Patent Number: 
Section: claims

1. A TBP (tri-butyl phosphate)-nitrate based solvent extraction process for the production of high purity nuclear grade rare metal oxides comprising:subjecting ammonium nitrate-ammonium sulphate effluent generated in a TBP (tri-butyl phosphate)-nitrate based solvent extraction process for the production of high purity nuclear grade rare metal oxides to recycling as a stripping solution so as to strip metal nitrate values from a solvent stream organic phase into an aqueous phase comprising (i) common ion electrolytes based ammonium nitrate-ammonium sulphate effluent to strip hydrolysable rare metal species and (ii) sulphate anion in said ammonium nitrate-ammonium sulphate effluent with complexing ability towards rare metal ions favouring stripping of the rare metal ions from the organic phase into the aqueous phase by equilibration of rare metal solvent extract comprising rare metal nitrate TBP adduct with an aqueous solution containing ammonium nitrate and ammonium sulphate thereby enabling contact of said rare metal nitrate TBP adduct in the organic phase with (NH4)2SO4 in the aqueous phase, andforming aqueous soluble complex salts of respective rare metal ions in the aqueous phase to favor stripping of the rare metal ion from the organic phase into the aqueous phase for recovery of high purity nuclear grade rare metal oxides from said aqueous phase. 2. The TBP (tri-butyl phosphate)-nitrate based solvent extraction process as claimed in claim 1, wherein for about 5 parts of solvent, about 0.7 to 0.8 parts of ammonium nitrate solution is used for complete stripping of the solvent. 3. The TBP (tri-butyl phosphate)-nitrate based solvent extraction process as claimed in claim 1, wherein the effluent ammonium nitrate and ammonium sulphate concentrations are in the range of 0 to 200 g/l and 30 to 100 g/l respectively to achieve efficient stripping. 4. The TBP (tri-butyl phosphate)-nitrate based solvent extraction process as claimed in claim 3, wherein maximum stripping efficiency is attained by the effluent involving about 200 gpl ammonium nitrate and about 30 gpl ammonium sulphate. 5. The TBP (tri-butyl phosphate)-nitrate based solvent extraction process as claimed in claim 1, comprising liquid-liquid extraction process steps of:i) carrying out extraction of a selective rare metal from a feed solution;ii) scrubbing or back extraction for removal of any other co-extracted rare metal impurities from said solvent thereby providing a purified loaded solvent;iii) subjecting the thus purified loaded solvent to the step of stripping of said selective rare metal from the solvent involving the ammonium nitrate-ammonium sulphate effluent generated in the process and thus maintaining common ion electrolyte based chemical ambience to the highly hydrolysable rare metal species to be stripped wherein the sulphate anion of said ammonium sulphate of the effluent forms aqueous soluble complex salt of the rare metal ion such as to be stripped effectively by said effluent and obtaining pure rare metal nitrate solution therefrom; andiv) precipitation of rare metal hydroxide by ammonium hydroxide solution containing trace quantity of sulphuric acid and obtaining said high purity nuclear grade selective rare metal oxide therefrom. 6. The TBP (tri-butyl phosphate)-nitrate based solvent extraction process as claimed in claim 1, wherein said production of high purity rare metal oxides include oxides of zirconium, uranium, plutonium, hafnium, niobium, and tantalum. 7. The TBP (tri-butyl phosphate)-nitrate based solvent extraction process as claimed in claim 1, wherein reduction of ammonium nitrate effluent volume attained is in the range of 12000 to 14000 liters for every metric ton of ZrO2 produced. 8. The TBP (tri-butyl phosphate)-nitrate based solvent extraction process as claimed in claim 5, wherein said liquid-liquid extraction involving the ammonium nitrate-ammonium sulphate effluent as a stripping agent is carried out to achieve substantial reduction in loss of rare metal to only about 0.3 to 0.4 gpl in the stripped solvent with increase in rare metal concentration in said pure rare metal nitrate solution in the range of 120 to 130 gpl with yield of >98% rare metal oxide product and an increase in ammonium nitrate concentration in said effluent in the range of 380 to 400 gpl thereby converting said effluent commercially attractive for disposal. 9. The process as claimed in claim 1 comprising drying wet precipitated rare metal hydroxide cake at a drying rate of 70 to 73 kg/hr.