2009
DOI: 10.1007/bf03402537
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Effective diffusivity of ferric ions and current efficiency in stagnant synthetic copper electrowinning solutions

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Cited by 7 publications
(4 citation statements)
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“…It is important to note that tests 3 and 4 were performed using an electrolyte containing 160 g/L H 2 SO 4 which was different from the concentration used to generate the models. Since the statistical models predicted the results accurately, this confirms the results of our previous work (11) were it was concluded that the sulfuric acid has a minimal effect on current efficiency and no significant effect on energy consumption. Therefore, these statistical models may predict CE and EC for electrolytes containing a sulfuric acid concentration varying from 160 g/L to 220 g/L with minimal error.…”
Section: Verification Of Modelssupporting
confidence: 88%
See 1 more Smart Citation
“…It is important to note that tests 3 and 4 were performed using an electrolyte containing 160 g/L H 2 SO 4 which was different from the concentration used to generate the models. Since the statistical models predicted the results accurately, this confirms the results of our previous work (11) were it was concluded that the sulfuric acid has a minimal effect on current efficiency and no significant effect on energy consumption. Therefore, these statistical models may predict CE and EC for electrolytes containing a sulfuric acid concentration varying from 160 g/L to 220 g/L with minimal error.…”
Section: Verification Of Modelssupporting
confidence: 88%
“…Also it has been shown by Das and Krishna (2) that increasing the electrolyte temperature leads to lowering the EC in CuEW. In our previous work (11) the effect of ferric concentration, copper concentration, current density, electrolyte temperature, sulfuric acid, cobalt, manganese and chloride on CE and EC were evaluated and the analysis of the results showed that the main important parameters which affect the CE and EC are the ferric concentration, copper concentration, current density and electrolyte temperature. According to a 2007 survey conducted by Robinson et al (12), copper electrowinning is industrially carried out under a wide temperature range varying between 25 and 65 o C. Therefore, there is no universal optimum for the temperature and the best temperature is determined by other operation parameters specific to each industrial operation.…”
Section: Introductionmentioning
confidence: 99%
“…The purified leach liquor containing 55-90 kg Zn 2+ and 125-175 kg•m −3 of H 2 SO 4 solution is electrolysed at about 30-35°C. Hard rolled aluminium cathodes are employed to attain higher over voltage and Pb-0.5-1.0% Ag alloy anodes (Moats et al 2008) to lower oxygen over-voltage for oxygen evolution, which is advantageous in retarding the corrosion of the anode. At a current density of 300 A•m −2 the cathode current efficiency of zinc deposition is 90% and energy consumption works out to be 3.2 kWh•kg −1 .…”
Section: Electrowinning Of Zincmentioning
confidence: 99%
“…As shown in figure 1, in the electrolytic refining process, copper is dissolved into copper ions from a fire-treated anode plate and passes through an electrolyte * Author to whom any correspondence should be addressed. made of a mixture of sulfuric acid and copper sulfate to a cathode, where it gains electrons to precipitate pure copper [2]. As shown in figure 2, in an electrolysis plant a large number of cells are distributed in a matrix, with approximately 34 pairs of cathode and anode plates in each cell.…”
Section: Introductionmentioning
confidence: 99%