Solvent extraction equilibrium of dysprosium(Ⅲ) from nitric acid solutions with 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester

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摘要 Inviewoftheimportanceofsolventextractionofrareearthmetalswiththeacidicorganophosphorousreagent,thedevelopmentofachemicallybasedmodelapplicabletohighconcentrationisdesired.Inthepresentstudy,theequilibriumdistributionofdysprosium(Ⅲ)betweenanaqueousnitricacidsolutionand2-ethylhexylphosphonicacidmono-2-ethylhexylester(PC88A)wasmeasuredintherangeofaninitialaqueousdysprosium(Ⅲ)concentrationfrom1.0×10-3to1.0×10-1kmol/m3andPC88Aconcentrationfrom0.16to0.65kmol/m3inShellsolD70asthediluent.Theobtaineddatawereanalyzedusingthechemicallybasedmodelinordertocorrelatetheequilibriumdistributionratios.Inthismodel,dysprosium(Ⅲ)wasassumedtobeextractedwiththePC88Adimerasa1:3complex,theactivitieswereconsideredfortheaqueousspecies,andtheeffectiveconcentrationofthePC88AdimerwascalculatedusingAlstad'sempiricalequation.Asaresult,theapparentextractionequilibriumconstantwasdeterminedtobe253(kmol·m-3)-2withanexcellentcorrelationbetweentheexperimentandcalculationresultsinthewiderangeofthelogarithmofthedistributionratiofrom-2to3.5.Inconclusion,themethodologyinthismodelwouldbeeffectiveforquantitativedescriptionofsolventextractionbehaviorofgeneralrareearthelementsaswellasdysprosium.
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出版日期 2010年04月14日(中国期刊网平台首次上网日期,不代表论文的发表时间)
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