1. 2. Hazards Survey
Suitable for identifying hazards for equipment design,
layout, storage etc.
Can be as simple as survey of inventory/stock of hazardous
Chemical.
Can be fairly rigorous/tough such as Dow Fire and
Explosion Index (Dow F&EI).
Requires little experience and gives quick result.

2. Dow Fire and Explosion Index (Dow F&EI)
Tailored for storage, handling and processing of explosive and flammable material in chemical processing industry (CPI).
Systematic approach using rating form.
Can be used at an early stage of a project and for audit of existing plant.
Final rating number (i.e. F&E Index) will provide a relative ranking of the hazard.
Could also estimate damage radius using Dow correlation.
Can also estimate dollar/RM losses in the event of accident using consequences analysis form.

3. Dow's Fire & Explosion Index Hazard Classification Guide, 7th Edition
American Institute of Chemical Engineers (AIChE)
ISBN: 
Pub No: T-80
Paperback
83 pages
June 1994
Purchase From Wiley
Description: This popular safety best-seller is designed to help the user quantify the expected damage of potential fire and explosion incidents in realistic terms, identify the equipment….

4. Steps in Dow F&EI Divide the process into separate units.
Select units that have highest likelihood of hazard (e.g. from process safety checklists).
Determine material factor (MF) from table (e.g. Table 10-1).
Higher MF means higher flammability and/or more explosive.
Determine Penalty Factor (F1) for general process hazards.
Determine Penalty Factor (F2) for special process hazards.
Calculate F&EI = (F1 x F2) x MF

5. Penalty Factor (F1) for general process hazards
Exothermic reaction that might self heat.
Endothermic reaction that could react because of external heat source.
Material handling and transfer.
Enclosed process unit.
Limited access for emergency equipment.
Poor drainage and spill control.

6. Penalty Factor (F2) for special process hazards
1. Toxic material that could impede/delay fire fighting
Less than atmospheric pressure- vacuum (outside air could leak into system)
Operation in/near flammability limit
Dust explosion risk
High pressure risk
Low temp operation that could lead to embrittlement (fragile)
Quantity of flammable material
Corrosion and erosion of process unit structures
Leakage around joints and packing
Used of fired heater (source of ignition)
Hot oil HEX (source of ignition)
Large rotating equipment

7. Material Factor; MF

8. Penalty Factors; F1 and F2

11. The following example shows how this method is applied (Dow F&EI).
To carry out this, we need Dow F&EI index booklet for details in determining the penalties (F1 and F2)

13. barrier
Railcar

14. Deluge/flood system
Dike/dam/barrier

15. Penalty Factor; F1 and F2

16. Results F&EI = 106 and Table 10.2 gives
Degree of Hazard = Intermediate
Refer to Dow index booklet and based on this
F&EI value,
The radius of exposure = 90 ft
Thus, the unloading facilities must be located a
minimum of 90 ft from other equipment or
processes.

17. DOW Chemical Exposure Index (DOW CEI)
A simple method of rating the relative acute health hazard potential for people (communities) in neighboring plants arising from possible chemical release incidents.

18. END OF PART 3
THANK YOU