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仲钨酸B-胍盐沉淀法分离钨钼的过程研究 被引量:6
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作者 徐志昌 张萍 《中国钼业》 2016年第6期28-32,共5页
含钼仲钨酸-B钠盐溶液,不仅被萃取分离法而且被本文的沉淀分离法证明是分离钨-钼的最佳方法之一。本文采用硝酸胍为含钼仲钨酸B钠盐的沉淀剂,对沉淀剂硝酸胍的用量、沉淀pH值以及仲钨酸B浓度等参数进行了实验研究,并对滤液相与沉淀相中... 含钼仲钨酸-B钠盐溶液,不仅被萃取分离法而且被本文的沉淀分离法证明是分离钨-钼的最佳方法之一。本文采用硝酸胍为含钼仲钨酸B钠盐的沉淀剂,对沉淀剂硝酸胍的用量、沉淀pH值以及仲钨酸B浓度等参数进行了实验研究,并对滤液相与沉淀相中的金属钨和钼,进行了浓度与含量分析。分析结果表明,沉淀剂、硝酸胍用量为理论量的1.063-1.068倍;沉淀pH7.70-7.79,仲钨酸B浓度0.500-0.600 mol/L;温度20-30℃;沉淀时间0.75h;陈化时间2h等沉淀条件下,金属钨-钼间的分离系数达到B(w/Mo)=459.23-460.31。此外,采用高浓度的硝酸铵-氨水溶液,使仲钨酸B胍盐沉淀转化为硝酸胍与仲钨酸铵的最佳试剂。 展开更多
关键词 硝酸胍 -B -B胍盐沉淀 沉淀法分离- 酸胍盐沉淀率 钨-钼分离系数
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从栾川浮选钼尾矿中综合利用白钨矿的过程研究 被引量:8
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作者 徐志昌 张萍 《中国钼业》 2002年第5期5-9,共5页
针对由我国栾川浮选钼尾矿综合回收伴生、难选白钨矿的系统工程问题 ,其中包括锥型螺旋分级、重选和浮选联合选矿、酸性洗涤、搅拌交流电场碱分解以及蒸发 -结晶和离子交换化学分离等过程 ,进行了专题性和系统性研究 ;本文的重点是述说... 针对由我国栾川浮选钼尾矿综合回收伴生、难选白钨矿的系统工程问题 ,其中包括锥型螺旋分级、重选和浮选联合选矿、酸性洗涤、搅拌交流电场碱分解以及蒸发 -结晶和离子交换化学分离等过程 ,进行了专题性和系统性研究 ;本文的重点是述说尾矿的精密分级和白钨矿中的搅拌交流电场碱分解技术。 展开更多
关键词 综合利用 锥型螺旋分级 酸性洗涤 搅拌交流电场碱分解 钨-钼分离 尾矿
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Precursor solution prepared by evaporation deamination complex method for solvent separation of Mo and W by H_2O_2-complexation 被引量:7
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作者 关文娟 张贵清 高从堦 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2013年第4期1139-1146,共8页
An novel method on preparation of precursor solution for solvent separation of molybdenum (Mo) and tungsten (W) by hydrogen peroxide (H2O2)-complexation from the ammonium tungstate solution containing high Mo wa... An novel method on preparation of precursor solution for solvent separation of molybdenum (Mo) and tungsten (W) by hydrogen peroxide (H2O2)-complexation from the ammonium tungstate solution containing high Mo was studied. The precursor solution was obtained via evaporation deamination and H202-complex transformation processes. Then it was extracted with a mixture extractant of tri-alkyl phosphine oxide (TRPO) and tributyl phosphate (TBP) to separate Mo and W. The results indicated that the evaporation deamination complex method reduced the acid consumption by more than 90% in comparison with the traditional directly acid regulation complex method. The transformation rates of W and Mo were higher than 95% and the decomposition rate of H202 was less than 15% at a 1.8-1.9 times H202 dosage, 45-50 ℃, initial pH of 1.80-1.90, and transformation volume ratio of 100% for 60 min in the H2O2-complexation transformation process. The minimum extraction rate of W was 2%, the maximum extraction rate of Mo was 82.6% and the highest separation coefficient was 76.7 in a single-stage extraction. 展开更多
关键词 TUNGSTEN MOLYBDENUM solvent extraction separation precursor solution H202
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Removal of tungsten and vanadium from molybdate solutions using ion exchange resin 被引量:14
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作者 Xian-zheng ZHU Guang-sheng HUO +1 位作者 Jie NI Qiong SONG 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2017年第12期2727-2732,共6页
The removal of tungsten(W)and vanadium(V)from molybdate solutions was studied using the poly hydroxyl chelating resin D403in batch and column experiments.The batch experiments indicated that tungsten and vanadium coul... The removal of tungsten(W)and vanadium(V)from molybdate solutions was studied using the poly hydroxyl chelating resin D403in batch and column experiments.The batch experiments indicated that tungsten and vanadium could be preferentially adsorbed by the D403resin for4h in molybdate solution at a pH of approximately9.25.Separation factors,αVMo andαWMo,wereabove45and18,respectively,when the molar ratios of Mo/V and Mo/W in the solution exceeded40.Elution tests illustrated that vanadium and tungsten could be easily eluted from the resin with1mol/L sodium hydroxide solution in only1h.To further explore the sorption mechanism of the resin,the experimental equilibrium isotherm data of the three metals fitted well with the Freundlich model.The column experiments confirmed the adaptability of the D403resin in the production of sodium molybdate with a removal rate of tungsten surpassing90%and that of vanadium of99.4%. 展开更多
关键词 TUNGSTEN VANADIUM REMOVAL ion exchange MOLYBDATE
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