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Technical documentation and software quality assurance for project ...

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Martin Goodrich Baker Engineering <strong>and</strong> Risk Consultants<br />

Greg Jackson University of Maryl<strong>and</strong><br />

Tom Spicer University of Arkansas<br />

Doug Walton National Institute of Science <strong>and</strong> Technology<br />

Kin Wong Department of Transportation<br />

Special Training Requirements/Certification:<br />

There are no special additional requirements or certification required to use the new fire<br />

<strong>and</strong> explosion option scenarios in ALOHA. However, certain terminology peculiar to<br />

these specific scenarios will be different from those involving the toxic gas model runs.<br />

It is recommended that anyone new to fire <strong>and</strong> explosives <strong>for</strong>ecasting review the user<br />

<strong>documentation</strong> <strong>and</strong> become familiar with the example problems. In particular, hazards<br />

now include overpressure <strong>and</strong> thermal radiation risk, as opposed to toxic chemical<br />

concentrations.<br />

Data Sources:<br />

Eagle-ALOHA uses the existing ALOHA/CAMEO chemical data sources with the<br />

exception of in<strong>for</strong>mation on fuel reactivity. For a small set of chemicals, ALOHA uses<br />

values <strong>for</strong> fuel reactivity referenced in Appendix C of John L. Woodward, Estimating the<br />

Flammable Mass of a Vapor Cloud, published by American Institute of Chemical<br />

Engineers, 1998. For all other flammable chemicals, ALOHA assigns medium reactivity.<br />

Program structure:<br />

TECHNICAL DOCUMENTATION<br />

Generally, the <strong>project</strong> only allows the new scenarios <strong>for</strong> that subset of existing ALOHA<br />

chemicals that are classified by the National Fire Protection Association's Fire Protection<br />

Guide to Hazardous Materials as a category 3 or 4 flammable hazard. This includes<br />

flammable gases <strong>and</strong> liquids with a flash point below 100 °F. The model will allow the<br />

user to select combustible liquids (category 1 <strong>and</strong> 2 flammable hazard) but may, <strong>for</strong> lowtemperature<br />

scenarios, provide a warning to the user that the chemical may not burn at<br />

the user-specified temperature.<br />

Figure 1 shows the possible scenarios <strong>for</strong> a chemical release from a tank, pool, or<br />

pipeline with an ignition source present at the beginning of the release. For a delayed<br />

ignition, there may be time <strong>for</strong> a flammable cloud to develop, thereby creating the<br />

potential <strong>for</strong> a flashfire or explosion. For a pool release, there is also the potential <strong>for</strong> a<br />

flashback causing a subsequent pool fire. This is not modeled in this <strong>project</strong>.<br />

4

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