2003
DOI: 10.1081/sei-120022518
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Experimental Verification of Caustic‐Side Solvent Extraction for Removal of Cesium from Tank Waste

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Cited by 30 publications
(21 citation statements)
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“…The process as currently practiced has been optimized [2][3][4][5][6] and demonstrated [7][8][9] for removal of cesium from salt waste at the Savannah River Site (SRS). To meet the needs of the SRS Salt Waste Processing Facility (SWPF) [10], the CSSX process has been designed and demonstrated to remove cesium with a decontamination factor (DF) in excess of 40,000, concentrating it by a factor (CF) of 15 in a stream of 1 mM HNO 3 suitable for vitrification.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…The process as currently practiced has been optimized [2][3][4][5][6] and demonstrated [7][8][9] for removal of cesium from salt waste at the Savannah River Site (SRS). To meet the needs of the SRS Salt Waste Processing Facility (SWPF) [10], the CSSX process has been designed and demonstrated to remove cesium with a decontamination factor (DF) in excess of 40,000, concentrating it by a factor (CF) of 15 in a stream of 1 mM HNO 3 suitable for vitrification.…”
Section: Introductionmentioning
confidence: 99%
“…Cesium distribution ratios (D Cs = [Cs] org /[Cs] aq ) for extraction of the specified feed compositions by the CSSX solvent were to be either calculated using an existing thermodynamic model, provided it was found to be suitably parameterized, or determined experimentally for selected feeds. Assuming a target cesium decontamination factor (DF) of 5000 and a concentration factor (CF) in the range [5][6][7][8][9][10][11][12][13][14][15], the values of D Cs corresponding to each feed are needed to calculate a flowsheet specifying the minimum number of centrifugal-contactor stages and phase flow rates needed to meet the process targets. Based on the physical properties of the phases, the contactor sizes that would furnish a throughput of 20.8 L/min.…”
Section: Introductionmentioning
confidence: 99%
“…As is the case with nearly all industrial applications of solvent extraction, the CSSX process is implemented in a counter-current flow configuration; that is, the organic solvent phase moves in a direction opposite to the aqueous phases. Figure 9 shows a sample CSSX flowsheet (Leonard et al 2003).…”
Section: Solvent Extractionmentioning
confidence: 99%
“…The CSSX process contains no less than 30 stages, sequentially 1 wash, 15 for extraction, 2 scrub, and 15 for stripping [52] . Originally, the organic phase has been constituted by three organic compounds, with a specific work to do, dissolved in Isopar L (aliphatic diluent): the extractant, actually calix [4]arene-bis-(tert-octylbenzo-crown-6) (BOBCalixC6), a modifier 1-(2,2,3,3-tetrafluoropropoxy)-3-(4-sec-butylphenoxy)-2-propanol (Cs-7SB) and finally a small amount of trioctylamine (TOA).…”
Section: Trends In Caesium Solvent Extraction-case Studymentioning
confidence: 99%