Principal Investigator: Boris M. Khudenko (Georgia Institute of Technology)
Principal Investigator: Harold F. Wiedeman (Georgia Institute of Technology)
Principal Investigator: Joseph P. Gould (Georgia Institute of Technology)
Sponsor: GWRI
Start Date: 1986-07-01; Completion Date: 1986-07-01;
Keywords: Cadmium, Magnesium, Resource Recovery, Hazardous Wastes, Toxic Substances, Industrial Wastes, Waste Treatment
Description:
The kinetics of cementation of cadmium by magnesium were studied in a completely mixed batch reactor at room temperature and constant mixing rate and ionic strength. Magnesium strips provided in stoichiometric excess were used as electrodes. The effect of pH and initial cadmium concentration on the rate of cadmium removal and reaction stoichiometry, or yield of magnesium consumed per cadmium cemented, were evaluated.
The rate of cadmium removal was shown to be independent of pH between 3 and 6. However, as pH increased, the process yield became more favorable. This was attributed to the competing reaction of magnesium dissolution which decreases with increasing pH. The rate of cadmium removal was studied at initial cadmium concentrations between 1 and 100 mM. It was found that the rate and stoichiometry were highly dependent upon initial cadmium concentration.
At initial concentrations of up to approximately 25 mM, the reaction was found to follow apparent half order kinetics consistent with a migration control mechanism. As initial cadmium concentrations increased through this range, removal rates also increased. At approximately 25 mM, a transition was observed to apparent first order kinetics consistent with a diffusion control mechanism. There was a significant decrease in removal rates as the initial cadmium concentration increased to levels of greater than 25 mM.
Stoichiometry was found to become more favorable as initial cadmium concentration increased, and in some cases, less than 1 mole of magnesium was required to cement 1 mole of cadmium. This effect was attributed to electrolysis of water by the induced electrochemical system.