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Nuclear Production of Hydrogen, Fourth Information Exchange ...

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PROPOSED CHEMICAL PLANT INITIATED ACCIDENT SCENARIOS IN A S-I CYCLE PLANT COUPLED TO A PEBBLE BED MODULAR REACTOR<br />

Figure 8: Section 2 reaction chamber rupture<br />

Figure 9: Section 3 reaction chamber rupture<br />

Preliminary modelling <strong>of</strong> reaction chamber rupture<br />

In this section a preliminary modelling <strong>of</strong> a reaction chamber rupture in Section 2 <strong>of</strong> the S-I cycle is<br />

described. The S-I cycle model utilised is detailed in Brown (2009) and the PBMR-268 model used is<br />

detailed in Seker (2005). The discharging gas is modelled using the source model presented in Bird<br />

(1960) for choked gas flows. The composition <strong>of</strong> the discharging gas is shown in Table 2. A graphical<br />

representation <strong>of</strong> the discharge is shown in Figure 10. The discharge rate model is:<br />

( 1−k<br />

[ ) 2 2 <br />

t = F − 1]<br />

<br />

k − 1 <br />

V<br />

C<br />

gckP0<br />

<br />

<br />

<br />

A <br />

0<br />

<br />

d k<br />

D<br />

−1<br />

2<br />

( k+<br />

1) ( k−1) 2 <br />

<br />

+ 1 <br />

NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 383

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