1999
DOI: 10.1081/ss-100100692
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Purification of Thorium From Uranium-233 Process Residue

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(4 citation statements)
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“…The saturation capacity was calculated according to the following equations: where V (S%=100) is the volume of solution at sorption percent = 100 (mL), C 0 is the Th concentration in the feed solution (mg/mL), m is the exchanger mass (g). From this figure it is clear that the extraction decreased by increasing of Th concentration, the saturation capacity of Th is 120 mg Th/g AMP in the case of 0.1 M HNO 3 and 80 mg Th/g AMP in 3 M HNO 3 .…”
Section: Batch Investigationmentioning
confidence: 87%
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“…The saturation capacity was calculated according to the following equations: where V (S%=100) is the volume of solution at sorption percent = 100 (mL), C 0 is the Th concentration in the feed solution (mg/mL), m is the exchanger mass (g). From this figure it is clear that the extraction decreased by increasing of Th concentration, the saturation capacity of Th is 120 mg Th/g AMP in the case of 0.1 M HNO 3 and 80 mg Th/g AMP in 3 M HNO 3 .…”
Section: Batch Investigationmentioning
confidence: 87%
“…The quality of the crystalline product determined by chemical analysis (Mo measured by atomic absorption, NH 4 + and PO 4 were measured by IC). The results of the analysis of the product are given below and show that they have the composition [(NH 4 ) 3 AMP was found insoluble in acidic solution (HNO 3 , HCl) but soluble in alkaline solution (NaOH, NH 4 OH).…”
Section: Characterization Of Ampmentioning
confidence: 98%
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