Dow's Fire & Explosion Index Hazard Classification Guide,

This well known security best-seller is designed to aid the consumer quantify the anticipated harm of power hearth and explosion incidents in lifelike phrases, establish the gear more likely to give a contribution to the construction or escalation of an incident, and speak the hearth and explosion chance power to administration. in accordance with Dow's fireplace and Explosion possibility research application, the index presents a step by step, target overview of the particular fireplace and explosion, in addition to reactivity capability of strategy gear and its contents.Content:

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Additional resources for Dow's Fire & Explosion Index Hazard Classification Guide, Seventh Edition

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1994 DETERMINATION OF FIRE AND EXPLOSION INDEX The Fire and Explosion Index calculation is used for estimating the damage that would probably result from an incident in a process plant. The various contributing factors, such as type of reaction. process temperatures, pressures, quantities of fuel, etc.. indicate the probability and potential magnitude of a fuel or energy release resulting from process control failures, equipment failures or from vibration or other sources of stress fatigue. Effects of a fire and/or fuel-air explosion following the release of a flammable material and its ignition are categorized according to the immediate causes: a.

3 . 9 1 0 5 10 - 25 MATERIAL FACTOR (MF) 20 See Appendix E for data equations. 0 9. Maximum Probable Days Outage (MPDO) As noted in the introduction, the estimate of Maximum Probable Days Outage (MPDO)is a necessary step in assessing the potential Business Interruption (BI) from a loss incident. The dollar impact of Business Interruption can often times equal or exceed that of property damage. depending cn inventory levels and product demand. A number of different conditions can cause variations in the relationship of MPDO to property damage.

The BI loss is to be entered on line 10 of the Process Unit Risk Analysis Summary, page 6 and in the Manufacturing Risk Analysis Summary, page 7. A. 1994 DISCUSSION OF MPPD, BI AND PLANT LAYOUT What is an acceptable Maximum Probable Property Damage (MPPD) and Business Intenuption (BI) risk? This is not an easy question to answer. It depends on the type of plant. For example, the potential loss from a hydrocarbon plant will always exceed the loss of a STYROFOAM0 plant. The best approach is to compare plants in similar technology areas.

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