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Extraction of Zr(IV) from hydrochloric acid with tri-octyl amine and cyanex 921 in kerosene

International Journal of Minerals,Metallurgy and Materials 2013年第9期20卷 823-828页

作者： Bhikari Charan Bhatta Nandita Panda Sujata Mishra Department of Chemistry College of Engineering and Technology Biju Pattanaik University of Technology Department of Chemistry Institute of Technical Education and Research Siksha O Anusandhan Deemed to be University

This article reports the extraction of zirconium （IV） from aqueous HC1 solution by tri-octyl amine （TOA）, cyanex 921, and their binary mixture using kerosene as the diluent. The effect of some parameters on the extraction of Zr（IV） was investigated such as equilibration time, aqueous phase acidity, extractant molarity, chloride ion concentration, nature of diluents, and temperature. The extraction of Zr（IV） was found to be 99% from 7.5 M HC1 using the mixture of extractants containing 0.1 M TOA and 0.02 M cyanex 921 in kerosene. Kerosene was found to be the effective diluent for the extraction of Zr（IV） with the binary mixture of TOA and cyanex 921. The positive enthalpy change and positive entropy change in the binary extraction system show the endothermic process with an increase in entropy. Stripping of Zr（IV） from the loaded organic phase containing the mixture of TOA （0.1 M） and cyanex 921 （0.02 M） indicates that HNO3 and Na2CO3 are the best stripping agents.

关键词： zirconium solvent extraction hydrochloric acid tri-octyl amine cyanex 921 kerosene

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Solvent extraction of neodymium(Ⅲ) from acidic nitrate medium using cyanex 921 in kerosene

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Journal of Rare Earths 2012年第8期30卷 794-797页

作者： Nandita Panda Niharbala Devi Sujata Mishra Department of Chemistry Institute of Technical Education and Research Siksha 'O' Anusandhan deemed to be University

The extraction of neodymium（III） from acidic nitrate medium was investigated using cyanex 921 as extractant in kerosene. The metal concentration in the aqueous phase before and after extraction was determined spectrophotometrically by Arsenazo III method. The complete equilibration was achieved in 15 rain. The effects of shaking time, nitric acid concentration, nitrate concentration, extractant concen- tration, and temperature on the extraction were studied. The extraction of Nd（III） was found to increase very slowly with increase in concen- tration of HNO3 in the range of 0.001-3.008 mol/L and then decreased when 0.01 mol/L HNO3 was used. The percentage of extraction was increased with increase in nitrate concentration from 0.01M）.45 mol/L and then decreased when nitrate concentration increased to 0.5 mol/L. Quantitative extraction of Nd（III）（98%） was obtained from the aqueous phase containing 0.001 mol/L HNO3 and 0.1 mol/L KNO3 using 0.5 mol/L cyanex 921. On the basis of slope analysis, the extracted complex in the organic phase was proposed to be Nd（NO3）3.2cyanex 921. The extraction of Nd（III） was found to increase with increase in concentration of metal ion in the range of 0.0014）.05 mol/L from 0.001 mol/L HNO3 and 0.1 mol/L KNO3 with 0.1 mol/L cyanex 921. The percentage of extraction of neodymium was found to decrease with in- crease in temperature. From temperature variation studies, the negative value of AH indicated the extraction reaction to be exothermic and the negative value of AS indicated the formation of a stable complex, Almost 100% Nd（III） was recovered from the fully loaded organic phase using 0.002 mol/L H2SO4 and 0.01 mol/L HCl.

关键词： extraction neodymium(III) acidic nitrate cyanex 921 kerosene stripping rare earths

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Separation of copper and iron from chloride media using cyanex 921 in kerosene

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Journal of Central South University 2014年第5期21卷 1752-1755页

作者： Sanghamitra Pradhan Niharbala Devi Sujata Mishra Department of Chemistry Institute of Technical Education and ResearchSiksha'O'Anusandhan University

The extraction and separation of Cu(Ⅱ)and Fe(Ⅲ)from HCl media using cyanex 921 in kerosene were *** effect of shaking time,aqueous phase acid concentration,Fe(Ⅲ)/Cu(Ⅱ)concentration,cyanex 921 concentration,temperature and aqueous to organic phase ratio on the separation of Cu(Ⅱ)and Fe(Ⅲ)was studied using 0.1 mol/L cyanex 921 in *** separation was achieved from 2 mol/L HCl containing 0.001 mol/L Cu(Ⅱ)and 0.005 mol/L Fe(Ⅲ)with 0.1 mol/L cyanex 921 in *** separation of copper and iron was also possible from 5 mol/L HCl using 0.02 mol/L cyanex 921.

关键词： solvent extraction copper iron hydrochloric acid cyanex 921

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