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作 者:杨绍文[1,2] 曹耀华[1,2] 高照国[1,2] 刘红召[1,2] 李琦[1,2]
机构地区:[1]中国地质科学院郑州矿产综合利用研究所,河南郑州450006 [2]国家非金属矿资源综合利用工程技术研究中心,河南郑州450006
出 处:《湿法冶金》2011年第1期33-36,共4页Hydrometallurgy of China
基 金:国土资源大调查项目子课题之一(121201066120113)
摘 要:针对河南淅川页岩钒矿分级擦洗得到的钒精矿,研究了两段逆流硫酸浸出—中和—还原—萃取—铵盐沉钒新工艺。在矿石w(V2O5)=2.50%、粒度-500目、硫酸用量为矿石质量的50%、浸出液固体积质量比1.3∶1、浸出温度95℃条件下,五氧化二钒浸出率大于75%;浸出液中的钒用15%P204+10%TBP+75%磺化煤油溶液为有机相,在常温下5级逆流萃取,有机相与水相的流量比为1∶1,钒萃取率在98%以上;负载有机相中的钒用1.5 mol/L硫酸溶液在常温下5级逆流反萃取,有机相与水相流量比为5∶1,钒反萃取率在99%以上;反萃取液中的钒氧化后用铵盐沉淀多钒酸铵,然后在氧化气氛中热解2 h,获得五氧化二钒产品。五氧化二钒总回收率大于70%,产品纯度大于99%。此工艺钒回收率高,符合环保要求,有一定的推广应用前景。Aiming at vanadium concentrates produced by scrubbing-classification,a new vanadium extraction process that two stage counter-current leaching—neutralization—reduction—solvent extraction—vanadium precipitate by ammonium salt was researched.The leaching rate was higher than 75% when the particle size of raw material was-500 mesh,dosage of sulfuric was 50% to ore mass,ratio of liquid to solid was of 1.3∶1 and leaching temperature was of 95℃.Vanadium in leaching solution was extracted using a mixed organic phase made up of 15%P204+10%TBP+75%sulfonated kerosene.At the conditions of nomal temperature,five stage counter-current extraction,flow rate of organic phase to liquid phase of 1∶1.The extraction rate of vanadium was more than 98%.Vanadium in loaded organic phase was five stage counter-current stripping using 1.5 mol/L sulfuric acid at the conditions of nomal temperature,flow ratio of organic phase to water phase of 5∶1.The stripping rate of vanadium was more than 99%.Vanadium in stripping solution was oxidized then deposited using ammonium salt.The ammonium polyvanadate was pyrolyzed in oxadition ambience to V2O5 product.The total recovery rate of V2O5 was more than 70% and the purity of V2O5 product was more than 99%.The hydrometallurgical process had high vanadium recovery,accorded with environment protection quirement,and had a good application prospect.
分 类 号:TF803.2[冶金工程—有色金属冶金] TF841.3
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