|
ABOUT
THE LAW ENFORCEMENT AND CORRECTIONS
STANDARDS AND TESTING PROGRAM
The
Law Enforcement and Corrections Standards and Testing Program is sponsored
by the Office of Science and Technology of the National Institute of Justice
(NIJ), U.S. Department of Justice. The program responds to the mandate
of the Justice System Improvement Act of 1979, which directed NIJ to encourage
research and development to improve the criminal justice system and to
disseminate the results to Federal, State, and local agencies.
The Law Enforcement
and Corrections Standards and Testing Program is an applied research effort
that determines the technological needs of justice system agencies, sets
minimum performance standards for specific devices, tests commercially
available equipment against those standards, and disseminates the standards
and the test results to criminal justice agencies nationally and internationally.
The program operates through:
The
Law Enforcement and Corrections Technology Advisory Council (LECTAC),
consisting of nationally recognized criminal justice practitioners from
Federal, State, and local agencies, which assesses technological needs
and sets priorities for research programs and items to be evaluated and
tested.
The
Office of Law Enforcement Standards (OLES) at the National Institute
of Standards and Technology, which develops voluntary national performance
standards for compliance testing to ensure that individual items of equipment
are suitable for use by criminal justice agencies. The standards are based
upon laboratory testing and evaluation of representative samples of each
item of equipment to determine the key attributes, develop test methods,
and establish minimum performance requirements for each essential attribute.
In addition to the highly technical standards, OLES also produces technical
reports and user guidelines that explain in nontechnical terms the capabilities
of available equipment.
The National
Law Enforcement and Corrections Technology Center (NLECTC), operated by
a grantee, which supervises a national compliance testing program conducted
by independent laboratories. The standards developed by OLES serve as
performance benchmarks against which commercial equipment is measured.
The facilities, personnel, and testing capabilities of the independent
laboratories are evaluated by OLES prior to testing each item of equipment,
and OLES helps the NLECTC staff review and analyze data. Test results
are published in Equipment Performance Reports designed to help justice
system procurement officials make informed purchasing decisions.
Publications are available at no charge through the National Law Enforcement
and Corrections Technology Center. Some documents are also available online
through the Internet/World Wide Web. To request a document or additional
information, call 800-248-2742 or 301-519-5060, or write:
| The
National Institute of Justice is a component of the Officeof Justice
Programs, which also includes the Bureau of Justice Assistance, the
Bureau of Justice Statistics, the Office of Juvenile Justice and Delinquency
Prevention, and the Office for Victims of Crime. |
National
Institute of Justice
|
The
technical effort to develop this report was conducted under Interagency
Agreement 94-IJ-R-004, Project No. 96-002.
This report was prepared with the assistance of the Office of Law
Enforcement Standards (OLES) of the National Institute of Standards
and Technology (NIST) under the direction of Kathleen M. Higgins,
Director of OLES.The work resulting from this report was sponsored
by the
National Institute of Justice (NIJ), Dr. David G. Boyd, Director,
Office of Science and Technology.
|
FOREWORD
The
Office of Law Enforcement Standards (OLES) of the National Institute of
Standards and Technology (NIST) furnishes technical support to the National
Institute of Justice (NIJ) program to strengthen law enforcement and criminal
justice in the United States. OLES's function is to conduct research that
will assist law enforcement and criminal justice agencies in the selection
and procurement of quality equipment.
OLES is:
(1) Subjecting existing equipment to laboratory testing and evaluation,
and (2) conducting research leading to the development of several series
of documents, including national standards, user guides, and technical
reports.
This document
covers research conducted by OLES under the sponsorship of the National
Institute of Justice. Additional reports as well as other documents are
being issued under the OLES program in the areas of protective clothing
and equipment, communications systems, emergency equipment, investigative
aids, security systems, vehicles, weapons, and analytical techniques and
standard reference materials used by the forensic community.
Technical
comments and suggestions concerning this report are invited from all interested
parties. They may be addressed to the Office of Law Enforcement Standards,
National Institute of Standards and Technology, 100 Bureau Drive, Stop
8102, Gaithersburg, MD 20899-8102.
Dr.
David G. Boyd, Director
Office of Science and Technology
National Institute of Justice
CONTENTS
| 1. |
|
INTRODUCTION |
| 2. |
|
ANALYTICAL
SPILL SIZE PREDICTION |
| 3. |
|
SPILL
AREA |
| 4. |
|
SPILL
IGNITION EXPERIMENTS |
|
4.1
|
Nonporous
Surfaces |
|
4.2 |
Carpeted
Surfaces |
| 5. |
|
ANALYSIS
AND RESULTS |
|
5.1 |
|
Spill
and Burn Areas |
|
5.2 |
|
Peak Heat Release Rate |
|
5.3 |
|
Heat
Release Rate Per Unit Area |
| 6. |
|
CONCLUSIONS |
| 7. |
|
REFERENCES |
| APPENDIX
A--HEAT RELEASE RATES |
TABLES
| Table
1. |
Physical
properties of spilled fuels 3 |
|
| Table
2. |
Spill thickness predictions |
|
| Table
3. |
Comparison of predicted and empirically derived spill thickness |
|
| Table
4. |
Carpet flooring composition |
|
| Table
5. |
Carpet spill areas |
|
| Table
6. |
Gasoline fire experimental matrix |
|
| Table
7. |
Nonporous spill fire and pool fire HRR |
|
| Table
8. |
Carpet spill fire and pool fire HRR |
|
FIGURES
| Figure
1. |
Fuel
pour apparatus. The dimension "A" is 510 mm ± 10
mm. The container opening diameter and volume are approximate |
|
| Figure
2. |
Infrared
image of gasoline spill on wood parquet floor |
|
| Figure
3. |
Infrared
image of gasoline on vinyl tile floor |
|
| Figure
4. |
Gasoline
spill fire under the furniture calorimetry hood in the large Fire
Research Laboratory at NIST |
|
| Figure
5. |
Ignition of 1000 mL gasoline spill on wood parquet flooring
|
|
| Figure
6. |
Burning in the cracks of the parquet flooring |
|
| Figure
7. |
Burning in the seams of the vinyl tile flooring |
|
| Figure
8. |
1000 mL gasoline spill fire burn pattern on wood parquet floor |
|
| Figure
9. |
Close-up of gasoline spill fire burn pattern on wood parquet floor |
|
| Figure
10. |
1000 mL gasoline spill fire pattern on vinyl tile floor |
|
| Figure
11. |
Close-up of gasoline spill fire pattern on vinyl floor |
|
| Figure
12. |
Close-up of gasoline spill fire burn pattern on vinyl floor. Photo
shows the retreat of the tiles at the intersections |
|
| Figure
13. |
Vinyl tile removed after a 1000 mL gasoline spill fire. Damage to
the fiberboard is limited to the vinyl tile seam locations |
|
| Figure
14. |
1000 mL kerosine spill burn pattern |
|
| Figure
15. |
1000 mL gasoline spill fire on carpet 1 at approximately 10 s |
|
| Figure
16. |
1000 mL gasoline spill fire on carpet 1 at approximately 100 s |
|
| Figure
17. |
1000 mL gasoline spill fire on carpet 2 at approximately 10 s |
|
| Figure
18. |
1000 mL gasoline spill fire on carpet 2 at approximately 100 s |
|
| Figure
19. |
Close-up view of 250 mL gasoline fire on carpet 1 |
|
| Figure
20. |
Close-up view of 250 mL gasoline fire on carpet 1 |
|
| Figure
21. |
Doughnut burn pattern on carpet 1. 250 mL gasoline fire, extinguished
at approximately 146 s with CO2 |
|
| Figure
22. |
Doughnut burn pattern on carpet 1. 1000 mL gasoline fire, extinguished
at approximately 111 s with CO2 |
|
| Figure
23. |
Doughnut burn pattern on carpet 2. 250 mL gasoline fire, extinguished
at approximately 171 s with CO2. Exposed padding can be seen in the
center and toward the left side of the pattern |
|
| Figure
24. |
Doughnut burn pattern on carpet 2. 1000 mL gasoline fire, extinguished
at approximately 1763 s ("30 min) with CO2 |
|
| Figure
25. |
Carpet padding intact inside the doughnut pattern. 500 mL gasoline
spill fire on carpet 2. Fire was extinguished at approximately 234
s with CO2 |
|
| Figure
26. |
1000 ML gasoline spill fire on carpet 2 at approximately 600 s. This
fire yielded the pattern shown in figure 24. |
|
| Figure
27. |
Carpet and padding removed from floor leaving doughnut pattern behind
results shown for 250 mL gasoline spill on carpet 1, extinguished
with CO2 after approximately 213 s of burning |
|
| Figure
28. |
Gasoline
spill and burn pattern areas on wood parquet floors |
|
| Figure
29. |
Gasoline spill and burn pattern areas on vinyl tile floors |
|
| Figure
30. |
Gasoline spill and initial burn areas on carpet covered floors |
|
| Figure
31. |
Peak heat release rates for gasoline spills on wood parquet and vinyl
tile floors |
|
| Figure
32. |
Peak heat release rates for gasoline spills on carpet covered floors |
|
| Figure
33. |
Average peak heat release rate per unit area for gasoline spill fires
on wood parquet and vinyl tile floors. |
|
| Figure
34. |
Average peak heat release rate per unit for gasoline spill fires on
carpeted floors |
|
| Figure
A1. |
Heat release rates for 250 mL gasoline spill fires on wood parquet
floors |
|
| Figure
A2. |
Heat release rates for 500 mL gasoline spill fires on wood parquet
floors |
|
| Figure
A3. |
Heat release rates for 1000 mL gasoline spill fires on wood parquet
floors |
|
| Figure
A4. |
Heat release rates for 250 mL gasoline spill fires on vinyl tile flooring |
|
| Figure
A5. |
Heat release rates for 500 mL gasoline spill fires on vinyl tile flooring |
|
| Figure
A6. |
Heat release rates for 1000 mL gasoline spill fires on vinyl tile
flooring |
|
| Figure
A7. |
Heat release rates for 250 mL spill fires on carpet 1 |
|
| Figure
A8. |
Heat release rates for 500 mL spill fires on carpet 1 |
|
| Figure
A9. |
Heat release rates for 1000 mL gasoline spill fires on carpet 1 |
|
| Figure
A10. |
Heat release rates of 250 mL gasoline spill fires on carpet 2 |
|
| Figure
A11. |
Heat release rates for 500 mL gasoline spill fires on carpet 2 |
|
| Figure
A12. |
Heat release rates of 1000 mL gasoline spill fires on carpet 2 |
|
|
COMMONLY
USED SYMBOLS AND ABBREVIATIONS
A ampere
H henry nm nanometer
ac alternating current h
hour No. number
AM amplitude modulation
hf high frequency o.d. outside diameter
cd candela
Hz hertz W ohm
cm centimeter
i.d. inside diameter p. page
CP chemically pure
in inch Pa pascal
c/s cycle per second
IR infrared pe probable error
d day
J joule pp. pages
dB decibel
L lambert ppm parts per million
dc direct current
L liter qt quart
°C degree Celsius lb pound rad radian
°F degree Fahrenheit lbf pound‑force rf radio frequency
dia diameter
lbf in pound‑force inch
rh relative humidity
emf electromotive force
lm lumen s second
eq equation
ln logarithm (base e) SD standard deviation
qF farad
log logarithm (base 10) sec. section
fc footcandle
M molar SWR standing wave ratio
fig. figure
m meter uhf ultrahigh frequency
FM frequency modulation min minute UV ultraviolet
ft foot
mm millimeter V
volt
ft/s foot per second mph miles per hour vhf very
high frequency
g acceleration
m/s meter per second W watt
g gram
N newton l wavelength
gr grain
N m newton meter
wt weight
area=unit2 (e.g., ft2, in2, etc.); volume=unit3 (e.g., ft3, m3, etc.)
PREFIXES
d deci (10-1) da deka
(10)
c centi (10-2) h hecto
(102)
m milli (10-3) k kilo
(103)
µ micro (10-6) M mega
(106)
n nano (10-9) G giga
(109)
p pico (10-12) T tera
(1012)
|
COMMON
CONVERSIONS
(See ASTM E380)
|
| 0.30480
m =1ft |
4.448222 N = l lbf |
| 2.54
cm = 1 in |
1.355818
J =1 ft lbf |
| 0.4535924
kg = 1 lb |
0.1129848
N m = l lbf in |
| 0.06479891g
= 1gr |
14.59390
N/m =1 lbf/ft |
| 0.9463529
L = 1 qt |
6894.757
Pa = 1 lbf/in2 |
| 3600000
J = 1 kW hr |
1.609344
km/h = l mph |
Temperature: T C
= (T F
-32)×5/9
|
Temperature:
T F
= (T C
×9/5)+32
|
|

FLAMMABLE
AND COMBUSTIBLE LIQUID
SPILL/BURN PATTERNS
Anthony
D. Putorti Jr.
Jay A. McElroy
Daniel Madrzykowski
Fire
Safety Engineering Division, Building and Fire Research Laboratory
National Institute of Standards and Technology, Gaithersburg, MD 20899-8641
Discussions
with fire investigators indicate that it would be beneficial to have
the ability to predict the quantity of liquid fuel necessary to create
a burn pattern of a given size. Full-scale spill and fire experiments
were conducted with gasoline and kerosene on vinyl, wood parquet, and
carpet covered plywood floors using various quantities of fuel. Spill
areas were measured, and for nonporous floors the results were compared
to analytical predictions. Burn pattern areas are correlated with the
spill areas, resulting in a method for predicting the quantity of spilled
fuel required to form a burn pattern of a given size. The heat release
rates of the fuel spill fires were determined through experiment and
compared to an existing reference for burning liquid pools of the same
surface area. The peak spill fire heat release rates for nonporous surfaces
were found to be approximately 1/8 to 1/4 of those from equivalent area
pool fires. The peak heat release rates for spill fires on carpet were
found to be approximately equal to those from equivalent area pool fires.
The heat release rates can be used as inputs for fire modeling or for
evaluating fire scenarios.
Key words:
accelerants; arson; building fires; burn patterns; carpets; char; charring;
fire investigations; fire measurements; flammable liquids; floors; floor
coverings; heat release rate; pour patterns; spill fires.
1.
INTRODUCTION
Discussions
with fire investigators indicate that it would be beneficial to have the
ability to predict the quantity of liquid fuel necessary to create a burn
pattern of a given size. Past studies conducted with liquid fuels contained
too many variables to determine the relationship between spill quantity
and burn pattern area. In an effort to reduce the variables involved,
and thereby understand the process of pattern formation, experiments are
conducted in the laboratory under an instrumented exhaust hood, without
a room or enclosure. This layout would represent a fire burning in a large
space, or in an enclosure before the formation of a significant upper
layer of heated combustion products. Due to the rapid combustion of fuel
spills on nonporous surfaces, the results of the study may be applicable
to many enclosures.
Analytical
predictions and empirical data concerning the spread of liquids on ideal
surfaces are available in the literature. The analytical predictions are
based on perfectly smooth, level, and nonporous surfaces. The empirical
data is derived from spills on very smooth level surfaces, such as epoxy-coated
concrete and metal.
The floor
materials of interest to fire investigators, such as wood and vinyl flooring,
carpet, and unsealed concrete differ from the ideal surfaces assumed in
the analytical predictions. These flooring materials contain joints and
texture, and may be porous or semiporous. The spread of liquids on these
surfaces is expected to differ from those measured or predicted on more
ideal surfaces. This study investigates the spill and burning behavior
of liquid fuels on vinyl tile, wood parquet, and carpet flooring materials.
In order to provide inputs for fire modeling that can be especially useful
in fire condition prediction and fire scenario evaluation, the heat release
rates (HRRs) of the spill fires are measured. The liquid fuels used are
gasoline and kerosene, which are commonly encountered by fire investigators
in the field.
2.
ANALYTICAL SPILL SIZE PREDICTION
The
literature [1]1 contains methods for predicting the spread
of fluids on smooth, level surfaces. The methods consist of fluid mechanics
models that assume a smooth, level surface and negligible evaporation.
This assumption will be an approximation in the case of wood and vinyl
floors due to surface texture, cracks, and the inability to produce a
perfectly smooth, level surface. The analysis is not applicable to carpeted
surfaces due to absorption into the carpet and pad.
Properties
of the spreading fuel are important to the spreading process. Characteristics
such as fuel density, viscosity, surface tension, and the interfacial
tension between the liquid, the air, and the floor surface all affect
the spreading process.
When a liquid
is spilled on a surface, a condition that is assumed to occur instantaneously
in the analytical predictions, the spreading process may be divided into
a series of three regimes, each of which is dominated by different physical
forces. The regimes occur in the following order: gravity-inertia, gravity-viscous,
and viscous-surface tension. In the gravity-inertia regime, the forces
of gravity are working to spread the fluid and are opposed by the inertia
of the fluid. In the gravity-viscous regime, the viscous forces within
the fluid oppose the gravity forces. Finally, in the viscous-surface tension
regime, the viscous forces within the fluid oppose the surface tension
forces. For the fuels and spill sizes investigated here, the spill enters
the viscous-surface tension regime very rapidly, on the order of a few
seconds from the time of the spill. The process for calculating the spill
thickness as a function of time differs depending on the spill regime
at the time of interest. Equation 1 is used to determine the time at which
the spill enters the viscous-surface tension regime. Fort > t2,
the spill is in the viscous-surface tension regime, and equation 2 may
be used to calculate the radius of the spill and derive the spill thickness.

| Where: |
t2
/ boundary time between the gravity-viscous and viscous-surface
tension regime(s) |
|
G / acceleration of gravity (9.81 m/s2) |
|
V
/ spill volume (m3) |
|
:1
/ absolute viscosity (N s/m2) |
|
F
/ Interfacial tension (N/m) |
|
<1
/ kinematic viscosity (m2/s) |

Where:
|
R /
radius of spill (m) |
|
T /
time (s) |
The spill
area was predicted as a function of time according to eq (1) and eq
(2), using the properties [2] listed in table 1. The results for two
times of interest are listed in table 2.
Table
1. Physical properties of spilled fuels
|
Properties
|
Gasoline
|
Kerosene
|
|
F
(N/m)
|
2.12
x 10-2
|
2.77
x 10-2
|
|
<
1 (m2/s)
|
4.29
x 10-7
|
2.39 x 10-6
|
|
:1
(N s/m2)
|
2.92
x 10-4
|
1.92
x 10-3
|
Table
2. Spill thickness predictions
|
Predicted Thickness, mm (in)
|
|
Fuel
|
60 s
|
120
s
|
|
Gasoline
|
0.56
(0.022)
|
0.41
(0.016)
|
|
Kerosene
|
1.3
(0.050)
|
0.89
(0.035)
|
The
spreading of liquid fuels in industrial facilities has been studied for
fire hazard analyses [3]. In these experiments, spill thickness of 0.22
mm resulted from unconfined spills of #2 fuel oil on epoxy-coated concrete
and steel surfaces. The study found that the unconfined spill thickness
was independent of the spill volume, a result that is applied in the current
study.
3.
SPILL AREA
A
series of eight spill area measurements were conducted using wood parquet
and vinyl flooring. Various quantities of fuel were poured onto sections
of flooring. The flooring sections consisted of a wood frame constructed
of 50 mm by 100 mm (2 in x 4 in) nominal wood lumber covered with 16 mm
(5/8 in) nominal plywood secured with nails. The wood parquet flooring
sections were constructed by applying adhesive to the plywood surface
and attaching the 300 mm by 300 mm (12 in by 12 in) nominal wood parquet
flooring tiles to the flooring sections. The wood tiles are coated with
a clear polyurethane finish at the factory and are manufactured with tongue
and groove connections along the tile perimeter. The vinyl flooring sections
were constructed by attaching a 6 mm (1/4 in) nominal layer of dense fiberboard
to the plywood surface with nails. Self-sticking 300 mm by 300 mm (12
in by 12 in) nominal vinyl flooring tiles were applied to the surface
of the fiberboard.
The liquid fuels were poured in the center of the flooring sections, with
approximate dimensions of 1.22 m by 1.22 m (4 ft x 4 ft), using the apparatus
shown in figure 1. The fuel was poured by rotating the container, thereby
discharging the fuel onto the center of the floor sample from a height
of 510 mm ± 10 mm. (This estimated expanded uncertainty is the
result of a Type B evaluation with a coverage factor of 2.) The fuel was
allowed to spread and sit on the surface of the flooring for a duration
of approximately 60 s. In all cases, the fuel was observed to have stopped
spreading within the 60 s time period. The temperatures of the floor samples
and fuel were approximately equal to the ambient temperature, which was
approximately 24 oC (75 oF).
Spill areas
were measured using infrared imaging. The use of infrared imaging was
made possible by emissivity differences between the flooring materials
and the fuels, which were at approximately the same temperature. This
avoided the need to add dyes or other impurities to the fuels to make
them visible. The nominal thickness of the spill was calculated from the
spill area and spill quantity. Fuel evaporation and soak-in were ignored
due to the short duration of the measurements and the use of nonporous
surfaces. Figures 2 and 3 show the extent of the spread of gasoline on
wood parquet and vinyl tile floors. The fluid traveling within the cracks
of the flooring material can be clearly seen along the periphery of the
wood parquet floor spill. The presence of these fuel dendrites was ignored
in the calculation of spill thickness.
Spill thicknesses
calculated using the analytical method are compared to the experimental
results in table 3. All of the uncertainties stated in this report, unless
otherwise noted, are expanded uncertainties derived from Type A evaluations
(statistical analysis of the data) with a coverage factor, k, equal to
2. A coverage factor of 2 corresponds to a confidence interval of approximately
95 %, assuming a normal distribution applies [4].
Due to the
assumptions made in the analytical predictions, most importantly the ideal
surface, the spreading behavior of the spill is a function of time. While
the spreading in the experiments appeared to cease in less than 60 s,
the analytical predictions using eq (1) and eq (2) indicate continual
spread. Due to the differences in the analytically predicted and empirical
spill thicknesses for the floor coverings studied, the use of the empirical
data is recommended. The analytical prediction method is useful, however,
for understanding the spreading mechanisms of a fluid spill. The predictions
could be valuable for instances where the spill method, fuels, or floor
surfaces differ from those studied in this paper. To this end, the analytical
prediction method could be used to understand the sensitivity of the spill
thickness to variables such as fuel temperature, floor temperature, fuel
variations, etc.
Table
3. Comparison
of predicted and empirically derived spill thickness
|
|
Predicted
Thickness, mm (in)
|
Empirically
Derived Thickness,
mm (in)
|
|
Fuel/Floor
Material
|
60
s
|
120
s
|
|
|
Gasoline/Wood
|
0.56
(0.022)
|
0.41 (0.016)
|
0.67
"± 0.05 (0.026 ±
0.002)
|
|
Gasoline/Vinyl
|
0.56
(0.022)
|
0.41
(0.016)
|
0.56
±0.05
(0.022 ±
0.002)
|
|
Kerosene/Wood
|
1.3
(0.050)
|
0.89
(0.035)
|
0.82
±0.05
(0.032 ±0.002)
|
|
Kerosene/Vinyl
|
1.3
(0.050)
|
0.89
(0.035)
|
0.79
±0.05
(0.031 ±0.002)
|
Spill
areas were also measured on carpeted floors. In this case, the edge of
the spill was indicated on the carpet with a black permanent marker, and
the dimensions of the elliptical spill measured with a meter stick. Two
types of carpet were used. Carpet "1" was composed of polyolefin,
with polypropylene backing. This carpet is designated as a home/office
carpet, with dense loop construction, and an approximate mass per unit
area of 0.68 kg/m2 (20 oz/yd2). Carpet "2"
was a cut pile carpet composed of nylon, with an approximate mass per
unit area of 0.85 kg/m2 (25 oz/yd2). Both carpet
types were installed over polyurethane carpet padding, with an approximate
mass per unit area of 0.98 kg/m2 (29 oz/yd2), and
attached to a plywood sub-floor with tack strips along the perimeter.
Descriptions of the carpets and padding are summarized in table 4.
Table
4.
Carpet flooring composition
|
Carpet
Flooring Component
|
Description
|
|
Carpet
1
|
Home/office
carpet with dense loop construction. Polyolefin loops and polypropylene
backing. Approximate mass per unit area of 0.68 kg/m2. |
|
Carpet
2
|
Cut
pile nylon carpet. Approximate mass per unit area of 0.85 kg/m2. |
|
Padding
|
Polyurethane
foam pad constructed from shredded foam. Approximate mass per unit
area of 0.98 kg/m2. Pad thickness approximately 10 mm. |
The
carpet spills were conducted in an identical manner to those on the nonporous
surfaces, except for the area measurement method stated above, and that
a 2.44 m x 2.44 m section of flooring was used for all of the spills.
Since the carpet and pad absorb the spilled gasoline, the spill areas
for various quantities of fuel are listed in units of area instead of
length (thickness). The results are shown in table 5.
|
Carpet
Type
|
Spill
Quantity mL (gal.)
|
Spill
Area, m2 (sq. ft.)
|
|
1
|
250
(0.066)
|
8.51
x 10-2 ± 0.00 (0.916 ± 0.00)*
|
|
1
|
500
(0.13)
|
1.63 x 10-1 ± 3.33 x 10-2 (1.76 ±
0.359)
|
|
1
|
1000
(0.26)
|
2.89 x 10-1 ± 1.49 x 10-2 (3.11 ±
0.161)
|
|
2
|
250
(0.066)
|
3.95 x 10-2 ± 1.05 x 10-2 (0.425 ±
0.113)
|
|
2
|
500
(0.13)
|
5.95 x 10-2 ± 6.44 x 10-3 (0.640 ±
6.93 x 10-2)
|
|
2
|
1000
(0.26)
|
1.07 x 10-1 ± 1.20 x 10-2 (1.15 ±
0.129)
|
4. SPILL
IGNITION EXPERIMENTS
The
full-scale fire experiments were conducted under an instrumented exhaust
hood in the laboratory. The laboratory space is temperature controlled
and for all experiments was approximately 20 oC (68 oF). The fuel was
poured over the center of each 2.44 m by 2.44 m (8.00 ft x 8.00 ft) nominal
flooring section by rotating the vessel to the horizontal. Upon completion
of the pour, a soak-in time of approximately 60 s was observed to allow
for the spread of the fuel over the surface. During the soak-in time,
an electric match consisting of a nickel-chromium wire run through a book
of paper matches, was placed in the center of the spill. The spill was
ignited at the end of the soak-in period. The real-time heat release rate
of the fire was calculated using oxygen consumption calorimetry during
the fire [5]. The nonporous flooring fires were allowed to burn until
they self-extinguished. The carpet fires were extinguished at various
times after ignition. Following extinguishment, the burn pattern resulting
from the fire was measured and photographed. The experimental setup is
shown in figures 1 and 4, while the gasoline fire experimental matrix
is shown in table 6.
4.1
Nonporous Surfaces
As
expected, the ignition and burning behaviors of gasoline and kerosene
differed. Gasoline (87 octane), a liquid with a closed cup flashpoint
of -38 oC [6], ignited readily and consistently with flame spreading rapidly
over the entire surface of the spill (see fig. 5). In addition, vapors
spread past the confines of the spill during the soak-in time, resulting
in momentary burning over a larger area, which was not measured. Spill
fires approaching extinction are shown in figures 6 and 7. In both cases,
fire can be seen lingering in the cracks and seams present in the surfaces
of the floors.
Figures 8
through 11 show the typical patterns left by the gasoline fires. Upon
inspection of the floors after the burns, it was noted that the charring
was limited to the upper surface of the flooring and in the cracks of
the tiles. In the wood parquet flooring experiments, the plywood underlayment
was undamaged. In the vinyl flooring tests, the fiberboard underlayment
was undamaged, except for charring at the seams between the tiles. The
charring of the fiberboard can be seen in figures 12 and 13 where the
tiles pulled away from each other at the seams upon fire exposure.
Kerosene,
a liquid with a closed cup flashpoint of 55 oC [7], did not ignite readily
or consistently. The kerosene failed to ignite in most cases. In some
of the experiments, the kerosene did ignite in the locality of the matches
and slowly spread in the confines of cracks in the floor. This behavior
led to the pattern shown in figure 14. The kerosene fires self-extinguished
leaving large areas of the spill unburned. Given the limited amount of
burning from the kerosene, most of the experiments were conducted with
gasoline.
Table
6. Gasoline fire experimental matrix
|
Floor
Type
|
Spill
Quantity
(mL)
|
Number
of
Experiments
|
| Wood
Parquet |
250
|
3
|
| Wood
Parquet |
500
|
3
|
| Wood
Parquet |
1000
|
3
|
| Vinyl |
250
|
3
|
| Vinyl |
500
|
3
|
| Vinyl |
1000
|
4
|
| Carpet
1 |
250
|
3
|
| Carpet
1 |
500
|
3
|
| Carpet
1 |
1000
|
3
|
| Carpet
2 |
250
|
3
|
| Carpet
2 |
500
|
3
|
| Carpet
2 |
1000
|
4
|
4.2
Carpeted Surfaces
The
spill fires on carpeted flooring utilized gasoline (87 octane) as the
spilled fuel. As with the nonporous surfaces, the gasoline ignited readily
and consistently with flame spreading rapidly over the entire surface
of the spill. In addition, vapors spread past the confines of the spill
during the soak-in time, resulting in momentary burning over a larger
area, which was not measured. The two types of carpet differed qualitatively
in the rate of flame spread over the carpet surface. The flame spread
rate of the cut pile nylon carpet (carpet 2) was significantly less than
that of the polyolefin carpet (carpet 1) of loop construction. The flame
spread rates were not characterized quantitatively, but the fire area
of the polyolefin carpet experiments more than doubled in 90 s, as opposed
to the nylon carpet experiments where the burn area only increased slightly
over the same time period. This behavior is illustrated in figures 15
through 18.
Close-up
views of the burning carpet spills are shown in figures 19 and 20.
Post-fire,
the burn pattern present on the carpeted floors exhibited a "doughnut"
type pattern, as can be seen in figures 21 through 24. The presence of
gasoline was limited to the inside doughnut, where significant quantities
of fuel were present. The melted carpet material inside the doughnut protected
the carpet padding from the effects of the fire (fig. 25). The protected
carpet pad was soaked with gasoline post-fire, and could be reignited
with an open flame. Several of the nylon carpeted fires were allowed to
burn for extended periods of time, approximately 1800 s (30 min), until
the fire consisted of distributed areas of small individual flames (fig.
26). The protected carpet padding inside the doughnut pattern was soaked
with gasoline after the extended burn time. After the fires were extinguished,
the carpet and padding could be removed, leaving the doughnut pattern
attached to the underlying plywood flooring. This is shown in figure 27.
5.
ANALYSIS AND RESULTS
5.1 Spill
and Burn Areas
The spill
areas and burn areas for the nonporous floors are compared in figures
28 and 29. The error bars on the graphs represent the expanded uncertainty
in the measurement of the spill area. The graphs illustrate good agreement
between the spill and burn areas for gasoline. The burn areas from the
gasoline spill fires on wood and vinyl floors are well represented by
a linear curve fit. The y-intercept is positive, suggesting the effects
of uncertainty, or that the burn area is slightly larger than the spill
area. For wood floors, the latter is illustrated by the comparison of
the spill and burn areas. In the case of vinyl, however, the spill and
burn areas are essentially the same. Note that for the wood and vinyl
surfaces, the spill areas on the graph are extrapolated from the 250 mL
spills to the 500 mL and 1000 mL spills. The basis for the extrapolation
was previous work in the literature [3] where unconfined spill thicknesses
on nonporous surfaces were found to be independent of spill volume. Points
are shown at 500 mL and 1000 mL in order to illustrate the uncertainty
in the extrapolation, derived from the law of propagation of uncertainty
and the uncertainty in the 250 mL result.
The spill
and initial burn areas for the carpet experiments, shown in figure 30,
are well represented by a linear curve fit. The areas are greater for
the low pile looped polyolefin carpet as compared to the cut pile nylon
carpet as a consequence of the quantity of fuel the carpet is able to
hold. In both cases, the y-intercept is positive due to uncertainties
and/or the pouring of the fuel. Since the area of the pour stream is the
same for all of the pours, it would compose a greater percentage of the
spill area at smaller spill volumes. There is also a small amount of slop
and splatter that occurs when the fuel stream contacts the surface of
the floor. As the spill volume approaches zero, a minimum spill area would
be expected, and the extrapolation would cease to be valid. Note that
the spill areas of the porous surfaces are an order of magnitude smaller
than those on the nonporous surfaces studied.
5.2 Peak
Heat Release Rate
The peak
heat release rate versus spill volume relationships for the vinyl and
wood flooring are well represented by a linear curve fit, shown in figure
31. Note that the y-intercept for the vinyl flooring is positive; it is
the result of uncertainty in the measurement, or possibly it illustrates
the contribution of the vinyl flooring material to the heat release rate.
In contrast to the vinyl-flooring plot, the linear fit for the wood flooring
has a negative y-intercept. This could be the result of uncertainty, or
the combined effects of the heat release rate contribution of the flooring
and the fluid lost into the cracks of the flooring material.
The peak
heat release rate versus spill volume of the carpeted floors, shown in
figure 32, are both represented well by a linear fit, with the polyolefin
carpet spills having greater rates of heat release than the nylon carpet
spills, at the spill sizes examined. This result was expected given the
qualitative behavior observed during the experiments, where the polyolefin
burns exhibited a greater rate of flame spread than the nylon carpet burns.
In both cases, the fit has a positive y-intercept, due to the uncertainty
in the data, or to the heat release rate component of the carpet and pad.
The peak
heat release rates for the spill fires are compared to steady state pool
fire heat release rates in tables 7 and 8. The pool fire HRR values were
computed from correlations derived from large-scale pool fire experiments
[8,9]. The diameters used in the pool fire HRR correlations are equivalent
diameters, i.e., the areas of the pool fires are the same as the areas
of the spill fires. Peak heat release rates for the spills examined on
nonporous surfaces are approximately 1/4 to 1/8 of the heat release rates
of the pool fires. For the carpet spill fires, the peak heat release rates
are approximately equal to the steady state heat release rates of the
equivalent diameter pool fires. For the scenarios examined, the pool fire
heat release rates would not be good approximations for gasoline spills
on nonporous surfaces for modeling purposes. The pool fire heat release
rates, however, are good approximations for gasoline spill fire heat release
rates on the carpeted flooring surfaces examined.
The heat
release rates of the fire experiments as a function of time are included
in the graphs in appendix A.
Table
7. Nonporous spill fire and pool fire HRR
|
Spill
Volume, mL (gal.)
|
Peak
HRR (kW)
|
Pool
Fire Steady HRR (kW)
|
|
|
Wood
|
Vinyl
|
Wood
|
Vinyl
|
|
1000
(0.26)
|
770
± 120
|
590
± 160
|
3200
|
3900
|
|
500
(0.13)
|
320
± 80
|
310
± 30
|
1500
|
1800
|
|
250
(0.066)
|
110
± 100**
|
180
± 80
|
700
|
800
|
Table 8. Carpet spill fire and pool fire HRR
|
Spill
Volume, mL (gal.)
|
Peak
HRR (kW)
|
Pool
Fire Steady HRR (kW)
|
|
|
Carpet
1
|
Carpet
2
|
Carpet
1
|
Carpet
2
|
|
1000
(0.26)
|
460
± 30
|
180
± 30
|
470
|
130
|
|
500
(0.13)
|
230
± 20
|
110
± 0
|
230
|
60
|
|
250
(0.066)
|
130
± 10
|
60
± 10
|
100
|
40
|
5.3
Heat Release Rate Per Unit Area
The
heat release rate per unit area (HRR/area) is nearly constant for the
vinyl flooring spill fires studied, and is shown in figure 33. The wood
flooring experiments, however, displayed an increase in the heat release
rate per unit area as the spill size increased. Given the overall behavior
of the HRR/area for the wood floor spills, and the HRR linear curve fit
which has a negative y-intercept, some of the fuel may have been lost
into the cracks of the parquet surface. Given the construction of the
flooring, it would be expected that more fuel would be lost into the parquet
than into the vinyl due to the greater crack length per unit area of the
parquet flooring.
The HRR/area
for the spills on carpet are shown in figure 34. The spills on polyolefin
carpet have a nearly constant HRR/area over the spill size range studied.
For the nylon carpet, a linear fit is not a good representation for the
HRR/area data. As a comparison, the pool fire HRR/area is nearly constant
over the range of equivalent pool fire diameters examined [8]. The resulting
pool fires in this range would be in the turbulent flow regime, where
radiative feedback effects and turbulent flow effects are important. The
reason for the larger HRR/area value resulting from the 500 mL nylon carpet
burns should be studied further.
6.
CONCLUSIONS
Based
on a limited number of experiments, the conclusions of this study can
be summarized by the following:
- The spill
area can be predicted from the fuel quantity. The empirically derived
spill thickness can be used to predict the size of spills.
- In all
but one scenario, the nonporous flooring gasoline burn areas were found
to be the same as the spill areas within the experimental uncertainty.
- Initial
carpet burn areas were found to be the same as the carpet spill areas,
within the experimental uncertainty.
- The quantity
of gasoline spilled could be determined from the burn pattern area on
nonporous flooring.
- Significant
quantities of spilled fuel were present after extinguishment and extinction
of the carpeted fires. The melted carpet inside the doughnut protected
the unburned liquid.
- Peak
heat release rates for the spills examined on nonporous surfaces are
approximately 1/4 to 1/8 of the heat release rates of equivalent diameter
pool fires. For the carpet spill fires, the peak heat release rates
are approximately equal to the steady state heat release rates of the
equivalent diameter pool fires.
- Pool
fire heat release rates may be useful for fire modeling and fire scenario
evaluation for spill fires on carpeted floors. Fire modeling and fire
scenario evaluation for spill fires on nonporous floors should not be
conducted using the heat release rates derived from pool fires.
This
report provides a means for fire investigators to predict the quantity
of spilled gasoline necessary to produce a fire pattern of a particular
size on various types of commonly used flooring materials. It also includes
measurements of spill fire heat release rates that provide fire investigators
and other fire professionals with previously unavailable data for fire
modeling and fire scenario evaluation.
-
P.P.K.
Raj and A.S. Kalelkar, Assessment Models in Support of the Hazard
Assessment Handbook. U.S. Coast Guard Report AD-776 617, U.S. Coast
Guard Headquarters, Washington, DC (1974).
-
J.W.
Murdock, "Mechanics of Fluids." Marks' Standard Handbook
for Mechanical Engineers. Tenth Edition, E.A. Avallone and T. Baumeister
III, eds., McGraw-Hill, New York, NY (1996), pp. 3-31 to 3-33.
-
A.T. Modak, "Ignitability of High-Fire-Point Liquid Spills."
EPRI Report NP-1731, Electric Power Research Institute, Palo Alto,
CA (1981).
-
B.N.
Taylor and C.E. Kuyatt, "Guidelines for Evaluating and Expressing
the Uncertainty of NIST Measurement Results." NIST Technical
Note 1297, 1994 Edition, National Institute of Standards and Technology,
Gaithersburg, MD 20899.
-
V.
Babrauskas, R.L. Lawson, W.D. Walton, and W.H. Twilley, "Upholstered
Furniture Heat Release Rates Measured With a Furniture Calorimeter."
NBSIR 82-2604, National Bureau of Standards, December 1982.
-
D. Drysdale, "Ignition: The Initiation of Flaming Combustion."
An Introduction to Fire Dynamics. John Wiley & Sons Ltd., Reprinted
September 1986, p. 197.
-
A.M.
Kanury, "Ignition of Liquid Fuels." SFPE Handbook of Fire
Protection Engineering, Second Edition, P.J. DiNenno et al. eds.,
Society of Fire Protection Engineers, Boston (1995), pp. 2-163.
-
K.S. Mudan and P.A. Croce, "Fire Hazard Calculations for Large
Open Hydrocarbon Fires." SFPE Handbook of Fire Protection Engineering,
Second Edition, P.J. DiNenno et. al. eds., Society of Fire Protection
Engineers, Boston (1995) pp. 3-199.
-
A.
Tewarson, "Generation of Heat and Chemical Compounds in Fires."
SFPE Handbook of Fire Protection Engineering, Second Edition, P.J.
DiNenno et al. eds., Society of Fire Protection Engineers (1995),
pp. 3-78.
NOTES
1
Numbers in brackets refer to references in section 7.
*
An estimated expanded uncertainty of ± 5.37 x 10-3 m2 (±
5.79 x 10-2 ft2) results from application of the law of propagation of
uncertainty to Type B uncertainties using a coverage factor of 2.
**If
one of the three experiments could be classified as a statistical outlier,
the average peak heat release rate would be 80 kW ± 0 kW. Using
|