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Dow Fire

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A step-by-step objective evaluation of the realistic fire or ... Maximum Probable Days Outage (MPDO) Business Interruption (BI) 14. 15. 16. 17. 18. So What! ... – PowerPoint PPT presentation

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Title: Dow Fire


1
2004 CSChE-PSM Summer Institute
  • Dow Fire Explosion Index
  • prepared by
  • Steve Coe
  • Irving Oil

2
Dow FEIFire Explosion Index
  • A step-by-step objective evaluation of the
    realistic fire or explosion potential of
    processing or storage equipment.
  • Purpose is to
  • Quantify expected fire and explosion damage
  • Identify equipment likely to contribute
  • Communicate FE risk to management

3
Dow FEI Some History
  • Originally developed 1964, now 7th edition.
  • Based on empirical analysis of actual events.
  • Widely used in many industries.
  • Referenced in some countries regulations.
  • Insurance assessments tend to be worst imaginable
    case.
  • FEI is a more realistic case that could
    actually happen.

4
FEI Procedure
5
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6
FEI - General Information
7
Material Factor
  • A measure of the intrinsic rate of potential
    energy release from a fire or explosion.
  • Obtained from the NFPA ratings NF and NR.
  • Adjusted for operating temp.
  • Mixtures can be accommodated.

8
General Hazards Event Magnitude
  • General Process Hazards Penalty Factor
    Range
  • Base Factor 1.00
  • A. Exothermic Reactions 0.30 to 1.25
  • B. Endothermic Processes 0.20 to 0.40 
  • C. Matl Handling and Transfer 0.25 to
    1.05 
  • D. Enclosed/ Indoor Process 0.25 to
    0.90 
  • E. Access 0.20 to 0.35 
  • F. Drainage and Spill Control 0.25 to
    0.50
  •  
  • Add them up
  • General Process Hazards Factor F1

9
Special Hazards - Likelihood
  • 2. Special Hazards Penalty Range
  • Base Factor 1
  • A. Toxicity 0.2 0.8
  • B. Sub-Atm pressure 0.5
  • C. Operation in flammable range
  • storage 0.5
  • process upset 0.3
  • always in flammable 0.8
  • D. Dust Explosion 0.25 2.0
  • E. Pressure operating/relief 0 0.85
  • F. Low Temperature 0.2 0.3
  • G. Quantity of material
  • in process 0.1 3.0
  • in storage 0.1 1.65
  • H. Corrosion/erosion 0.1 0.75
  • I. Leakage joints, packing 0.1 1.5
  • J. Fired equipment 0.1 1.0
  • K. Hot Oil system 0.15 1.15
  • L. Rotating Equipment 0.5

10
FEI - Calculation
  • General Process Hazard Factor F1
  • Special Process Hazard Factor F2
  • Process Unit Hazard Factor (F1xF2) F3
  • FEI F3 x MF

11
Loss Control Credit Factors
12
Loss Control Credit Factors
  • Process Control Factors (C1)
  • Emergency Power, Cooling, Computer Control, Inert
    gas, Hazard Analysis, Operating Instructions
  • Material Isolation Factors (C2)
  • Remote control valves, Dump tanks, Drainage,
    Interlocks
  • Fire Protection Factors (C2)
  • Leak detection, Steel protection, Fire Water
    supply, Deluge, Foam, Monitors, Cable Protection
  • Loss Control Credit Factor
  • (LCCF) C1xC2xC3

13
FEI Risk Analysis
  • FEI
  • Radius of Exposure ? Area of Exposure
  • Value of the Area/Volume of Exposure
  • Damage Factor (function of F3 MF)
  • Base Maximum Probable Property Damage
  • Loss Control Credit Factor (LCCF)
  • Actual MPPD
  • Maximum Probable Days Outage (MPDO)
  • Business Interruption (BI)

14
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15
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16
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17

18
So What!
  • Useful for plant siting, plot plan development
  • Eliminate penalties for Inherent Safety
  • Incorporate Loss Control Credit Factors
  • Technologically elegant can be Minimum Risk

19
How?
  • Include calculation of risk a part of the plant
    design project.
  • Getting a Quick Handle on Major Site Hazards
    guide on the PSM Division page of the CSChE web
    site
  • www.cheminst.ca/division/psm/index.htm
  • Dr. F. Khan, Dr. P. Amyotte Quantifying
    Inherent Safety Aspects of Dow Indices

20
Dow Fire and Explosion Index
  • What questions are there?
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