首页   按字顺浏览 期刊浏览 卷期浏览 MODELLING OF EXTRACTION EQUILIBRIUM FOR COPPER( II) EXTRACTION BY PYRIDINECARBOXYLIC AC...
MODELLING OF EXTRACTION EQUILIBRIUM FOR COPPER( II) EXTRACTION BY PYRIDINECARBOXYLIC ACID ESTERS FROM CONCENTRATED CHLORIDE SOLUTIONS AT CONSTANT WATER ACTIVITY AND CONSTANT TOTAL CONCENTRATION OF IONIC OR MOLECULAR SPECIES DISSOLVED IN THE AQUEOUS SOLUTION

 

作者: G. COTE,   A. JAKUBIAK,   D. BAUER,   J. SZYMANOWSKI,   B. MOKILI,   C. POITRENAUD,  

 

期刊: Solvent Extraction and Ion Exchange  (Taylor Available online 1994)
卷期: Volume 12, issue 1  

页码: 99-120

 

ISSN:0736-6299

 

年代: 1994

 

DOI:10.1080/07366299408918202

 

出版商: Taylor & Francis Group

 

数据来源: Taylor

 

摘要:

The extraction of copper(D) from concentrated chloride ion solutions by various pyridinecarboxylic acid esters is investigated. It is shown that the efficiency of the extraction is strongly dependent on the water activity (aw) and total concentration (σ) of ionic or molecular species dissolved in the aqueous phase. For decyl nicotinate, decyl isonicotinate, decyl picolinate and ACORGA CLX-50 (all denoted EXT) in toluene, the distribution of copper(II) can be satisfactorily represented by the formation of CuCl2(EXT)2in the organic phase on the condition of taking into account the existence of CuClx(2-X)complexes (x = 1 to 4) in the aqueous phase. The apparent extraction constant KeX and stability constants |βi of the variousCuOx(2-X)complexes are estimated for two aqueous media corresponding to awandσ= 0.835 and a = 8.0 mol.L-1, and aw= 0.617 and σ = 12.0 mol.L-1, respectively. On the other hand, in the case of ACORGA CLX-50 in kerosene, more complex phenomena influencing the activity coefficient of the extractant seem to occur.

 

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