3. Photos shown in this presentation may depict situations that are not in compliance
with applicable OSHA/MSHA/FHWA requirements.
It is not the intent of the content developers to provide compliance-based training in
this presentation, the intent is more to address hazard awareness in the construction
and mining industry, and to recognize the overlapping hazards present in many
workplaces.
It should NOT be assumed that the suggestions, comments, or recommendations
contained herein constitute a thorough review of the applicable standards, nor
should discussion of “issues” or “concerns” be construed as a prioritization of
hazards or possible controls. Where opinions (“best practices”) have been expressed,
it is important to remember that safety issues in general and jobsites specifically will
require a great deal of site- or hazard-specificity – a “one size fits all” approach is not
recommended, nor will it likely be very effective.
4. No representation is made as to the thoroughness of the presentation, nor to the
exact methods of remediation to be taken. It is understood that site conditions vary
constantly, and that the developers of this content cannot be held responsible for
safety problems they did not address or could not anticipate, nor those which have
been discussed herein or during physical presentation. It is the responsibility of the
employer, its subcontractors, and its employees to comply with all pertinent rules
and regulations in the jurisdiction in which they work.
It is assumed that individuals using this presentation or content to augment their
training programs will be “qualified” to do so, and that said presenters will be
otherwise prepared to answer questions, solve problems, and discuss issues with their
audiences.
Areas of particular concern (or especially suited to discussion) have additional
information provided in the “notes” section of slides throughout the program…as a
presenter, you should be prepared to discuss all of the potential issues/concerns, or
problems inherent in those photos particularly.
5. Know and understand:
Principles of combustible and flammable liquids,
including limits, and classification
Basics of fire chemistry
Fire classes
How extinguishing agents work
Be familiar with
Types of fire extinguishers
How to control flammable liquid hazards
Basic fire prevention and protection
6. Annual $2.2 billion loss
Over 300 workplace deaths
Over 3% of workplace fatalities
Fire losses can be catastrophic
Unlike other hazards, the event may not be self-
limiting
Fire hazards MUST be controlled to a low level of
probability, as losses are so high
7. Lower explosive limit, LEL (also LFL)
The minimum concentration of vapor in air below
which a spread of flame does not occur when the
vapor is in contact with a source of ignition
Acetone LEL = 2.5%
Upper explosive limit, UEL (also UFL)
The maximum concentration of vapor in air above
which a spread of flame does not occur when the
vapor is in contact with a source of ignition.
Acetone UEL = 12.8%
Explosive range (also flammable range)
The spread between the LEL and UEL
Acetone explosive range = 2.5 - 12.8%
10. Ignition temperature
The temperature at which ignition (production of
flame) and burning will be continued after the
source of ignition or the source of heat is removed
Flash point
The lowest temperature at which enough vapor is
given off near the surface of a liquid to produce a
flammable mixture with air.
Flammable liquid
Liquids with a flash point below 100 F
Combustible liquid
Liquids with a flash point 100 F or greater
11. NFPA OSHA Flashpoint Boiling point
Flammable
Liquids
4 IA <73F < 100F
3 IB <73F >100F
3 IC >73 - <100F
Combustible
liquids
2 II >100 - <140F
2 IIIA >140 - <200F
1 IIIB >200F
Non-
combustible
0
12. Flame fire
Gases or vapors
High burning rate
Surface fire
Burning rate may be slow
Explosion
An event leading to a rapid increase of pressure
13. Deflagration
Combustion wave propagates at subsonic velocity
Detonation
Combustion wave propagates at supersonic velocity
Gas or vapor explosion
Combustion of pre-mixed gas or vapor
Dust explosion
Finely divided solids, suspended in air
14. BLEVE
Boiling Liquid Expanding
Vapor Explosion
Flash evaporation after
vessel rupture
May not involve
combustion
18. Four components:
Oxygen
Heat
Fuel
Reaction
Removing any
component stops
the fire
19. Cooling
Applying water
Removing Fuel
Shut off supply to gas or liquid fires
Pump liquid from burning tanks
Limiting oxygen
Mechanical smothering
Foam
Displace oxygen with inert gas
Interrupt chain reaction
Capture free radicals using an extinguishing agent
20. Class A
Ordinary combustibles
Wood, paper, rubbish
Extinguish with water
Class B
Flammable liquids
Water may aggravate a burning liquid fire
Extinguish with foam, chemical agents
21. Class C
Fires in electrical equipment
Use non-conductive extinguishing agent
Class D
Combustible metal fires
Extinguish by smothering with dry powder
Water will cause burning metals to explode
Special categories
22. Water
Removes heat from a fire
Streams, spray or fog
Best for Class A fires
Not for electrical or combustible metal fires
Water mist may be used on electrical fires. These are special
fire extinguishers, filled with distilled water, that produce a fine
mist (no solid stream of water)
Foam
Excludes oxygen from burning liquid fires
Aqueous Film Forming Foam (AFFF)
Fire can re-ignite if foam breaks down
24. Dry Chemical
Inhibit chain reactions
Sodium or potassium bicarbonate
For Class B or C fires
Multipurpose Dry Chemical
Monoammonium phosphate
For Class A, B, or C fires
Excludes oxygen by coating surfaces
Dry Powder
Excludes oxygen from burning metal
Sodium chloride, graphite
25. Water
For Class A fires
Minimum 2 1/2 gallons or 2A
"A" unit rating = 5 quart water
or equivalent
Usually stored pressure type
Inverting soda-acid
extinguisher are obsolete and
dangerous
Foam
For Class A or B
Stored pressure
26. Dry Chemical
Class ABC or BC
"B" unit rating = 1
square foot flammable
liquid fire
No rating for "C“
Stored pressure or
cartridge- operated
27. Liquified Gas
CO2, Class BC
HALON, Class
ABC
Dry powder
Class D (no
rating)
Cartridge
operated
28. Placement
Maximum 75 foot travel distance for "A" or "D“
Maximum 50 foot travel distance for "B“
Inspection
Monthly visual
Annual maintenance
5-year hydrotest
12 yr. hydrotest for dry chemical or HALON (6 yr. recharge)
Training and Education
For all workplaces with fire extinguishers
29. P.A.S.S.
Pull Pin
Aim at base of fire
Squeeze handle
Sweep back and forth
30. Flammable liquid safety
Limit quantities
Store liquids in
flammable liquid
cabinets or rooms
Use "Safety" cans
Ventilation
Pressure relief valves
31. Flammable liquid safety
Controlling ignition sources
Grounding and bonding
Non-sparking tools
Approved dispensing hoses
Classified "explosion proof"
wiring
"Hot Work Permit“
For welding, etc.
Test for LEL
Observer stands by with
extinguisher or fire hose
32. Fire Suppression Systems
Automatic sprinklers
Wet pipe (buildings)
Dry pipe (industrial)
Deluge
Dry chemical
CO2, HALON