PC-88A为流动载体的支撑液膜中Pt(Ⅳ)的迁移  被引量:1

Transport of Pt(Ⅳ) through a Supported Liquid Membrane with PC-88A as a Carrier

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作  者:姚秉华[1] 郭攀峰[1] 赵青[1] 

机构地区:[1]西安理工大学应用化学系,陕西西安710048

出  处:《分析测试学报》2008年第8期848-850,855,共4页Journal of Instrumental Analysis

基  金:西安市科技攻关项目(GG05074);陕西省教育厅科学研究基金资助项目(06JK215)

摘  要:研究了以烷基膦酸PC-88A为流动载体的聚偏氟乙烯支撑液膜中Pt(Ⅳ)的传输行为。考察了料液相盐酸浓度、解析相盐酸浓度、载体浓度、SnCl2浓度对Pt(Ⅳ)迁移的影响,获得了Pt(Ⅳ)迁移的最佳实验条件:料液相盐酸浓度为1.0 mol/L、解析相盐酸浓度为6.0 mol/L、载体质量分数为5.0%、SnCl2浓度为0.05mol/L。当料液相Pt(Ⅳ)初始质量浓度为1.0 mg/L时,在最佳实验条件下,Pt(Ⅳ)可在3 h内完全迁移。将本法用于含Pt(Ⅳ)(0.8 mg/L),Cu(Ⅱ)(75.0 mg/L),Zn(Ⅱ)(75.0 mg/L),Co(Ⅱ)(75.0 mg/L)和Ni(Ⅱ)(75.0 mg/L)的模拟试样中Pt(Ⅳ)的分离,取得了满意结果。The transport behavior of Pt ( Ⅳ ) through a supported liquid membrane, polyvinylidene fluoride ( PVDF), using 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester(PC-88A) as the mobile carrier has been studied. The effects of the concentration of HCl in feed and stripping phases, concentration of PC-88A in membrane, and concentration of SnCl2 in feed phase on the transport process of Pt(Ⅳ) have been studied. It was found that under optimum conditions: 1.0 mol/L HCl in feed phase, 6.0 mol/L HCl in stripping phase, 5.0% carrier concentration, 0. 05 mol/L SnC12, 1.0 mg/L Pt ( Ⅳ ) as initial concentraton, Pt ( Ⅳ ) could be completely transported in 3 h. This method has been used to separate Pt( Ⅳ ) in the simulated electroplating wastewater from the other elements : 0.8 mg/LPt(Ⅳ) , 75.0mg/LCu(Ⅱ) , 5.0mg/LZn(Ⅱ) , 75.0mg/L Co(Ⅱ) and 75.0mg/L Ni( Ⅱ ) with satisfactory result.

关 键 词:液膜分离 支撑液膜  烷基磷酸 PC-88A 

分 类 号:O614.826[理学—无机化学] TQ450.42[理学—化学]

 

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