Fire Resistive Materials: THERMAL PERFORMANCE TESTING Performance Assessment and Optimization of...
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![Page 1: Fire Resistive Materials: THERMAL PERFORMANCE TESTING Performance Assessment and Optimization of Fire Resistive Materials NIST July 14, 2005.](https://reader036.fdocuments.us/reader036/viewer/2022062718/56649ea05503460f94ba2b48/html5/thumbnails/1.jpg)
Fire Resistive Materials: THERMAL PERFORMANCE
TESTING
Performance Assessment and Optimization of Fire Resistive Materials
NIST
July 14, 2005
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MicrostructureExperimental
3-D Tomography2-D optical, SEM
Confocal microscopy
Modeling3-D Reconstruction
ParametersPorosity
Pore SizesContact Areas
Properties(all as a function of T)
ThermalHeat CapacityConductivity
DensityHeats of Reaction
AdhesionPull-off strength
Peel strengthAdhesion energy
Fracture toughness
EquipmentTGA/DSC/STASlug calorimeter
DilatometerBlister apparatus
Materials Science-Based Studies of Fire Resistive Materials
EnvironmentalInterior
Temperature, RH, load
ExteriorTemperature, RH, UV, load
Performance PredictionLab scale testingASTM E119 Test
Real structures (WTC)
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Importance of Thermal Properties
• The major role of the FRM is to slow down the temperature rise of the structural steel during a fire exposure
• Its effectiveness will be largely determined by its thermal properties
• While heat capacity, density, and heats of reaction and phase changes do play a role, it is mainly the effective thermal conductivity of the material as a function of temperature that will dominate the performance
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Fourier’s Law of Heat Conduction
q=-kA(∂T/∂x)• Heat transfer is proportional to temperature
gradient, exposed area, and thermal conductivity k
• k and thickness (x) are the variables “under our control”
• k is really an effective thermal conductivity as it includes contributions of conduction, radiation, and convection
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But, what about endothermic reactions?
• Endothermic reactions and phase changes (evaporation) do absorb energy, but a couple of additional points merit consideration– 1) Energy absorption will maintain a higher temperature
gradient across the FRM specimen which will in turn increase the driving force for heat transfer (∂T/∂x) --- as noted to me by Prof. Fred Mowrer of Univ. of MD.
– 2) Steam and hot gases generated during these reactions may be transferred inward towards the steel surface, actually temporarily but significantly increasing the effective thermal conductivity
– 3) If the material has a low permeability, these reactions may result in (explosive) spalling (Example- high performance concrete)
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A brief aside on “liquid” water in FRMs
• Thermal conductivity of liquid water is about 0.6 W/m•K; air or water vapor is about 0.03 W/m•K (a factor of 20)
• Materials with “liquid” water also have a higher propensity for spalling, etc.
• Make sure that your materials are really dry before E119 (or other) testing
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Thermal Conductivity at High Temperatures
• How to measure it?– ASTM C1113: Hot wire method– High-temperature guarded hot plate (world-
class facility under construction in BFRL)– Transient plane source method (Hot Disk®-
will be delivered to BFRL in August 2005)– Slug calorimeter (built at BFRL in 2004 and
used extensively since then)• Similar in principle to the Cenco-Fitch Apparatus
used in ASTM D2214 for estimating the thermal conductivity of leather (first published by Fitch in 1935)
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Hot Disk® System
• Manufactured in Sweden• Measures k in range of
0.005 to 500 W/m•K• With high temperature
attachments, temperature range of room temperature to 700 oC
• Also provides volumetric heat capacity values
• http://www.hotdisk.se
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Slug Calorimeter Technique• Sandwich specimen of two “slabs” of FRM
covering two sides of a steel slug of known mass and heat capacity
• Monitor slug temperature change as entire sandwich is exposed to a heating/cooling cycle
• Calculate effective thermal conductivity during multiple heating/cooling cycles
• For detailed information see: Bentz, D.P., Flynn, D.R., Kim, J.H., and Zarr, R.R., “A Slug Calorimeter for Evaluating the Thermal Performance of Fire Resistive Materials,” accepted by Fire and Materials, 2005, available at http://ciks.cbt.nist.gov/garbocz/slugpaper1 .
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Slug calorim
eter
Specim
en
Specim
en
Guardinsulation
Guardinsulation
Q directionheating
cooling
Retainingplate
6 “3/16” inch holes at 2”, 3”, and 4”
½”
2”
4”
6”
Slug Calorimeter
Experimentalsetup
Details of slug calorimeter
304 stainless steel
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Raw Data for Exposure of Intumescents
0
150
300
450
600
750
900
0 60 120 180 240 300 360
Time (min)
Tem
per
atu
re (
C)
Furnace - Int. A Furnace - Int. B
Slug - Int. A Slug - Int. B
Time for central slug to reach 538 oC varied from 52 minutes to 93 minutes for the two different materials
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Determination of Effective k∂2T/ ∂z2=(1/α)(∂T/∂t)
With B.C.: T(0,t)=Ft, k(∂T/∂z) +H(∂T/∂t)=0α is the thermal diffusivity
H is the thermal capacity of one half of the slug plateF is the rate of temperature increase/decrease of the slug
Solution: T(z,t)=F[t-(H+lC)z/k+Cz2/(2k)]l is the specimen thickness, C its volumetric heat capacity
ΔT = (Fl/k)*[H+lC/2]ΔT is the temperature difference across the specimen
k=Fl(H+lC/2)/ΔT=Fl(MScpS+MFRMcpFRM)/2AΔT
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Slug Calorimeter Results: Fumed Silica Board
-Results for (non-reactive) fumed silica board in good agreement with previous NIST (1988) measurements
0.00
0.01
0.02
0.03
0.04
0.05
0 50 100 150 200 250 300 350 400 450 500 550
Mean Specimen Temperature (oC)
k [W
/(m
•K)]
NIST data heating (1)
cooling (1) heating (2)
cooling (2) heating (3)
cooling (3)
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Slug Calorimeter Results: FRM A
-Good agreement with previously measured values-Differences between 1st and 2nd heating cycle provide valuable information on influences of endothermic and exothermic events, including reactions and phase changes- Good repeatability in cooling curves for different runs
0.0
0.1
0.2
0.3
0.4
0 100 200 300 400 500 600 700 800
Mean Specimen Temperature (OC)
k [
W/(
m•K
)]
heating (1) cooling (1)
heating (2) cooling (2)
heating (5-16h) cooling (5)
hot wire TPS
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Slug Calorimeter Results: FRM C
-Reasonable agreement with previously measured values-Differences between 1st and 2nd heating cycle provide valuable information on influences of endothermic and exothermic events - Good repeatability in cooling curves for 3 different runs
0.0
0.1
0.2
0.3
0.4
0 100 200 300 400 500 600 700 800
Mean Specimen Temperature (oC)
k [W
/(m
•K)]
hot wire method TPS methodheating (1) cooling (1)heating (2) cooling (2)heating (3) cooling (3)
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Slug Calorimeter Results: Comparison
0.0
0.1
0.2
0.3
0.4
0.5
0 150 300 450 600 750
Mean Specimen Temperature (oC)
k [W
/(m
•K)]
- High variability between different FRMs especially at higher T- High T insulation boards (two lower curves) have effective k
values significantly lower than current FRMs and exhibit minimal increases at higher temperatures
k from 2nd heating curves
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Comparison of Time for Steel Slug to Reach 538 oC
40
50
60
70
80
90
100
110
120
A B C D E F G H I J K L M N O P
"Fai
lure
" ti
me
(min
)
1st heating
2nd heating
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Determination of Heat Capacity• Volumetric heat capacity provided
directly with Hot Disk® thermal conductivity measurements
• For small specimens, can measure using differential scanning calorimetry (DSC) or simultaneous thermal analysis (DSC/STA)– Both units available in BFRL at NIST– Equipment for larger sample volumes (12
mL) and temperatures up to 1000 oC is available from Setaram ($$$)
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Heat Capacity via DSC (ASTM E1269)
0.4
0.8
1.2
1.6
2
2.4
2.8
3.2
3.6
4
4.4
0 100 200 300 400 500 600 700
Temperature (oC)
Hea
t Cap
aci
ty (
J/g
•K)
.Sapphire reference
Sapphire calculated
FRM (no mass corr.)
FRM (mass corr.)
Need to run a sapphire reference scan and applicationof a correction (fudge) factor
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Summary• Thermal conductivity at high temperatures
is a critical performance parameter for FRMs to properly protect structural steel
• BFRL/NIST labs are uniquely equipped for measuring this property and are continually upgrading our capabilities
• Measurement of effective thermal conductivity provides product differentiation that can be utilized both to improve existing materials and to develop new ones