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chemical thermodynamics of neptunium and plutonium - U.S. ...

chemical thermodynamics of neptunium and plutonium - U.S. ...

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A. Discussion <strong>of</strong> selected references 659<strong>of</strong> this paper was on the determination <strong>of</strong> the formation constants <strong>of</strong> the aqueous TTAcomplexes <strong>of</strong> Np(IV) <strong>and</strong> Pu(IV), respectively. In addition to the constants ∗ K 1 (A.51,M=Np)=(48 ± 2) <strong>and</strong> ∗ K 1 (A.51,M=Pu)=(83 ± 5),M 4+ + HTTA(aq) Å MTTA 3+ + H +(A.51)the complexation constants <strong>of</strong> the 1:1 <strong>and</strong> 1:2 complexes <strong>of</strong> fluoride <strong>and</strong> sulphate havebeen reported for Np(IV) <strong>and</strong> Pu(IV).From the <strong>neptunium</strong> HSO − 4experiments, sufficient data are provided to allow recalculationusing a non-linear least squares model, but the errors in log 10 β 1 <strong>and</strong> log 10 β 2are large because <strong>of</strong> the small number <strong>of</strong> data points. Because <strong>of</strong> the large errors inthese determinations, the results, although consistent with previous results, are ignoredin the calculation <strong>of</strong> best values.The constants for the reaction <strong>of</strong> Np 4+ with HF(aq), corrected for aqueousTTA complexing, are used in the selection procedure in Part III, Section 9.2.1.2with estimated uncertainties: log ∗ 10 β 1 (NpF 3+ , I = 2M) = (4.70 ± 0.15) <strong>and</strong>log ∗ 10 β 1 (NpF 2+2, I = 2M) = (7.38 ± 0.30).In the <strong>plutonium</strong> experiments, 238 Pu or 239 Pu was used. Based on the data given inthis paper log 10 β 1 (I)(19.4) = (2.73 ± 0.18) <strong>and</strong> (2.80 ± 0.13) <strong>and</strong> log 10 β 2 (I)(19.5)= (4.66 ± 0.07) <strong>and</strong> (4.47 ± 0.08). We have not made any correction for aqueousTTA complexing <strong>of</strong> Pu(IV) on these data or any other data set used for evaluating thecomplexation constants for the sulphato complexes. The maximum effect is likely tobe approximately 6 % in β 1 (I)(19.4) or β 2 (I)(19.5) (i.e., it is within the range <strong>of</strong> thevariation <strong>of</strong> the measurements themselves). The constants for the reaction <strong>of</strong> Pu 4+ withfluoride, corrected for aqueous TTA complexing, are used in the selection procedure inPart IV, Section 18.2.1.2 with estimated uncertainties: log ∗ 10 β 1 (PuF 3+ , I = 2M) =(4.64 ± 0.15) <strong>and</strong> log ∗ 10 β 1 (PuF 2+2, I = 2M) = (7.62 ± 0.30).[76BAG/RAM2]The purpose <strong>of</strong> this study was to review earlier solvent extraction studies <strong>of</strong> Pu(IV)complexation by different authors, as well as to remeasure these systems, in particularwith regard to controlling the Pu(IV) oxidation state before <strong>and</strong> after the experiments.In the absence <strong>of</strong> a holding oxidant (which in principle may interact with other componentsin the system <strong>and</strong> thus introduce systematic errors), Pu(IV) may be reduced toPu(III) which is much less readily extractable than Pu(IV). The presence <strong>of</strong> this extraunextracted <strong>plutonium</strong> may be mistakingly interpreted as evidence for the formation <strong>of</strong>hydrophilic complexes. Also, in earlier studies, the complex formation <strong>of</strong> Pu(IV) <strong>and</strong>TTA − in the aqueous phase was neglected. Such complexation was taken into accountin this study [76BAG/RAM2], although it should be mentioned that the correctionfactor is very small.The method used was solvent extraction, with HTTA, dinonylnaphthalenesulphonicacid (HDNNS), <strong>and</strong> tributylphosphate (TBP) as extractants, <strong>and</strong> an aqueous phasecontaining varying proton concentrations, as well as sulphate, nitrate, chloride <strong>and</strong> fluoride,respectively, as aqueous lig<strong>and</strong>s. The temperature was reported as (25 ± 0.1) ◦ C

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