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Dive into the research topics where Gary A. Kordosky is active.

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Featured researches published by Gary A. Kordosky.


JOM | 1992

Copper solvent extraction: The state of the art

Gary A. Kordosky

Copper recovery by solvent extraction has progressed from a technology with limited application for copper recovery from dilute sulfuric acid leach solution to a technology with broad application for copper recovery from a variety of leach solutions. Reagent improvements have led the way, but they have been accompanied by innovations in leaching and improvements in electrowinning. Of particular interest is the fact that specialized reagents have been developed to meet the specific needs of certain leaching solutions.


Hydrometallurgy | 1992

Gold solvent extraction from typical cyanide leach solutions

Gary A. Kordosky; J.M. Sierakoski; M.J. Virnig; P.L. Mattison

Abstract The guanidine ion pairing functionality, which exists in its protonated form at pH 13.5. Continuous solvent extraction circuits, run in the laboratory and in the field, suggest that leach-SX-EW technology, so successfully applied in the copper industry, is technically feasible for gold.


Tsinghua Science & Technology | 2006

Equilibrium Copper Strip Points as a Function of Temperature and Other Operating Parameters: Implications for Commercial Copper Solvent Extraction Plants

Gary A. Kordosky; Michael J. Virnig; Burrel Boley

Abstract The development of pressure and bioleaching processes for high grade copper ores and concentrates will result in copper solvent extraction plants treating solutions with high copper and acid concentrations at temperatures up to 45°C and these copper solvent extraction plants will run with reagent concentrations up to 40 vol.%. There is also a trend to use copper stripping solutions with less acid than typically used in recent years. Cognis has developed a model that accurately predicts the copper strip point for virtually any copper solvent extraction reagent or combination of reagents under a wide variety of conditions. The equilibrium strip points for several well known commercial copper solvent extraction reagents are given as a function of reagent concentration, the copper and acid concentration of the strip aqueous, and the temperature. It is shown that the equilibrium strip point is not a straight line function of reagent concentration and that the equilibrium strip point increases with an increase in temperature. Copper extraction also increases as the temperature increases.


Archive | 1988

Process for jointly removing undesirable elements from valuable metals containing electrolytic solutions

Ralf Kehl; Werner Schwab; Robert Brantley Sudderth; Gary A. Kordosky


Archive | 1993

Nickel extraction process

Gary A. Kordosky; Stephen M. Olafson


Archive | 1989

Process for the removal of impurity elements from electrolyte solutions containing valuable metals

Ralf Kehl; Werner Schwab; Robert Brantley Sudderth; Gary A. Kordosky


Archive | 1990

Process of extracting anions with quaternary amines

Thomas J. Stierman; Michael J. Virnig; Gary A. Kordosky


Archive | 1997

Beta-diketones for the extraction of copper from aqueous ammoniacal solutions

Michael J. Virnig; Gary A. Kordosky; Sang I. Kang; Kevin V. Martin; Phillip L. Mattison


Archive | 2001

Process for extracting copper values from copper containing ores

Gary A. Kordosky


Archive | 2005

Processes for recovering metals from ores using organic solvent extraction and aqueous stripping at selected temperature differentials

Michael J. Virnig; R. Brantley Sudderth; Philip Crane; Andrew Nisbett; Burrel Boley; Dustin Gordon; Gary A. Kordosky

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