Name | HeptanePan2
|
---|---|
Date | |
Description | Small baking pan 7.5" x 5" 1.25" with 300 mL Heptane |
Specimen | Pool Burner
|
Ignition | propane wand
|
Project ID (s) | |
Test Director | Maranghides A
|
Measurement | Value | Uc | Unit |
---|---|---|---|
Peak Heat Release Rate, PHRR
|
59.7
|
3.1
|
kW
|
Time to Peak Heat Release Rate
|
3.33
|
0.17
|
min
|
Total Heat Released, THR
|
9.43
|
0.51
|
MJ
|
Natural Gas Burner Total Heat Released, NGTHR
|
0
|
- | MJ
|
Heat Release Quality Confirmation, HRQC
|
Not measured | - | MJ/MJ
|
Net Specimen Mass (gravimetric), NM = Mi-Mf
|
Not measured | - | kg
|
Total Fuel Mass Burned, TFM = THR / HOCf
|
0.212
|
0.013
|
kg
|
Net Effective Heat of Combustion = THR / NM
|
Not measured | - | MJ/kg
|
O2 Yield = O2 Consumed / TFM
|
3.29
|
0.23
|
kg/kg
|
CO2 Yield = CO2 Generated / TFM
|
3.01
|
0.22
|
kg/kg
|
CO Yield = CO Generated / TFM
|
0.00719
|
0.00052
|
kg/kg
|
Soot Yield = Soot Generated / TFM
|
0.0230
|
0.0037
|
kg/kg
|
Baseline Hood Exhaust Flow
|
1.858
|
0.056
|
kg/s
|
Test Duration = Time(Fire Out) - Time(Ignition)
|
4.43
|
0.03
|
min
|
Uc = Combined Expanded Uncertainty with 95% confidence level
Parameter | Value | Uc | Unit |
---|---|---|---|
Fuel Type
|
Heptane
|
- | - |
Hood Size
|
3
|
- | m
|
Effective Duct Diameter
|
0.483
|
0.004
|
m
|
Exhaust Flow Correction Factor
|
1.033
|
0.029
|
- |
Net Heat of Combustion (per unit mass O2), Ef
|
12.68
|
0.50
|
MJ/kg
|
Net Heat of Combustion(per unit mass fuel), HOCf
|
44.40
|
1.30
|
MJ/kg
|
Initial Specimen Mass, Mi (gravimetric)
|
Not measured | - | kg
|
Final Specimen Mass, Mf (gravimetric)
|
Not measured | - | kg
|
Event | Time (min) | Description | Video Snapshot Image |
---|---|---|---|
1
|
0.00
|
Ignition
|
|
peak
|
3.33
|
Peak HRR
|
|
2
|
4.43
|
Fire Out
|
Bryant, R. and Bundy, M. The NIST 20 MW Calorimetry Measurement System for Large-Fire Research, Technical Note (NIST TN) 2077, 2019
https://doi.org/10.6028/NIST.TN.2077
NIST Fire Calorimetry Database (FCD)
https://doi.org/10.18434/mds2-2314