IGCAR : Annual Report - Indira Gandhi Centre for Atomic Research
IGCAR : Annual Report - Indira Gandhi Centre for Atomic Research
IGCAR : Annual Report - Indira Gandhi Centre for Atomic Research
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
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