The process and mechanism for cesium and rubidium extraction with saponified 4-tert-butyl-2-(α-methylbenzyl) phenol
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The process and mechanism for cesium and rubidium extraction with saponified 4-tert-butyl-2-(α-methylbenzyl) phenol
Chinese Journal of Chemical EngineeringVol. 46, Issue 6, Pages: 31-39(2022)
Affiliations:
1. Key Laboratory of Comprehensive and Highly Efficient Utilization of Salt Lake Resources, Qinghai Institute of Salt Lakes, Chinese Academy of Sciences,Xining,China,810008
2. University of Chinese Academy of Sciences,Beijing,China,100049
Author bio:
Funds:
DOI:
CLC:
Published:2022
Accepted:
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DOI:
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The process and mechanism for cesium and rubidium extraction with saponified 4-tert-butyl-2-(α-methylbenzyl) phenol
Cesium (Cs) and rubidium (Rb) separation from brine is an important and application-oriented topic. 4-tert-butyl-2-(
α
-methylbenzyl) phenol (
t
-BAMBP) has been used for Cs and Rb extraction. However
the traditional extraction technology is base and acid consumed. In the present work
an innovative process for Cs and Rb extraction with
t
-BAMBP is developed
which consists of saponification
extraction
scrubbing and stripping. Both infrared spectrum and electrostatic potential analysis indicate the hydrogen of phenolic hydroxyl is dissociated from
t
-BAMBP during saponification and the oxygen of phenolic hydroxyl is the binding site for alkali metal ions. Saponified organic phase shows an excellent extraction effect for Cs
+
and Rb
+
. The extraction reaches equilibrium in 5 min
with 99.5% Cs
+
and 46.7% Rb
+
are loaded into the organic phase in the single-stage extraction. Slope method indicates the structure of the extraction complex is MOR·3ROH (M = Cs
+
Rb
+
K
+
)
where the electrostatic attraction between M
+
and the oxygen of phenolic hydroxyl is dominant
and the cation–π interaction has a significant effect also. The extraction complex of MOR·3ROH dissociates in the acid environment while scrubbing and stripping is completed. The Cs
+
and Rb
+
are separated from the mixture phase
the proton H bonds to the phenolic hydrox
yl group
and the extractant is regenerated.
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Recovery rubidium chloride and cyclic utilization of hexacyanoferrate(II) ion from hexacyanoferrate-internediate solutions via solvent extraction
Environmental, economic and exergy analysis of separation of ternary azeotrope by variable pressure extractive distillation based on multi-objective optimization
Catalytically active membranes for esterification: A review
Thermodynamical and catalytic aspects of zinc separation from aqueous solution
Extraction of rubidium by t-BAMBP in cyclohexane
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