THE RADIOCHEMISTRY OF PLUTONIUM - Sciencemadness.org
THE RADIOCHEMISTRY OF PLUTONIUM - Sciencemadness.org
THE RADIOCHEMISTRY OF PLUTONIUM - Sciencemadness.org
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1.0<br />
D<br />
0.1<br />
—--L~,20<br />
HNOO; CO&NT R’ATION (~)<br />
Fig. 36. Extraction of Pu(IIT) and<br />
Pu(VI) into TTA-benzene as a function<br />
of HN03 concentration at constant total<br />
nitrate concentration. LiN03 added. 174<br />
Pu(VI) Pu(III)<br />
TTA cone. (~) 0.74 1,65<br />
Total nitrate (M) 0.175 0.096<br />
Aqueous condi~ons 0.005 M<br />
2 X 10-4 ~ KMnOy Fem104)2<br />
1000<br />
100<br />
f)l<br />
10<br />
o.I<br />
0.01<br />
0.001<br />
0,0001 01234567S9 101112<br />
HN03 MOLARl~<br />
Fig, 37. Distribution coefficients of<br />
various ions from nitric acid solutions<br />
into 0.2 M TTA in benzene .ll O. Ill<br />
—<br />
TTA has been used to separate a<br />
194 or<br />
small amotmt of b“ from macro Pu,<br />
vice versa,415to concentrate Pu from en-<br />
352<br />
vironmental w-ater samples and to<br />
determine the oxidation state of Pu in<br />
environmental samples, including sea<br />
water.’ 36 In the latter procedure, Pu(IV)<br />
is extracted from 0.5 ~ HC1 and the<br />
acqueous raffinate adjusted to pH 4.3 with<br />
ammonium acetate from which the Pu(III)<br />
and Pu(VI) are extracted together. On a second sample, the Pu(IV) and Pu(III) are<br />
coprecipitated together with LaF3. The relative amounts of the three valence states<br />
are then calculated by difference.<br />
TTA has been used to separate Pu from impurities for a spectrographic<br />
analysis. 411 In this procedure an HC1 solution of the metal is reduced to Pu(III) with<br />
hydroxylamine and impurity elements extracted with TTA in hexone. The Pu in the<br />
aqueous phase is then oxidized to Pu(IV) and extracted into TTA-hexone. By this pro-<br />
cedure both extractable and non-extractable impurities can be determined.<br />
TTA has been used for several procedures for the determination of Pu in bio-<br />
logical material, especially urine 125,349, 360,257,56, 316 (see, for example,<br />
Procedure 21, Section VIII).<br />
68