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A review of HSE's risk analysis and protection-based analysis ...

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Assumption Explanation Application Comment<br />

Releases from highpressure<br />

gas pipelines<br />

are assumed to be<br />

vertical jets.<br />

Rupture <strong>of</strong> a high-pressure gas<br />

pipeline is a violent event that<br />

results in disruption <strong>of</strong> the ground<br />

cover <strong>and</strong> formation <strong>of</strong> a crater<br />

around the point <strong>of</strong> failure. It is<br />

assumed that the gas is projected<br />

vertically upwards from this crater.<br />

The probability that a Potential ignition sources for<br />

release <strong>of</strong> flammable accidental releases are many <strong>and</strong><br />

material will be ignited. varied. On-site sources may include<br />

welding activity or equipment<br />

containing flames, such as boilers or<br />

furnaces. Off-site sources may<br />

include vehicles, traffic lights,<br />

smoking <strong>and</strong> domestic appliances.<br />

Risk <strong>analysis</strong> studies for The distance to which the cloud<br />

toxic substances like generated by a vessel failure remains<br />

chlorine model failure hazardous depends on the quantity<br />

<strong>of</strong> the vessel in two released to atmosphere. The larger<br />

ways – release <strong>of</strong> the the quantity, the greater the distance<br />

entire vessel contents at which the cloud is still hazardous.<br />

upwards into the air;<br />

<strong>and</strong> release <strong>of</strong> the entire<br />

contents downwards, so<br />

that half is retained in<br />

the vessel bund. The<br />

vessel is assumed to be<br />

completely full when it<br />

fails.<br />

Risk <strong>analysis</strong> <strong>of</strong><br />

pipelines.<br />

Risk <strong>analysis</strong> <strong>of</strong> MHPs<br />

<strong>and</strong> MHIs h<strong>and</strong>ling<br />

flammable substances.<br />

Risk <strong>analysis</strong> <strong>of</strong><br />

installations h<strong>and</strong>ling<br />

toxic, pressurised<br />

liquefied gases (such as<br />

chlorine).<br />

There is evidence from accident reports, experiments <strong>and</strong> computer<br />

modelling work that the release <strong>of</strong> gas may be in directions other than<br />

vertical. <strong>HSE's</strong> pipeline <strong>risk</strong> <strong>analysis</strong> models are to be covered by the<br />

model evaluation exercise (see Section 2.4.1).<br />

Currently ignition probabilities are established using expert<br />

judgement informed by research on the numbers <strong>of</strong> potential ignition<br />

sources present in different typical types <strong>of</strong> l<strong>and</strong> use (residential,<br />

industrial, rural etc.). However, HSE has invested in further research<br />

in this area with a view to putting these values on a more rigorous<br />

basis in the future. It is partly because <strong>of</strong> the uncertainty associated<br />

with establishing ignition probabilities that many analyses <strong>of</strong> MHIs<br />

h<strong>and</strong>ling flammable materials are currently <strong>protection</strong> <strong>based</strong>.<br />

This assumption considers two different ways in which a chlorine<br />

storage vessel could fail catastrophically, representing the two<br />

extremes <strong>of</strong> a spectrum <strong>of</strong> possible failures. The assumption <strong>of</strong> 100%<br />

fill <strong>of</strong> the vessel is related to the Hazardous Substances Consent that<br />

the site would hold for storing the material. A site would be entitled to<br />

store this much material for as long <strong>and</strong> as <strong>of</strong>ten as they liked. Note<br />

that the kind <strong>of</strong> vessel failure event considered here is very different<br />

from a BLEVE.

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