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Technical documentation and software quality assurance for project ...

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versus dosage <strong>for</strong> chemical inhalation. Also there was some discussion on setting ignition<br />

location. Center of cloud seemed to be conservative consensus.<br />

Flare notes<br />

View factor : There was discussion about using a cylindrical optically dense flame, as in<br />

the pool fire model rather than using point source view factor. One recommendation was<br />

to always assume a clear, dry day. This is equivalent to neglecting atmospheric<br />

dampening.<br />

gas exist velocity: Model currently assumes that flame will blow out when Mach number<br />

exceeds 0.5. Suggested that there may be a better number or that this restriction be<br />

dropped (flame could simply start farther away from source). Match rate of combustion<br />

to release rate to achieve steady state case. Most felt that horizontal jets also be allowed<br />

rather than only vertical ones. Model will not work well with oil fires due to smoke<br />

generation.<br />

2-phase: Model currently trans<strong>for</strong>ms 2-phase release into gas release. Some pointed out<br />

that 2-phase incident could produce both flare <strong>and</strong> pool fire. Suggested reviewing<br />

existing references on 2-phase flow to see how to h<strong>and</strong>le <strong>for</strong> flare situation<br />

BLEVE<br />

fireball size: Experts agreed that limits should be placed upon fireball size. One<br />

suggestion is to limit fireball mass to three times the fraction that is adiabatically flashed.<br />

Another is to restrict user input to largest common propane tank. Compare our simplified<br />

model to results from more sophisticated models.<br />

terminology: Consensus was that careful wordsmithing needs to be done to maintain<br />

consistency of language, technical accuracy, <strong>and</strong> fit within common usage.<br />

other hazards: Model only considers thermal hazard. People agreed that user should be<br />

warned about all hazards, including overpressure <strong>and</strong> shrapnel. Some discussion on<br />

shrapnel models<br />

Pool fire<br />

pool size: Model currently stops spreading when the burn rate equals the chemical release<br />

rate. Recommendation was to eliminate this restriction <strong>and</strong> stop spreading only when<br />

minimum thickness was reached. Need to ascertain upper limit on model applicability <strong>for</strong><br />

large fires.<br />

pool shape: Suggested that LOC footprint be circular rather than elliptical in order to be<br />

more conservative.<br />

burn regression rate: Approximation of burn regression rate as ratio of heat of<br />

combustion to heat of vaporization may not be good approximation, particularly <strong>for</strong><br />

43

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