the surface of ZnS in the form of As2S3 precipitation after the reaction. This process takes advantage of the dissolution characteristics of zinc sulfide, slowly releasing S2- to remove arsenic from the waste acid. It avoids the introduction of sodium ions, reduces the burden on the system, and lowers environmental risks, effectively removing arsenic from the waste acid. This provides a new approach for the treatment of waste acid.

    参考文献
    相似文献
    引证文献
引用本文

张萌萌, 李静, 董庆峰. 缓释硫化剂ZnS去除冶炼污酸中As(Ⅲ)的试验及动力学研究[J].中国有色冶金,2025,54(1):157-165.

复制
分享
相关视频

文章指标
  • 点击次数:
  • 下载次数:
  • HTML阅读次数:
  • 引用次数:
历史
  • 收稿日期:2024-08-26
  • 最后修改日期:
  • 录用日期:
  • 在线发布日期: 2025-12-18
  • 出版日期:
文章二维码