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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 12: Extent <strong>of</strong> reaction in Section 3 for area = 0.02 m 2 break<br />

Figure 13: Extent <strong>of</strong> reaction in Section 3 for area = 0.02 m 2 break<br />

Conclusions<br />

It is evident that important transient scenarios can be initiated by the chemical plant side <strong>of</strong> a coupled<br />

nuclear thermochemical hydrogen generation scheme. The first step to understanding these potential<br />

accident scenarios is proposing the scenarios and investigating through qualitative reasoning and<br />

later modelling.<br />

This paper presents seven potential accident scenarios in two categories. The categories are<br />

dubbed as: i) discontinuous reactor accidents; ii) reaction chamber rupture events. Brief qualitative<br />

descriptions and analyses <strong>of</strong> these accident scenarios are presented. Additionally, a scheme is<br />

proposed for modelling scenarios where a reaction chamber rupture is present.<br />

Additional work must be performed regarding the efficacy and specific applicability <strong>of</strong> these<br />

scenarios. Limiting factors should be identified, and more specific examples <strong>of</strong> these scenarios must be<br />

established. Parametric studies <strong>of</strong> these limiting factors must be performed. Essential to the modelling<br />

<strong>of</strong> these scenarios is an S-I cycle flow sheet which has been properly scaled-up to an industrial scope.<br />

This is in contrast to the current flow sheets, which are for bench scale type experiments (Brown, 2003).<br />

NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 385

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