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Extraction kinetics of cerium(IV) from sulfuric acid medium by the primary amine N1923 using a constant interfacial area cell with laminar flow

✍ Scribed by Jianjun Liu; Yanliang Wang; Deqian Li


Publisher
Wiley (John Wiley & Sons)
Year
2007
Tongue
English
Weight
164 KB
Volume
82
Category
Article
ISSN
0268-2575

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✦ Synopsis


Abstract

BACKGROUND: Thermodynamic studies on Ce(IV) extraction with primary amine N1923 demonstrate that primary amine N1923 is an excellent extractant for separation of Ce(IV) from Re(III). In order to clarify the mechanism of extraction and to optimize the parameters in practical extraction systems used in the rare earth industry, the extraction kinetics was investigated using a constant interfacial area cell with laminar flow in the present work.

RESULTS: The data indicate that the rate constant (k~ao~) becomes constant when stirring speed exceeds 250 rpm. The apparent forward extraction rate is calculated to be 10^−1.70^. The activation energy (E~a~) was calculated to be 20.5 kJ/mol from the slope of log k~ao~ against 1000/T. The minimum bulk concentration of the extractant necessary to saturate the interface (C~min~) is lower than 10^−5^ mol L^−1^.

CONCLUSION: Studies of interfacial tension and the effects of stirring rate and specific interfacial area on the extraction rate show that the extraction rate is kinetically controlled, and a mass transfer model has been proposed. The rate equation has been obtained as: − d[Ce(IV)]/dt = 10^−1.70^[Ce(IV)] [(RNH~3~)~2~SO~4~]^1.376^. The rate‐controlling step has been evaluated from analysis of the experimental results. Copyright © 2007 Society of Chemical Industry


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Mass transfer kinetics of neodymium(III)
✍ Wenwei He; Wuping Liao; Weiwei Wang; Deqian Li; Chunji Niu 📂 Article 📅 2008 🏛 Wiley (John Wiley & Sons) 🌐 English ⚖ 136 KB

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