Solvent extraction of lanthanum and cerium ions from hydrochloric acidic aqueous solutions using partly saponified 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester
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Solvent extraction of lanthanum and cerium ions from hydrochloric acidic aqueous solutions using partly saponified 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester
Chinese Journal of Chemical EngineeringVol. 24, Issue 1, Pages: 79-85(2016)
Affiliations:
2 The State Key Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University,Beijing,China,100084
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Published:2016
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Hailong Hou, Jianhong Xu, Yundong Wang, Jinnan Chen. Solvent extraction of lanthanum and cerium ions from hydrochloric acidic aqueous solutions using partly saponified 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester[J]. Chin.J.Chem.Eng., 2016, 24(1): 79-85.
DOI:
Hailong Hou, Jianhong Xu, Yundong Wang, Jinnan Chen. Solvent extraction of lanthanum and cerium ions from hydrochloric acidic aqueous solutions using partly saponified 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester[J]. Chin.J.Chem.Eng., 2016, 24(1): 79-85.DOI:
Solvent extraction of lanthanum and cerium ions from hydrochloric acidic aqueous solutions using partly saponified 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester
摘要
Abstract
In order to clarify the extraction process with saponified extractant
the solvent extraction experiments of rare earth elements (REEs)
lanthanum and cerium
by using partly saponified 2-ethylhexyl phosphoric acid mono-2-ethylhexyl ester (EHEHPA
HL) from hydrochloric acidic solutions have been performed. The concentration of initial aqueous rare earth ion was in a range of 0.0010-0.1000 mol·L
-1
; EHEHPA in a range of 0.2877-0.8631 mol·L
-1
with saponification rate of 0.3 (mole fraction)
and the initial aqueous pH in a range of 1.00-4.00. Firstly
the extracted species were determined by the saturation extraction capacity method. Secondly
according to the equilibrium aqueous pH values
the extraction processes were divided into three different categories: extraction with saponified EHEHPA
extraction with un-saponified EHEHPA
and hydrolysis process. Finally
for the first two processes
in order to predict the distribution ratio
two semi-empirical calculation models were developed with. The calculation results are in good agreement well with the experimental data.
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