砷
硫黄
硫酸
过氧化氢
浸出(土壤学)
硫化氢
化学
硫化物
残留物(化学)
环境化学
冶炼
选择性浸出
粒径
浸出剂
硫化铜
铜
无机化学
湿法冶金
过氧化物
核化学
硫化物矿物
Mercury(编程语言)
氧化剂
体积流量
作者
Zhen Miao,Fei He,Yadong Zhang
标识
DOI:10.1002/slct.202501773
摘要
Abstract Arsenic‐containing sulfide residue from copper smelting is a kind of dangerous solid waste. However, the residue is also a recycling resource due to its numerous valuable components. Sulfuric acid‐hydrogen peroxide was used to leach containing‐arsenic sulfide residue, followed by the recovery of arsenic (As). The effects of temperature, dosage of hydrogen peroxide, the concentration of sulfuric acid, particle size, and solid‐to‐liquid ratio on sulfuric acid‐hydrogen peroxide leaching were investigated. The results show that the optimal leaching conditions were leaching time of 120 min, the temperature of 60 °C, H 2 O 2 dosage of 1 mL/g, H 2 SO 4 concentration of 200 g/L, particle size of 200 mesh, and solid‐to‐ liquid ratio of 1:4. Leaching rates for As and Cu were 98.42% and 97.57%, with As and Cu concentrations of 38.2 and 3.73 g/L in the leaching solution, respectively. During the reduction of As(V) using SO 2 in the leaching solution, the optimal conditions were SO 2 flow rate of 60 mL/min, reaction temperature of 10 °C, and reaction time of 2 h. The reduction efficiency of As(V) reached 95.75%, with the purity of As 2 O 3 achieving 98.71%. The overall recovery rate of As throughout the entire process was 90.67%.
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