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Nuclear Production of Hydrogen, Fourth Information Exchange ...

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USE OF PSA FOR DESIGN OF EMERGENCY MITIGATION SYSTEMS IN A HYDROGEN PRODUCTION PLANT<br />

Methodology for PSA-aided design<br />

The methodology for design <strong>of</strong> mitigation systems, which is proposed in this paper, is a simple<br />

combination <strong>of</strong> existing techniques, based on the dynamic feedback <strong>of</strong> process engineering and<br />

probabilistic safety assessment, which aims to develop reliable and effective systems in mitigation <strong>of</strong><br />

unwanted consequences to events, using a lesser amount <strong>of</strong> calculations and iterations through a<br />

sequential process.<br />

The system design follows a logical sequence, which starts with hazard identification from a<br />

process flow sheet, goes through the initial proposal <strong>of</strong> the protection system, and culminates in the<br />

final design <strong>of</strong> the system, as shown in Figure 1. It should be noted that this process covers all the<br />

mitigation systems in the plant; however, this study only presents a case for an acid leak in Section II<br />

<strong>of</strong> the General Atomics SI process. This danger was identified in a previous qualitative analysis, in<br />

which Hazop was used (Mendoza, 2009).<br />

In this paper, we show a simple case starting from the preliminary design structure, which was<br />

postulated by following the steps shown in Figure 1. It should be noted that this case relates to risks<br />

during operation and does not cover other states such as shutdown and start-up.<br />

Figure 1: Process for PSA-aided design<br />

Physical demarcation <strong>of</strong> the analysis area<br />

Although the sulphuric acid achieves a final concentration <strong>of</strong> 90% in the distillation column bottoms,<br />

the negative pressure in the tower minimises the possibility <strong>of</strong> leaks in this equipment.<br />

The region which is considered in the analysis lies between the column bottoms pumping system<br />

and the chemical reactor E207, due to the severe conditions <strong>of</strong> acidity pressure and temperature in<br />

this part <strong>of</strong> the SI cycle (90% ac., T 1 100 K and up to 7 bar) (Brown, 2003).<br />

Figure 2 shows, framed in a box (at the bottom left), the mechanical equipment that will be<br />

covered by the emergency mitigation system designed in this paper.<br />

NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 399

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