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作 者:孙振 曾理 关文娟 张贵清 王应松 SUN Zhen;ZENG Li;GUAN Wen-juan;ZHANG Gui-qing;WANG Ying-song(School of Metallurgy and Environment,Central South University,Changsha 410083,China)
机构地区:[1]中南大学冶金与环境学院
出 处:《稀有金属与硬质合金》2018年第6期25-31,共7页Rare Metals and Cemented Carbides
基 金:国家自然科学青年基金(NSFC51404297)
摘 要:采用斜率法、恒摩尔法、饱和容量法研究从酸性硫酸盐溶液中用P204和4PC协同萃取镍的机理,并测定协萃反应的热力学平衡常数,得到协萃反应的焓变和熵变。结果表明,P204/4PC协同萃取镍的反应呈正协同效应,镍萃合物的结构为NiA2L2,且协萃过程为吸热反应,焓变和熵变分别为29.52J/mol和-6.53kJ/(mol·K)。采用P204与4PC协萃体系可显著提高酸性硫酸盐溶液介质中镍的选择性萃取效果。The mechanism of synergistic solvent extraction of nickel by P204 and 4PC from acidic sulfate solution was studied with slope method,constant molecale method and saturation extraction method,respectively. The thermodynamic equilibrium constant of the synergistic reaction was determined,and its enthalpy and entropy changes were also obtained.The results show that the combination of P204 with 4PC has a positive synergistic effect for nickel extraction,and the extracted complex is identified as NiA2L2.The synergistic solvent extraction is an endothermic reaction with enthalpy change of 29.52J/mol and entropy change of-6.53kJ/(mol·K).The synergistic solvent extraction system of P204and 4PC can obviously promote the selective extraction of nickel from acidic sulfate solution.
关 键 词:镍 协同溶剂萃取 选择性 P204 4PC 机理 热力学
分 类 号:TF804.2[冶金工程—有色金属冶金]
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