首页|氧化锌烟尘浸出液中和沉淀—浸出分离富集锗

氧化锌烟尘浸出液中和沉淀—浸出分离富集锗

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湿法炼锌过程采用单宁沉锗回收锗的工艺,存在单宁消耗量大、单宁价格上涨导致锗回收成本高和单宁带入有机物对湿法炼锌系统产生不利影响等问题,本文以含锗氧化锌烟尘浸出液为原料,利用工业氧化锌烟尘为中和剂,开展中和沉淀—浸出分离富集锗的工艺研究。研究结果表明:通过两段逆流中和沉淀制备中和锗渣,在一段中和温度为45℃、时间为2。0 h、pH为4。0~4。5,二段中和温度为45℃、时间为1。5 h、通氧速率为60 L/h、pH为5。0~5。2的条件下,所得中和锗渣中锗的质量分数为1。34%,沉锗后液中锗的质量浓度为1。98 mg/L,锗沉淀率达99%以上;在浸出温度为150℃、时间为4。0 h、氧分压为0。7 MPa、终点硫酸质量浓度为30 g/L的条件下,中和锗渣中的锗、铁、砷和硅的浸出率分别为86。54%、23。74%、54。41%和10。53%,氧压浸出液中锗的质量浓度为1。80 g/L;与含锗氧化锌烟尘浸出液相比,氧压浸出液中锗的质量浓度为原液中的9。06倍,锗铁的质量浓度比由0。05提升至1。18、锗砷的质量浓度比由0。34提升至3。11、锗硅的质量浓度比由1。26提升至7。65;在浸出温度为90℃、时间为2。0 h、终点硫酸质量浓度为100 g/L的条件下,氧压浸出渣中的锗浸出率提升至95。31%。
Separation and enrichment of germanium in zinc oxide dust leaching solution by leaching after neutralizing precipitation
To solve the problems of recovery germanium by tannin precipitation method in the hydrometallurgy zinc process,such as high tannin consumption,the high costs for germanium recovery which is caused by rising price of tannin,and the adverse effects of tannin which brings in organics on the hydrometallurgy zinc system,the recovery process of germanium through leaching after neutralizing precipitation from zinc oxide dust leaching solution by industrial zinc oxide dust was studied.The results show that neutralized germanium precipitation is obtained through a two-stage countercurrent neutralization and precipitation process,under the conditions of the first-stage neutralization temperature of 45℃,time of 2.0 h,and pH of 4.0-4.5,and the second-stage neutralization temperature of 45℃,time of 1.5 h,oxygen flow rate of 60 L/h,and pH of 5.0-5.2.The germanium mass fraction of the neutralized germanium precipitation is 1.34%,the germanium mass concentration in the liquid of precipitated germanium is 1.98 mg/L,and the germanium precipitation rate is above 99%.Under the condition of leaching temperature of 150℃,time of 4.0 h,oxygen pressure of 0.7 MPa,and final sulfuric acid mass concentration of 30 g/L,the leaching rates of germanium,iron,arsenic,and silicon in the neutralized germanium precipitation are 86.54%,23.74%,54.41%and 10.53%,respectively.The germanium mass concentration in the oxygen pressure leaching solution is 1.80 g/L,which is 9.06 times of that in the original solution.The germanium-to-iron ratio increases from 0.05 to 1.18,and the germanium-to-arsenic ratio increases from 0.34 to 3.11.The germanium-to-silicon ratio increases from 1.26 to 7.65.Under the conditions of leaching temperature of 90℃,time of 2.0 h,oxygen-enriched atmosphere,and final sulfuric acid mass concentration of 100 g/L,the leaching rate of germanium in the oxygen pressure leaching residue increases to 95.31%.

neutralization and precipitationoxygen pressure leachingenrichment of germaniumseparation of impurity

甄勇、王梓澎、邓志敢、陆占清、魏昶、戴兴征、李兴彬

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昆明理工大学冶金与能源工程学院,云南昆明,650093

云南云铜锌业股份有限公司,云南昆明,650032

云南驰宏锌锗股份有限公司,云南曲靖,655011

中和沉淀 氧压浸出 富集锗 分离除杂

云南省科技人才计划项目云南省重大科技专项云南省重大科技专项昆明理工大学分析测试基金资助项目Science and Technology Talent Program of Yunnan ProvinceMajor Scientific and Technological Projects of Yunnan ProvinceAnalysis and Test Fund of Kunming University of Science and Technology

202405AC350015202202AG050008202302AB0800122022T20090030

2024

中南大学学报(自然科学版)
中南大学

中南大学学报(自然科学版)

CSTPCD北大核心
影响因子:0.938
ISSN:1672-7207
年,卷(期):2024.55(7)