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首页> 外文期刊>RSC Advances >The kinetics and mechanism of solvent extraction of Pr(III) from chloride medium in the presence of two complexing agents with di-(2-ethylhexyl) phosphoric acid
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The kinetics and mechanism of solvent extraction of Pr(III) from chloride medium in the presence of two complexing agents with di-(2-ethylhexyl) phosphoric acid

机译:在两种二(2-乙基己基)磷酸络合剂存在下从氯化物介质中溶剂萃取extraction(III)的动力学和机理

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摘要

The extraction kinetics of Pr(III) from chloride medium containing two complexing agents lactic acid (HLac) and citric acid (H(3)cit) with di-(2-ethylhexyl) phosphoric acid (D2EHPA, H(2)A(2)) have been investigated by constant interfacial area cell with lamina flow. The influence of stirring speed, temperature, specific interfacial area, extractant and hydrogen ion concentrations on the extraction rate has been studied. It is concluded that the extraction of Pr(III) takes place at the liquid-liquid interface, while the extraction regime belongs to diffusion-controlled kinetics process. The extraction rate equation and the rate-determining step have been obtained under the experimental conditions, and the extraction rate constant is calculated. The interfacial reaction model is proposed based on the kinetic steps.
机译:从含两种络合剂乳酸(HLac)和柠檬酸(H(3)cit)与二-(2-乙基己基)磷酸(D2EHPA,H(2)A(2)的氯化物介质中提取Pr(III)的动力学))已通过具有层流的恒定界面区域单元进行了研究。研究了搅拌速度,温度,比界面面积,萃取剂和氢离子浓度对萃取速率的影响。结论是,Pr(III)的萃取发生在液-液界面,而萃取机理属于扩散控制的动力学过程。在实验条件下获得了萃取速率方程和速率确定步骤,并计算了萃取速率常数。基于动力学步骤,提出了界面反应模型。

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