Influence of Salting-Out Effects, Temperature and the Chemical Structure of the Extractant on the Rate of Copper(ii) Extraction From Chloride Media With Dialkyl Pyridine Dicarboxylates
Abstract:ABS1RACTThe kinetics of copper(II) extraction from chloride solutions with ACORGA CLX-50 and three model dipentyl pyridine dicarboxylates having ester groups at various positions in the pyridine ring is investigated. It is shown that the extraction occurs in a diffusional regime and that both the ionic strength and temperature have a strong effect on the rate of copper extraction. Basically, the initial rate of copper extraction (denoted hereafter J0) increases as the ionic strength is increased, whereas J o i… Show more
“…Compared the stability constants of copper with nickel (Table 1), it can be found that the stability of chloride-bearing metal species is markedly lower than that of metal ammine species. Additionally, some studies indicated that the salting-out effect is favorable to the extraction reaction [31,32]. Because the nickel chloride species is very unstable, the salting-out effect could play a major role during the nickel extraction.…”
Section: Effect Of Total Ammonia and Chloride Concentrationmentioning
“…Compared the stability constants of copper with nickel (Table 1), it can be found that the stability of chloride-bearing metal species is markedly lower than that of metal ammine species. Additionally, some studies indicated that the salting-out effect is favorable to the extraction reaction [31,32]. Because the nickel chloride species is very unstable, the salting-out effect could play a major role during the nickel extraction.…”
Section: Effect Of Total Ammonia and Chloride Concentrationmentioning
“…In the previous work [15] it was suggested that the limiting step of the copper(II) extraction by ACORGA CLX-50 from concentrated chloride media could be diffusional in nature. It was confirmed by low values of activation energy (about 20 kJ=mol for moving drop experiments).…”
Section: Marcel Dekker Inc • 270 Madison Avenue • New York Ny 10016mentioning
The rate of copper(II) extraction from chloride solutions by commercial extractants: ACORGA CLX-50 and LIX 54 used alone and in equimolar mixture 1 : 1 mole=mole were studied. The interfacial tension and co-adsorption at the hydrocarbon= water interface for systems containing the individual extractants and their mixtures were measured. For kinetics studies a moving drop method was used. The interfacial tension was measured by a drop volume method. It was found that the rate of extraction in binary mixed system is lower in comparison with the rate of copper(II) extraction by individual solvating extractant and strongly depends on the concentration of chloride ions in the aqueous phase. The amount of copper(II) extracted by LIX 54 used alone is very low. The interfacial activity of ACORGA CLX-50 in the toluene=water system is much higher in comparison with LIX 54. The observed decrease of copper(II) extraction rate in systems containing equimolar mixtures of solvating and chelating extractants in the organic bulk solution can be explained as a result of the co-adsorption of the both extractants at the hydrocarbon=water interface.
736CIERPISZEWSKI AND PROCHASKA
“…However, granules of copper are obtained because the electrowinning is carried out from chloride solutions. The extraction of copper from chloride solutions with individual model esters and amides of various pyridinecarboxylic acids was broadly described by us (5)(6)(7)(8)(9)(10)(11)(12)(13)(14)(15)(16)(17)(18)(19)(20).…”
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