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IGCAR : Annual Report - Indira Gandhi Centre for Atomic Research

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IGC<br />

<strong>Annual</strong> <strong>Report</strong> 2007<br />

in thermoelectric peltier<br />

element module <strong>for</strong><br />

maintaining temperature of<br />

sample. Samples were loaded<br />

in polystyrene cups and placed<br />

into the activity meter. The<br />

activity meter was standardized<br />

using a two-step procedure. In<br />

the first step, purified and<br />

degassed ASTM-Grade-1 water<br />

was used as a standard in<br />

addition to the four aqueous<br />

electrolyte solutions supplied in<br />

sealed ampules as standards.<br />

These solutions were 0.5 m KCl<br />

(a W =0.984±0.003), 6.0 m<br />

NaCl (a W = 0.760±0.003),<br />

8.57 m LiCl (a W =0.500±<br />

0.003) and 13.3 m LiCl (a W<br />

=0.250±0.003). In the second<br />

step, 19 aqueous solutions of<br />

AR grade urea (1 x 10 -4 to 13 m<br />

approx.) were made and their<br />

water activities were<br />

determined experimentally.<br />

Experimentally determined<br />

water activity values <strong>for</strong> ureawater<br />

system were compared<br />

with two sets of literature data<br />

and an excellent agreement<br />

was observed. 14 solutions of<br />

uranyl nitrate were made<br />

(~5x10 -4 to 5 m). The water<br />

activity values <strong>for</strong> the uranyl<br />

nitrate solutions were<br />

determined and plotted in Fig.1<br />

along with the values reported<br />

in the literature<br />

The osmotic coefficient was<br />

derived from water-activity<br />

values and based on that<br />

activity coefficient of uranyl<br />

nitrate in aqueous solution was<br />

estimated. From water activity<br />

values, vapour pressure of<br />

aqueous solutions of uranyl<br />

nitrate was also estimated and<br />

is shown in Fig.2 along with the<br />

literature data. Both match<br />

well. Based on similar<br />

methodology, activity<br />

coefficients of various other key<br />

and non-key solutes of interest<br />

to reprocessing are being<br />

evaluated. Incorporation of<br />

these activity coefficients in the<br />

mathematical models <strong>for</strong><br />

nuclear solvent extractions<br />

would reduce the margin of<br />

error in the predictions from the<br />

computer simulations.<br />

Fig.2 Variation of vapour pressure of<br />

aqueous solution of uranyl nitrate<br />

hexahydrate with concentration at<br />

298.15 K and 0.l MPa. The present<br />

experimental and calculated<br />

data are compared with those<br />

reported in the literature.<br />

IV.B.3 Study of TBP-Nitric Acid Runaway Reaction<br />

and Synthesis of Red-Oil<br />

TBP nitric acid runaway<br />

reaction was studied in a high<br />

temperature-high pressure<br />

autoclave (shown in Fig.1) and<br />

red-oil was synthesized. It was<br />

established that presence of<br />

metallic nitrates was not<br />

essential <strong>for</strong> red-oil <strong>for</strong>mation<br />

as thought earlier. Various<br />

single-phase as well as twophase<br />

experiments have been<br />

completed.<br />

From Fig.2 it is observed that<br />

temperature profile had a<br />

threshold of about 403K. This<br />

Autoclave<br />

Fig.1 A view of the experimental<br />

setup <strong>for</strong> study of runaway chemical<br />

reactions of interest to reprocessing<br />

threshold temperature is<br />

initiation temperature. From<br />

Fig.3, it can be seen that the<br />

amount of pressure generated<br />

per mL of TBP exceeds even<br />

500 psi /mL of TBP. It<br />

underlines the absolute<br />

necessity of removal of<br />

entrained as well as dissolved<br />

organics from the aqueous salt<br />

solutions be<strong>for</strong>e they are<br />

concentrated by means of<br />

FUEL CYCLE 99

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