Masters Theses

Date of Award

12-1997

Degree Type

Thesis

Degree Name

Master of Science

Major

Chemistry

Major Professor

George K. Schweitzer

Abstract

Electrolytic reduction of Yb3+ at a Hg cathode to the somewhat unstable Yb2+ was performed in various aqueous media in an attempt to separate Yb3+ from Lu3+ by forming relatively insoluble YbSO4. The effects of the aqueous medium, current, and pH on the formation of Yb2+ and YbSO4 were examined. The best experimental conditions for the reduction of Yb3+ to Yb2+ and the formation of YbSO4 were found to be: 0.20-M Yb3+, 0.40-M H2SO4, and 0.50-M (NH4)2SO4 in the aqueous phase, a direct current of 0.20-A, and a pH of 4.0-5.4(±0.3). Under these conditions, approximately 90-95% of the Yb3+ in solution was removed as YbSO4. Several experiments were conducted to determine suitable conditions for countercurrent solvent extraction for the separation of Lu3+ from a mixed lanthanide ore. A mixer-settler type counter-current solvent extraction process was used. The effects of settling time between the aqueous and organic phases, chemical equilibrium time between the lanthanides and the extractant mono-(2-ethylhexyl)2-ethylhexyl-phosphonate (IQ-801) in kerosene, the load concentration of the aqueous phase, and the equilibrium acidity of the aqueous phase were studied. The experimental results indicated that an adequate settling time was approximately 30 sec, and a mixing time of 2 min was sufficient to reach chemical equilibrium. Furthermore, the aqueous load concentration of 0.15-M Ln3+ in 1.4- M to 2.2-M HCl along with an organic phase of 0.45-M IQ-801 in kerosene was satisfactory for limiting emulsion formation while properly utilizing the extractant. The optimum equilibrium acidity range in the aqueous phase was found to be 1.4-M to 1.9-M HCl using a titration method and 1.6-M to 2.2-M HCl using inductively coupled plasma/mass spectrometry for analysis.

Files over 3MB may be slow to open. For best results, right-click and select "save as..."

Share

COinS