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THE RADIOCHEMISTRY OF PLUTONIUM - Sciencemadness.org

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D<br />

103 ~<br />

,.2 _<br />

10<br />

I<br />

H<br />

,0-1 ~<br />

/<br />

P<br />

/<br />

Pu(m)<br />

/pU(m)<br />

j’ >U(m)<br />

Pu (m)<br />

AQUEOUS I-& CON:ENTR:TION ([j)<br />

Fig. 8. Extraction of U and Pub<br />

TBP in CC14 from HC1 solutions .24 $3070<br />

essentially unextractable. Larsen and<br />

Seils249 measured the extraction of U<br />

and Pu into 30% TEIP in CC14 (Fig. 8),<br />

and used this system as the basis of an<br />

analytical procedure for these elements<br />

(Procedure 15, Sect. VIII). Both Pu(IV)<br />

and Pu(VI) extract better at all acidities<br />

than U(IV) and “U(VI). The quadrivalent<br />

actinides have higher, distribution co-<br />

efficients than the hexavalent above 5-6<br />

~ HC1, while the reverse is true at<br />

lower acidities. These authors report a<br />

distribution coefficient of about 10 -3 for<br />

Pu(III) and 10-4 for Am(III) in 8 ~ HC1<br />

under the same conditions. The value<br />

for Am is considered more reliable be-<br />

cause of possible partial oxidation of<br />

the Pu(III) to Pu(IV). HC1 is much less<br />

extractable than HN03 into TBP. Larsen<br />

and Seils report D = 0.01 at 6 M HC1 and<br />

—<br />

0.12 at 8&l HC1 into 3070 TBP in<br />

CC14.2’4’<br />

Solovkin et al. 390 found that the<br />

extraction of Pu(IV) into 1.1 &l (3070)<br />

TBP in CC14 from perchloric acid was<br />

appreciable. The distribution co-<br />

efficients varied from 0.0045 at 0.4 M .<br />

HC104 to 0.9 at 6.4 ~ HC104. The ex-<br />

tracted complex was determined to be<br />

di-solvated by TBP dilution experiments.<br />

Pu(IV) and Pu(VI) extract well<br />

into TBP from trichloro - and trifluoroacetic acids. 183 The distribution coefficients<br />

decrease with increasing acidity, rather than the usual increase. The distribution co-<br />

efficients for both Pu(IV) and Pu(VI) are about 4 to 5 times as great for CC13COOH as<br />

for CF3COOH at low acid concentrations. For extraction of Pu(IV) into 30~0 TBP in<br />

Amsco- 125 (a kerosene type diluent) f> m an initial concentration of 0.5 M CC13COOH,<br />

—<br />

D = 21; for Pu(VI), D = 4.<br />

The effect of addition of sulfuric acid and phosphoric acid to l%(~) or Pu(VI) –<br />

nitric acid — TE3P systems is invariably to lower the distribution coefficient<br />

438, 440>437<br />

sulfuric439<br />

– phosphoric. This effect is presumably due to the formation of unextractable<br />

sulfate and phosphate complexes of Pu. The effect is more pronounced in Pu(IV) than in<br />

Pu(VI), and at lower nitric acid concentrations. For example, making the aqueous phase<br />

0.08 M in H2S04 lowered D for Pu(IY) from 16 to 9.5 in 4 JYJHN03; in 2 ~ HN03 the<br />

437<br />

corresponding decrease was from 9 to 1.4. On the other hand the lowering of D for<br />

34<br />

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