选择性浸出硫化镍精矿中的镁  被引量:1

Selective Leaching of Magnesium from Nickel Sulfide Concentrate

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作  者:卢苏君[1,2] 杨粉娟 马天飞 豆银丽 

机构地区:[1]金川镍钴研究设计院,甘肃金昌737100 [2]兰州大学,兰州730000

出  处:《有色金属(冶炼部分)》2013年第7期23-26,共4页Nonferrous Metals(Extractive Metallurgy)

摘  要:采用硫酸选择性浸出高含镁硫化镍精矿,考察了加酸量、液固比、反应时间、反应温度对浸出率的影响。结果表明,在每千克精矿加入150mL浓硫酸、液固比1∶1、常温反应0.5h的条件下,镍、铜、钴浸出率分别为6.61%、6.67%、6.84%,精矿中MgO含量可以从10.80%降至5.57%,降镁后硫化镍精矿热值低于2 017MJ/t,浸出液加入硫化钠可将浸出液中镍、铜分别降至5.2mg/L、0.6mg/L以下。High magnesium bearing nickel sulfide concentrate was selectively leached by sulfuric acid.The effects of dosage of sulfuric acid,ratio of liquid to solid(L/S),reaction time and temperature on leaching rate were investigated.The results show that the leaching rate of nickel,copper,and cobalt is 6.61%,6.67%and 6.84%,respectively,and the MgO content is reduced from 10.80%to 5.57%under the optimum conditions including dosage of sulfuric acid of 150mL for one kilogram concentrate,L/S of 1∶1,and leaching time of 0.5hat room temperature.The smelting calorific value of de-magnesium nickel sulfide concentrate is less than 2 017MJ/t.The concentration of nickel and copper in lixivium is reduced to 5.2 mg/L and 0.6mg/L respectively after adding of sodium sulfide.

关 键 词:硫化镍精矿 酸浸 降镁 浸出率 硫化钠    

分 类 号:TF815[冶金工程—有色金属冶金]

 

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