The chemical feasibility of the Dapex and h e x solvent extraction processes for recovery of uranium from sulfuric acid leach slurry (20 wt 70solid) of magnesium reduction slag was demonstrated, Extraction isotherms show that only 3 to 4 theoretical stages are needed for good urmiuna rccoverg. Phase separation is rapid w i t h virtuallby no emulsion i f the mixing is controlled to disperse slurry in continuous solvent phase
In continuous countercurrent tests with the napex process using 5 extraction stages and 3strip stages ux-aniurn recovery was 99.$%, and the product contained -=..500 ppn of any one impurity, The solvent loss was less than 0,s gal/lOQQgal of slurry, The cost of chemicals for extrac- tion, strdpping, precipitation, and solvent loss was 13d per pound of uranium recovered,