Selective Extraction of U(VI) by Counter-Current Liquid-Liquid Extraction withN,N-di(2-Ethylhexyl)-2,2-Dimethylpropanamide

2011 ◽  
Vol 29 (4) ◽  
pp. 519-533 ◽  
Author(s):  
Yasutoshi Ban ◽  
Shinobu Hotoku ◽  
Yasuji Morita
Keyword(s):  
Selective Extraction ◽  
Liquid Extraction ◽  
Liquid Liquid Extraction ◽  
Counter Current

scholarly journals Tantalum and Niobium Selective Extraction by Alkyl-Acetophenone

Metals ◽  
2018 ◽  
Vol 8 (9) ◽  
pp. 654 ◽  
Author(s):  
Moussa Toure ◽  
Guilhem Arrachart ◽  
Jean Duhamet ◽  
Stephane Pellet-Rostaing
Keyword(s):  
Extraction Efficiency ◽  
Methyl Isobutyl Ketone ◽  
Selective Extraction ◽  
Extraction Process ◽  
Liquid Extraction ◽  
Methyl Isobutyl ◽  
Isobutyl Ketone ◽  
Waste Solution ◽  
Liquid Liquid Extraction ◽  
D Values

A study has been carried out on Ta and Nb recovery by a liquid-liquid extraction process using 4-methylacetophenone (4-MAcPh) as the organic phase. The 4-MAcPh was compared to methyl isobutyl ketone (MIBK) with respect to extraction efficiencies (D values) at different concentrations of H2SO4 in the aqueous phase. The results showed a similar extraction of Nb for both solvents. However, for Ta, extraction efficiency is increased by a factor of 1.3 for 4-MAcPh. In addition, the MIBK solubilized completely after 6 mol∙L−1 of H2SO4 against only a loss of 0.14–4% for 4-MAcPh between 6 and 9 mol∙L−1 of H2SO4. The potential of 4-MAcPh has also been studied to selectively recover Ta from a model capacitor waste solution. The results showed a selectivity for Ta in the presence of impurities such as Ag, Fe, Ni and Mn. The 4-MAcPh also presents the advantage of having physicochemical properties adapted to its use in liquid-liquid extraction technologies such as mixer-settlers.

scholarly journals Counter Current Liquid-Liquid Extraction Column with Agitators.

1956 ◽  
Vol 20 (1) ◽  
pp. 2-10
Author(s):  
S. Nagata ◽  
W. Eguchi ◽  
T. Yokoyama ◽  
K. Maeda
Keyword(s):  
Liquid Extraction ◽  
Extraction Column ◽  
Liquid Liquid Extraction ◽  
Counter Current

Quaternary ammonium based task specific ionic liquid for the efficient and selective extraction of neptunium

2017 ◽  
Vol 105 (9) ◽  
Author(s):  
Nishesh Kumar Gupta ◽  
Arijit Sengupta ◽  
Sujoy Biswas
Keyword(s):  
Ionic Liquid ◽  
Cation Exchange ◽  
Quaternary Ammonium ◽  
Acidic Solution ◽  
Selective Extraction ◽  
Liquid Extraction ◽  
Exchange Mechanism ◽  
Liquid Liquid Extraction ◽  
Aqueous Acidic Solution ◽  
Task Specific Ionic Liquid

Abstract:Liquid–liquid extraction of neptunium from aqueous acidic solution using quaternary ammonium based task specific ionic liquid (TSIL) was investigated. The extraction of Np was predominated by the ‘cation exchange’ mechanism via [NpO

scholarly journals Jigsaw cooperative learning of multistage counter-current liquid-liquid extraction using Mathcad®

2021 ◽  
Author(s):  
Ma Carmen Cerón-García ◽  
Lorenzo López-Rosales ◽  
Juan José Gallardo-Rodríguez ◽  
Elvira Navarro-López ◽  
Asterio Sánchez-Mirón ◽  
...  
Keyword(s):  
Cooperative Learning ◽  
Liquid Extraction ◽  
Liquid Liquid Extraction ◽  
Counter Current

scholarly journals Tantalum and Niobium Selective Extraction by Alkyl-Acetophenone

2018 ◽  
Author(s):  
Moussa Toure ◽  
Guilhem Arrachart ◽  
Jean Duhamet ◽  
Stephane Pellet-Rostaing
Keyword(s):  
Physicochemical Properties ◽  
Aqueous Phase ◽  
Organic Phase ◽  
Extraction Efficiency ◽  
Selective Extraction ◽  
Extraction Process ◽  
Liquid Extraction ◽  
Waste Solution ◽  
Liquid Liquid Extraction ◽  
Kd Values

A study has been carried out on Ta and Nb recovery by liquid-liquid extraction process using 4-methylacetophenone (4-MAcPh) as organic phase. The 4-MAcPh was compared to methylisobutylketone (MIBK) with respect to extraction efficiencies (kD values) at different concentrations of H2SO4 in the aqueous phase. The results showed a similar extraction of Nb for both solvents. However, for Ta extraction efficiency is increased by a factor of 1.3 for 4-MAcPh. In addition, the MIBK solubilized completely after 6 mol L-1 of H2SO4 against only a loss of 0.14 to 4% for 4-MAcPh between 6 and 9 mol L-1 of H2SO4. The potential of 4-MAcPh has also been studied to selectively recover Ta from a model capacitor waste solution. The results showed a selectivity for Ta in the presence of impurities such as Fe, Ni, Mn. The 4-MAcPh also presents the advantage of having physicochemical properties adapted to its use in liquid-liquid extraction technologies such as mixer-settlers.

scholarly journals Identification of Transient Receptor Potential Vanilloid 3 Antagonists from Achillea alpina L. and Separation by Liquid-Liquid-Refining Extraction and High-Speed Counter-Current Chromatography

Molecules ◽  
2020 ◽  
Vol 25 (9) ◽  
pp. 2025 ◽  
Author(s):  
Shi-Wei Sun ◽  
Rong-Rong Wang ◽  
Xiao-Ying Sun ◽  
Jia-He Fan ◽  
Hang Qi ◽  
...  
Keyword(s):  
Ethyl Acetate ◽  
High Speed ◽  
Transient Receptor Potential ◽  
Receptor Potential ◽  
Ethanol Extract ◽  
Liquid Extraction ◽  
Transient Receptor Potential Vanilloid ◽  
Liquid Liquid Extraction ◽  
Transient Receptor ◽  
Counter Current

Bioassay-guided fractionation of the ethanol extract of whole herbs of Achillea alpina led to the isolation of isochlorogenic acids A and B as transient receptor potential vanilloid 3 (TRPV3) channel antagonists by using a calcium fluorescent assay. The structures were identified by spectroscopic analysis and the inhibitory activities of isochlorogenic acids A and B were confirmed by whole-cell patch clamp recordings of human embryonic kidney 293 (HEK293) cells expressing human TRPV3. Molecular docking results revealed that these two compounds reside in the same active pocket of human TRPV3 channel protein with lower binding energy than the agonist 2-aminoethoxydiphenyl borate (2-APB). High-speed counter-current chromatography (HSCCC) coupled with a liquid-liquid extraction approach was successfully established for the separation of isochlorogenic acids A and B from the whole herbs of A. alpina. Ethyl acetate and n-hexane-ethyl acetate-water (3:3:4 and 1:5:4, v/v/v) were selected as liquid-liquid extraction solvent systems to remove high- and low-polarity impurities in the mixture. Sixty g of ethanol extract was refined by solvent partition to yield 1.7 g of the enriched fraction, of which 480 mg in turn obtained 52.5 mg of isochlorogenic acid B (purity 98.3%) and 37.6 mg isochlorogenic acid A (purity 96.2%) after HSCCC with n-hexane-ethyl acetate-water containing 1% acetic acid (1:4:8, v/v/v).

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