The Absorption of Gold Cyanide Onto Activated Carbon. 1. The Kinetics of Absorption from Pulps

The Absorption of Gold Cyanide Onto Activated Carbon. 1. The Kinetics of Absorption from Pulps
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Release: 1984
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An account is given of the development of a relatively simple model that describes the kinetics of the absorption of gold cyanide on activated carbon. The model is based on the treatment of the carbon-solution interface as a homogeneous boundary across which gold is transported at a rate determined by the rate of mass transport to and from the interface. Rate equations derived from this model describe the results of various kinetic experiments under continuous or batch conditions in the laboratory and on operating pilot and full-scale plants.

The Absorption of Gold Cyanide Onto Activated Carbon. 2. Application of the Kinetic Model to Multistage Absorption Circuits

The Absorption of Gold Cyanide Onto Activated Carbon. 2. Application of the Kinetic Model to Multistage Absorption Circuits
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Release: 1984
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A relatively simple rate equation for the kinetics of the absorption of gold from cyanide solutions onto activated carbon was used as the basis in the development of a model for multistage carbon-in-pulp and carbon-in-leach absorption circuits. The model was used in the prediction of both the steady-state and the transient behaviour of the absorption process, and the results were found to be in reasonable agreement with those observed in an extended pilot-plant campaign. A number of practical implications of the model are discussed, and an assessment is made of the economic consequences of the various process options available for the design of a carbon-in-pulp plant.

The Absorption of Gold Cyanide Onto Activated Carbon. 3. Factors Influencing the Rate of Loading and the Equilibrium Capacity

The Absorption of Gold Cyanide Onto Activated Carbon. 3. Factors Influencing the Rate of Loading and the Equilibrium Capacity
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Release: 1984
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The results are reported of experiments on the influence of a number of variables on the rate of loading of gold cyanide onto activated carbon and the equilibrium capacity of the carbon. These variables include the concentrations of gold and free cyanide in solution, the pH value and ionic strength of the solution, the concentration of organic compounds in the solution, the temperature, the particle size of the carbon, and the mixing efficiency. The experiments were carried out under approximately steady-state conditions to simulate the conditions in a countercurrent carbon-in-pulp absorption plant. In addition, the results are reported of experiments to establish whether the absorption of gold cyanide onto activated carbon is a reversible process.

The Chemical Behaviour of Cyanide in the Extraction of Gold. 1. Kinetics of Cyanide Loss in the Presence and Absence of Activated Carbon

The Chemical Behaviour of Cyanide in the Extraction of Gold. 1. Kinetics of Cyanide Loss in the Presence and Absence of Activated Carbon
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Release: 1990
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The kinetics of cyanide loss were found to be first order under any given set of conditions, allowing rate constants to be easily determined. At room temperature and in the absence of activated carbon, some cyanide is lost by hydrolysis to hydrogen cyanide, but this does not occur to any significant extent at pH values higher than about 10. A higher rate of hydrolysis occurs when air-agitation is used. When activated carbon is present, an additional carbon-catalysed oxidation reaction is responsible for a fairly high loss of cyanide. The evidence indicates a reaction mechanism that consumes oxygen and produces cyanate ion. Some of the cyanate thus produced decomposes to form a mixture of ammonia, carbonate, and urea, depending on the solution conditions. Additional cyanide is lost as a result of the adsorption of sodium cyanide by the activated carbon. At high temperatures, an additional hydrolysis reaction, which involves the formation of ammonium formate as an intermediate, occurs and is responsible for a high loss of cyanide, leading ultimately to the formation of ammonia, hydrogen, and carbon dioxide. The presence of activated carbon has no effect on the rate of this reaction.

The Optimization of a Carbon-in-pulp Adsorption Circuit Based on the Kinetics of Extraction of Aurocyanide by Activated Carbon

The Optimization of a Carbon-in-pulp Adsorption Circuit Based on the Kinetics of Extraction of Aurocyanide by Activated Carbon
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Release: 1980
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Although the carbon-in-pulp (CIP) process for the recovery of gold from cyanide solutions is now well established, there is little fundamental understanding of the factors influencing the optimum performance of the adsorption circuit. Therefore, in the past, a trial-and-error procedure was generally adopted so that the twin goals of the process could be attained, namely carbon loadings with high gold concentrations and tailings with low concentrations of gold. If it is assumed that the head solution, the tailings solution, and the final carbon loading are fixed process requirements, then the basic process variables are the carbon concentration in each stage and the flow-rates of the carbon and the pulp from stage to stage. The factor that determines how these parameters can be varied to the best advantage is the rate of gold extraction in each stage. In this paper it is shown that these quantities can be calculated for any set of fixed process requirements and for any number of stages in the circuit. The calculations are based on an empirical rate of expression obtained from experiments carried out on a CIP pilot plant.