| 注册
首页|期刊导航|化工进展|湿法炼铜浸出液萃取分离硫酸机理

湿法炼铜浸出液萃取分离硫酸机理

马海飞 廖亚龙 武敏 贾小宝 杨双宇

化工进展2024,Vol.43Issue(6):3410-3419,10.
化工进展2024,Vol.43Issue(6):3410-3419,10.DOI:10.16085/j.issn.1000-6613.2023-0756

湿法炼铜浸出液萃取分离硫酸机理

Extraction mechanism of sulfuric acid from copper leaching solution of hydrometallurgical process

马海飞 1廖亚龙 1武敏 1贾小宝 1杨双宇1

作者信息

  • 1. 昆明理工大学冶金与能源工程学院,云南 昆明 650093
  • 折叠

摘要

Abstract

In view of the high content of free sulfuric acid in the copper leaching solution in hydrometallurgical process,neutralization treatment is required before copper extraction,which not only consumes large alkaline reagents and high operating cost,but also causes metal ion loss.In this paper,a solvent extraction process for sulfuric acid recovery was proposed and the mass transfer mechanism of the selective extraction process of trioctylamine(TOA)-n-octanol system was studied.The results showed that the third phase would be produced by hydration during TOA extraction of sulfuric acid.After adding n-octanol,the third phase can be avoided due to the formation of hydrophobic complexation((R3NH)2(A)0.3(H2O)1.7SO4).Under the conditions that the organic phase composition was 45%TOA+10%n-octanol+45%260#solvent oil,the ratio of O∶A(ratio of organic phase to aqueous phase)was 1∶1,the temperature was 25℃,the oscillation speed was 200r/min and the reaction time was 10min,the single-stage extraction rate of sulfuric acid reached 90.21%and the three-stage countercurrent extraction rate can achieve more than 99%.The extraction rates of Cu2+,Fe2+and Zn2+were less than 2.7%,2.2%and 2.3%,respectively.The extraction process was an exothermic reaction and the calculated ∆H of the extraction reaction was-14.9kJ/mol.

关键词

萃取/分离/综合回收/湿法炼铜/三辛胺

Key words

extraction/separation/comprehensive recovery/copper hydrometallurgy/trioctylamine

分类

矿业与冶金

引用本文复制引用

马海飞,廖亚龙,武敏,贾小宝,杨双宇..湿法炼铜浸出液萃取分离硫酸机理[J].化工进展,2024,43(6):3410-3419,10.

基金项目

国家自然科学基金(21978122). (21978122)

化工进展

OA北大核心CSTPCD

1000-6613

访问量0
|
下载量0
段落导航相关论文