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Nuclear Production of Hydrogen, Fourth Information Exchange ...

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EXPERIMENTAL STUDY OF THE VAPOUR-LIQUID EQUILIBRIA OF HI-I 2-H 2O TERNARY MIXTURES<br />

A good agreement between Prophy calculations and experimental results is observed for HI and<br />

H 2 O. I 2 concentration is underestimated.<br />

• For 12% iodine content, corresponding to the top <strong>of</strong> the column, three HI concentrations, 19.5,<br />

16.1 and 13.8% were studied (see Figure 8).<br />

A good agreement between Prophy calculations and experimental results is observed for HI and<br />

H 2 O. I 2 concentration is underestimated, and H 2 formation is observed for high HI concentration.<br />

• For 4% iodine content, at low HI concentration, a good agreement for H 2 O and HI is observed.<br />

• At HI high concentration, Hi concentration decreases versus time due to hydrogen formation.<br />

Conclusions<br />

The experimental study presented in this paper provides new data on liquid-vapour equilibrium <strong>of</strong><br />

HI-I 2 -H 2 O mixtures at high temperature and pressure (Doizi, 2009; Larousse, 2009). These results are<br />

important to improve the modelling <strong>of</strong> the distillation column used in the SI cycle.<br />

Optical online diagnostics have been used to determine the concentrations in the vapour phase.<br />

The results show that, for global compositions close to the azeotrope, the thermodynamic model<br />

correctly predicts concentrations <strong>of</strong> HI and H 2 O up to temperatures <strong>of</strong> about 260°C, while improvements<br />

must be made to better represent the iodine concentration in the vapour phase.<br />

For compositions with HI concentrations higher than the azeotropic one, it was pointed out that<br />

the model cannot converge on finite solutions for temperatures higher than 150°C. Moreover, HI<br />

dissociation into hydrogen and iodine has to be accounted for in high-HI and low-I 2 compositions.<br />

Table 1: Concentrations studied in the low-pressure device<br />

Compounds introduced Total P [H 2 O] & [HI) [I 2 ]<br />

The analysis <strong>of</strong> the pertinence <strong>of</strong> the number <strong>of</strong> significant figures<br />

is undergoing evaluation<br />

I 2 = 3.98% - HI = 13.43% - H 2O = 82.58% X X X<br />

I 2 = 4.04% - HI = 10.06% - H 2O = 85.90% X X X<br />

I 2 = 3.95% - HI = 15.63% - H 2O = 80.42% X X<br />

I 2 = 4.02% - HI = 18.91% - H 2 O = 77.08% X X X<br />

I 2 = 12.09% - HI = 15.19% - H 2 O = 72.72% X X X<br />

I 2 = 12.28% - HI = 15.5% - H 2 O = 72.22% X X X<br />

I 2 = 12.11% - HI = 13.82% - H 2 O = 74.07% X X X<br />

I 2 = 12.49% - HI = 17.85% - H 2 O = 69.66% X X X<br />

I 2 = 12.45% - HI = 20.16% - H 2 O = 67.40% X X<br />

I 2 = 11.94% - HI = 11.25% - H 2 O = 76.82% X X X<br />

I 2 = 39.11% - HI = 9.57% - H 2O = 51.32% X X<br />

I 2 = 38.61% - HI = 9.65% - H 2O = 51.74% X X X<br />

I 2 = 38.75% - HI = 11.02% - H 2O = 50.24% X X<br />

I 2 = 39.74% - HI = 11.67% - H 2O = 48.58% X X X<br />

I 2 = 39% - HI = 13.11% - H 2O = 47.90% X X X<br />

I 2 = 39% - HI = 13.56% - H 2O = 47.45% X X X<br />

I 2 = 38.83% - HI = 13.59% - H 2 O = 47.58% X X<br />

I 2 = 38.96% - HI = 13.625% - H 2O = 47.41% X X<br />

I 2 = 49.18% - HI = 9.11% - H 2O = 41.71% X X X<br />

I 2 = 63.95% - HI = 6.94% - H 2 O = 29.11% X X X<br />

I 2 = 62.11% - HI = 7.9% - H 2 O = 29.99% X X X<br />

I 2 = 64.97% - HI = 7.79% - H 2 O = 27.25% X X X<br />

I 2 = 64.25% - HI = 7.95% - H 2 O = 27.81% X X X<br />

I 2 = 85.37% - HI = 2.99% - H 2 O = 11.64% X X X<br />

I 2 = 85.01% - HI = 3.45% - H 2 O = 11.54% X X X<br />

I 2 = 84.5% - HI = 3.44% - H 2O = 12.06% X X X<br />

I 2 = 84.66% - HI = 3.27% - H 2 O = 12.07% X X X<br />

NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 195

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