Reference NES
cations
- atinor—resene [Whi IMU |
NBSIR 80-2054 105 131204
The Burning of Wood and Plastic
Cribs in an Enclosure:
Volume l!
James G. Quintiere, Bernard J. McCaffrey and Margaret Harkieroad
Center for Fire Research
National Engineering Laboratory
Nationai 8ureau of Standarcs
U.S. Department of Commerce
Nashington, OC 20234
November 1980
Final Renort
Products Research Committee
Grant No. RP-76-U-2: Assessing the Hazard of Ceijuiar Plastic Fires in a Room
senna ase =
Seo os
Re tcteartet el =
alienal Bureau ef Standards
Library, €-01 Admin, Bidg.
FEB 2> 199;
NBSIR 80-2054 ie
THE BURNING OF WOOD AND PLASTIC we
CRIBS IN AN ENCLOSURE: 7
VOLUME II . .
James G. Quintiere, Bernard J. McCaffrey and Margaret Harkieroad
Center for Fire Research
National Engineering Laboratory
National Bureau of Standards
U.S. Department of Commerce
Washington, OC 20234
November 1980
Final Report
Prepared for
Products Research Committee
Grant No. RP-76-U-2: Assessing the Hazard of Cellular Plastic Fires in a Room
U.S. DEPARTMENT OF COMMERCE, Philip M. Klutznick, Secretary
Jordan J. Baruch, Assistant Secretary for Productivity, Technology, and /nnovation
NATIONAL BUREAU OF STANDARDS, Ernest Ambier, Director
| i ——t—“‘( Ql 4
Page
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i i ee fs id Ss gos es =e &¢ ewe ee see eee cs eo oe st Ie
6. ROOM AND DOORWAY GAS TEMPERATURE PROFILES (T) ....++-++++22e 93
7a nn Terese Meee AW) «+s we ec eee ete em ee ew ew we ew ew CA
Ss BO Se FLOR RATE . «2 ee 8 8 8 8 ew 0 © piimirenn Cece at ie el we ABS
S. WOGM GTATIC PRESSURE. «.. 0 100 tarye 16 tne im eye ’e pies er eres «0 alle fe er kG
Ln Ga CEEMEEGRE fo 6 6 we eee eee we ew ee wee eee ee en eo JT
1h MA REFERENCES * * * * * * * * . te bel . * . . . * . . * . . . . . . . . . 218
APPENDIX A - EXERCISE IN AVERAGING... 2.22 ese e ee eee see 2 « 2g
APPENDIX 8 - TRANSIENT DATA
APPENDIX C - AVERAGE PEAK VALUES
10-1.
A-10.
A-11.
LIST OF FIGURES
Room instrumentation --thermocouple section (fig. 2-5,
MO a) erin Fos ou oo shag otek to ae tory aah rete Robt site tinel BYe4 tan Yai ah cs
Room instrumentation --side view (fig. 2-4, Col. I) . .
Through 2-20. Room temperatures as a function of time.
Through 3-20. Doorway temperatures as a function of
EMG cw ie er Hor we. Mel lRart War BamMar Soul mogMan Rem ct Mone cute: Mian ep Ton Na Too Ne: tar
Through 4-20. Crib mass loss as a function of time .
Through 5-20. Crib mass loss rate as a function of
(TINS y Aceh ts) Kowlic peptic eeroemaceMersts Mensa No rey rc oum aso ith or atient bereniats ett ts
Through 6-20. Room and doorway gas temperature profiles
for times at 30 seconds following ignition, the start of
the average peak burning time, its midpoint, and its end.
Through 7-39. Doorway velocity profiles at 35-second
intervals up to 60 ssecondls) Mitts ha he Was oh, Nat Oe tee en cer ae
Through 8-20. Doorway mass flow rates in and out as a
BUNCE VON: Oss EAS caesar law aN c ie eaav | Ne Byenl Gil “etive) nel ceycey ce
Through 9-20. Room pressure differentials at elevations
corresponding to the probe position designated by
Ehanned, Numbers’: os) (emt e sesh beipnsnc re oh its.4) eae Geer apm as
Through 10-20. Volumetric concentrations of 0, and CO,
(on a dry gas sample basis) measured at the top of the
doorway, als sae runcervon Of (Eames wee vel ios eure) dath edd nsio e's
Through A-6. Recorded differential pressure signals
for PRC-1-P-l1 at the sensor locations corresponding
tonchannelis 4 ehrougihy iow) mle ave rs iirel glen shell tes nertvec te
Time-averaged pressure (PRC 1-P-1), 50s interval,
rectangiuilarey aie gina vOM is ela) vet ats hem esteem eel iet cel cu sie) sess ne
Time-averaged pressure (PRC 1-P-1), 25s interval,
rape ZO watery Vee et sobre) veneer aren isl rela ey a) sen iotina vel eh seuss
Time-averaged pressure (PRC 1-P-1), 50s interval,
Era pezo cataileeaier Bish (sie creas aiepins cris, lou Malice: Wise Miele cles. fo) Sven\ae ls ers
Time-averaged pressure (PRC 1-P-1), 75s interval,
PSAP SE ZOG Vale eI Ceo vega te eer cops Meet Kap Tol ea) ert ae wher Miedite Maen cot uss
Time-averaged pressure (PRC 1-P-1), 100s interval,
Sap eS Zostera espe ited (ost sh) renyproniheMue eens May teuiWerc vet ten vial vei
iv
Page
94-113
iby Wey)
1657 5
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220-225
226
228
229
230
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Table
Table
Table
Table
1.
2.
3.
4.
LIST OF TABLES
Sequence of room fire experiments .....
Type of instrumentation ......+.-+.«.-
Comppelation key for raw data. . «. « « « « »
Average peak values for significant results
THE BURNING OF WOOD AND PLASTIC CRIBS IN AN ENCLOSURE:
VOLUME II
James G. Quintiere, Bernard J. McCaffrey and Margaret Harkleroad
1. INTRODUCTION
This is a summary and compilation of the room fire data referenced in
"The Burning of Wood and Plastic Cribs in an Enclosure: Volume I". A
complete set of the transient raw data in the format given in table 1 is
available on a 9-track, 1600 BPI, 132 character record, ASCII format
magnetic tape. A printed listing of the data is tabulated in appendix B.
Section 2.3 of volume I (1)? gives a detailed description of the
instrumentation. Here we include table 2 which describes the type of
instrumentation and table 3 which indicates the symbol and letter key use
to designate the sensor. Accordingly, the sensor locations are shown in
figures l-l and 1-2.
Typical of room fire experiments, an immoderate amount of data ~as
collected. For the most part, we have chosen to examine the quasi-steady
results during the peak burning period. These results have been thoroughly
discussed in volume I [1], and are presented here again in table 4 for
convenience. Since the general transient aspects of the experiments may
be of interest, these results are presented in the following sections. The
order of presentation for each parameter will follow the sequence given in
table 4; however, the first experiment (PRC 0) was not included.
I ;
Numbers in brackets refer to the literature references listed at the end
of this report.
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2. ROOM TEMPERATURES
Room temperatures measured as described in volume I [l], section 2.3.1
are shown as a function of time in figures 2.1 to 2.20. The curves are
labeled according to thermocouple number, as referenced in figure 1.1.
These results include the ceiling (TS) and wall (T25) temperatures, but
do not include the filter paper temperature (T24).
Some anomalous behavior of the data is present and may be explained.
Por example, the ceiling temperature generally follows the wall temperature,
but this is not the case in PRC 3. It appears that in that case TS was more
likely measuring the gas temperature near the ceiling. The temperature
fluctuations generally reflect the turbulence level but in some instances
extraordinary excursions are shown. These excursions do not reflect the
temperature; the cause of the error is not known. In PRC 9 and 10 it appears
that T23 was not recording the proper temperature, in fact T23 was found to
have had a short circuit at the thermocouple junction box located in the room.
Hence, it was probably measuring the temperature in the junction box for
these two experiments. Finally, during the fire decay period T28, the
aspirated thermocouple appears to have an anomolous behavior. [It occurs
for the high temperature fires with small doorways. The aspirated temperature
begins to exceed the bare thermocouple data: This is probably a valid
reading due to conduction from the hot aspirated probe metal tube which is
slow to cool. When this occurs T28 does not give a true gas temperature
reading.
PRC3-W-1-1
TEMPERATURE
ROOM
TEMPERATURE (C) :
1S9Q 209 252 302 352 UGB
12
52
POR Sp OL OIA Pa On
2 152 300 USQ
622 752
ia ee SiGe)
992
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4uS@ $00 75 900
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TEMPERATURE (C)
152 200 250 30 350 uaa
122
52
399
PRC2-W-3-1
TEMPERATURE
ROOM
759
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TEMPERATURE (C)
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1S@
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PRC7-W-4-1
TEMPERATURE
ROOM
Cr Asics zt
750
usa 500
Time <SEC)
13
320
PRCA =P =1 =
TEMPERATURE
ROOM
TEMPERATURE (C)
159 200 250 300 350 ry)
102
5
Q 152 302 750 989
US@ 622
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TEMPERATURE
PRCY-P-2
ROOM
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TIME (SEC)
3280
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622
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200
122
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TIME A SEG
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i
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4. CRIB MASS LOSS
The crib(s) mass monitored as described in volume 1 [1]. Section |
2.3.4 is shown as a function of time in figures 4-1 to 4-20. The wood
cribs would generally collapse at about 10 minutes after ignition whereas
the plastic cribs would swell and char but maintain a structure similar
to its original form. The char residue: after combustion was about 10 percent
for the wood and 13 percent for the plastic.
In form experiments, PRC 15 through 18, a malfunction of the load
platform was discovered. This was corrected and an attempt was made to
correct the errors in the mass loss data through a special calibration
procedure. These corrected results are shown here.
An anomaly occurred in PRC 2 which was a mass increase near the end
of the experiment. This coincided with the crib collapse. However, the
cause of this erroneous mass increase was not clear. Another obvious
error occurs as a brief excursion in PRC 18. This is likely a data
recording problem.
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The instantaneous rate of mass loss was obtained from the crib mass
data. In the interpretation of these results it should be realized that
they arise from a differentiation process applied to discrete data points
which may not be well-behaved in a mathematical sense due to experimental
fluctuations. The "smoothing" method selected was a least square linear
fit over successive mass loss data points. The slope of the linear fit
is the mass loss rate. This process was repeated for a running set of
ten data points for each five-second increment. The formula is given as
10 LO eo
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where t; is the time
and m5 is the mass.
The results cf these calculations are given in figures 5-1 through
5-20. Anomalous behavior can be traced back to problems with the mass
loss data or to the manner in which the differentiation method is responding
to the data fluctuations.
A comparison between repeat runs (PRC 17 with PRC 19, and PRC 20
with PRC 16) shows that the results are in fair agreement. (Note that the
ordinate scale varies in each of these figures.)
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A sequence of room and doorway temperature profiles is shown in
figures 6-1 to 6-20. In each figure the time sequence of profiles is
shown for 30 seconds after ignition, the start of the average peak burning
period, its midpoint, and its end. The plotted curves connect the data
points, which have not been shown explicitly. The distinguishing features
of the profiles are their shape and magnitude during the peak burning period.
The depth of the heated gases within the room is much lower for the smaller
doorway cases and stratification is stronger there. The "Star" data point
in tests PRC 9 through PRC 20 indicates the true gas temperature measured by
the aspirated probe at that point. A significant result is that the maximum
doorway temperature is lower in each case than the maximum temperature in
the room. This is probably due to heat loss from the gases flowing between
the two measuring stations. Thus a unique upper and lower room gas
temperature is an idealization. Yet this concept is useful in analyzing
room fire data and in predicting fire behavior from zone models. However,
there will always be some inconsistency between measured room temperatures
and those temperatures predicted by zone models.
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7. DOORWAY VELOCITY PROFILES (V)
Doorway velocity profiles over a 560-second period are shown in figures
7-1 to 7-20. Each figure contains 16 profiles with each produced at 35-
second intervals, the end of each complete velocity scan of the vertical
probe a ray in the doorway.
After an initial transient period the profiles reach a nearly steady
state and are relatively insensitive to fire changes up to burnout. In
general for a fixed room temperature level, the profiles indicate increasing
velocities and a decreasing zero velocity position (neutral plane height)
as the doorway width is decreased.
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8. DOORWAY MASS FLOW RATE
The mass flow rate of combustion products out of the room and airflow
into the room was calculated from the velocity and density (temperature)
measurements at the centerline of the doorway. The equation is
th = Mo | T, (V/T) dy
where the velocity and temperature was assumed invariant over the doorway
width. The perfect gas state equation for air was used where a a are
reference values of density and temperature. The integral was taken over
the bottom (or top) of the doorway to the neutral plane and the integral
Was evaluated by a trapezodial formula. ed anette of the neutral plane
was found by linear extrapolation of the velocity data at the flow reversal
point in the doorway. t should be realized that our data acquisition
limitations led to a complete vertical velocity traverse every 35 seconds.
Hence, the integral was evaluated every 35 seconds. Because of the inherent
fluctuation of the velocity due to turbulence, and the transient changes
due to fire growth and decay, a “smoothing” process was applied to this
Calculation. For all experiments the data results presented represent a
running three-point average of the mass flow rate over 35-second intervals.
The average was assigned to the mid-point. Also, for each run following
PRC 8, the pressure signal from each transducer was electronically averaged,
and this result was recorded every 35 seconds. The results of these
calculations are shown in figures 8-1 through 8-20. The results appear
much smoother following PRC 8 due to this electronic signal averaging
process. The lack of mass balance in the results is a serious problem
which could have been remedied by more comprehensive measurements.
435
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OW RATE
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9. ROOM STATIC PRESSURE
In this section the pressure differentials between the inside and
outside of the room are presented at six elevations. The results are
presented as a function of time in figures 9-1 through 9-20. The elevation
can be identified by the channel number listed in the figure, and the
information listed below (see also figure 1-2).
Channel Probe Distance Above the Floor (m)
Number Symbol PRC 0-8 PRC 9-20
41 DP1l 2310 aimee
42 DP2 72 Mal ib Arial
43 DP3 she HH Wy SIE
44 DP4 0.54 0.89
45 DP5 0.285 0.49
46 DP6 0.0285 0.04
The probe positions were changed after PRC 8 in order to yield a more
complete vertical distribution.
Since these probes responded to a turbulent phenomenon it is
appropriate to average their signal in order to present the near pressure
differential. The main result will depend on the averaging process used,
and in appendix A various averaging results are presented for illustration.
The results given in figures 9-1 through 9-20 have been time-averaged as
t.
pene Ge) A ueCke
1
B (t, ) = = }
tome (eaigeee
#2.
aL,
a 50-second running average using a rectangular rule for evaluating the
integral with a time increment equal to the data scan time of 5 seconds.
In the above formula, p is the pressure signal, and t, is the time at the
ith data scan.
176
PRC3-W-1-1
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u
2
-2
322
4S2
TIME
195
PRC16-P-3-1/74
STATIC PRESSURE SENSORS
LEFT REAR WALL
* CHANNEL
@ CHANNEL
€ CHANNEL
@ CHANNEL
4 CHANNEL
@ CHANNEL
732
U1
42
U3
uy
us
UG
PRC20-P-3-1/4
STATIC PRESSURE SENSORS
LEFT REAR WALL
* CHANNEL 41
#CHANNEL U2
@CHANNEL 43
@CHANNEL 4Yy
4 CHANNEL 4S
¢CHANNEL 46
2
N/M2)
8 12
URE (
6
SUBIC. Pines
p) 159 309 uSQ 620 759
Ps CS) S
196
10. GAS CONCENTRATION
The volume concentrations (dry basis) of 0, and co. measured at the
top of the doorway are shown in figures 10-1 to 10-2. These concentration
results are mirror-like images of each other provided a significant concen-
tration of CO is not produced which was certainly the case in our experiments.
In fact it can be shown from equations 6-30 through 6-32 of volume I that
(for insignificant fuel production)
"ed. YQ
x + ——— x = 0.21
02 Mo> CO, co,
where x is the volume concentration,
M is the molecular weight,
and v is the stoichiometric coefficient,
for the co, and o5 species respectively.
24 28 32
20
PERCENT GAS
12
1S2@
3289
PRCS-W-i-1
=
USO 609 75
(une CSG)
121%)
02
cee
02
CQ2
739
PRCS-W-2-1
620
(SEC)
392 uso
TIME
1S@
Ze 82 hz 2 QI
st, SUD LNSA9044d
199
PERCENT GAS
32
28
24
20
16
2
152
329
PRC2-W-3-1
USO 622 75
TIVES (SEey
992
02
C02
02
C02
922
PRC7-W-4-1
500 750
(SEG ]
159 300 4US@
TIME
ce 8e he et 8 h a)
G2 9I
| SUD LNAONAd
If
201
PROI-F 1-1
22 2u 28 32
PERCENT GAS
Q 152 329 USQ 620 75Q 329
THE CSE)
202
—sr se |
ra]
Q
D
Wi
ro)
“ 3 oF re
rat)
'
oO
1
FA —“~
2
x ()
(9
\
| ip =
a je |
b-
H 2
} i.)
”
ra]
_Ww
2
| ce 82 he St 8 h Q
2 31
eS SUS LN39YSd
j
ee a hlelhlelhlel ll
203
PERCENT GAS
32
28
ay
22
16
1S
399
ee ae 5 ee ee ee ae ee Oe ow .
PROG--S—3
USQ 629 752
TES CSE?
204
121%)
902
739
PRC8-P-U-1
3282
——— ee o~—-
et 8 h Ve)
Ze 82 he ez 91
SU9S LN30A4d
*”
205
16 20 24 28 ae
PERCENT GAS
12
152
389
PRC9-W-2-1/2
USO 620 752
hits (See.
02
C02
8929
~ ee eee
eC -
PRC11-W-3-1/72
—
ce
——*
—
c02
999
02
4US@ 620 75
bt ig | Aa) Oe,
322
1S2@
Be he et 8 h ®
e2 31
SUD LNS39DY4sd
. ~ a i) i
207
16 22 2yu 28 32
PERCENT GAS
12
152
398
PRC1S-W-4-1/2
02
C02
USQ 622 75Q 929
TESS CSaey
208
ee me
9Q2
02
732
PRC19-P-2-1/2
322
152
o2 31 et )
SUD LNSA90d44d ;
—< <= i<tmU,.i«“£nmnmmnoi—@m@ nmoioweminm@imerttprPpmhehHeheH CUM
ze 82 he
20 eu 28 32
PERCENT GAS
152
309
PRC18-P-3-1/2
02
c02
USQ 620 750
Pines (See)
210
~~ et ~
120)
02
C02
Q
g
Le)
{
: +
hy
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e bt
—
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ott!
p=
phot
=
1
g
‘ g
y Mm
i
\
, 2
1 _W
—_
gS
ce 82 he et 8 h e
2 91
SUD LN39N3d
‘
ret
™N
a ee
PERCENT GHs
16 22 2u 28 32
12
8
309
US@
Wun
212
PRC17-W-4-1/74
620 759
(SEC)
02
cO2
929
02
C02
7S@ 302
PRC19-W-4-1/74
>
3820
1S@
ce 82 he et 8 fh 0
2 31
SUS LNSA9N4d
-—_——s - -
16 20 2u 28 32
PERCENT GAS
12
152
392
See OO We
USO
Mins
214
PRC12-P-1-1/4
620 750
CSEGa
929
02
c02
02
C02
93229
7S
PRC14-P-2-1/4
329
—— ~~ ee ee. =
ce 8e he et 8 h a)
2 91
SUD LNS39Y3d
215
i : ~
16 20 2y 28 32
PERCENT GAS
12
- Te et nee
309 US@
Ae
216
PRCI6-P-3-1/4
02
C02
620
Cae?
929
Nee @.
~s- +> =
PRC2Q@-P-3-1/4
982
02
C02
320
ce 8e he et 8 h e
oz 31
SUD LN3ADY4d
217
ll. REFERENCES
[1] Quintiere, J. G. and McCaffrey, B. J., The Burning of Wood and Plastic
Cribs in an Enclosure, Volume I.
218
APPENDIX A
EXERCISE IN AVERAGING
Analysis of fire data often requires some type of time averaging. As an
illustration the static pressure data from PRC-l1-P-l were averaged by several
methods and these results are given here. Figures A-l through A-6 show the
raw data as recorded every 5 seconds. These are continuous plots through
these discrete data points. Figures A-7 through A-ll display continuous plots
of various running average operations applied to the raw data. The general
averaging formula is given as
cy + Ndt
> (e, +m at)= o p(t) dt
Ps
where At = 5 seconds, and the integral is evaluated by a quadrature rule for
the discrete data p(t) over the interval Ndt. In figure A-7, N = m = 10 and
the integral is evaluated by a rectangular rule. In figures A-8 through A-11,
N is 5, 10, 15 and 20 respectively, and the integral is evaluated by the
trapezodial rule. In each of these cases m was selected such that p was
evaluated each time at the center of the interval Nic.
219
PRCLrP-1-1
STATIC PRESSURE SENSORS
LEFT REAR WALL
CHU 1
6 8 18 ie
TY
STATIC PRESOURE (N72)
g 152 322
USQ 609 759
, ie AGS.)
Figure A-1
220
992
PRC1-P-1-1
STATIC PRESSURE SENSuRS
LEFT REAR WALL
CHU2
vi
--
CU
=o
“te
_.
uJ
© oo |
_
no |
¥ I |
&
os Wi Uli
© |
> —_—
—
3
—
my
2) 152 392 7S9 922
4S9 629
TIME (3S)
Figure A-2
221
RE (N/M2)
6 8 12 12
y
2
STATIC PRESSU
PRO1 <P 1.1
STATIC PRESSURE SENSSKS
LEFT REAR WALL
CH43
459 692 758 909
TIME tC Se
Figure A-3
222
STATIC PRESSURE (N/M2)
-2 2 4 6 8 1 12
iS@
322
uS@ 629
TIME (S)
Figure A-4
223
PRE} -P=1=1
STATIC PRESSURE SENSoRS
LEFT REAR WALL
CHYUY
732 922
uy 6 8 12 12
STATIC PRESSURE (N/Me2)
2
PRC1<-P=-1-1
STATIC PRESSURE SENSORS
LEFT REAR WALL
CH4US
329 USQ 622 752 9e9
Ties 4Gse
Figure A-5
224
7$2 9392
LEFT REAR WALL
STATIC PRESSURE SENSORS
CHUG
PRC1-P-1-1
r
|
5289
1
WH |
4uSO
TIME (S)
a
——aEa
———
——
————
—_—<__—— ee
ee
a =e
—eeee
pa
~~
as ——
aoe
ES S
Se cS)
—eeee = ~”
————
—_—_—- — ee
——w re
(0
— Sos
———————— EL aol
SS Pe
159
zt Or 8 9 h 2
(CW/N) SJYNSSAYd IJILULS
Figure A-6
225
PRC1-P-1-1
STATIC PRESSURE SENCCRS
LEFT REAR WALL
# CHANNEL
# CHANNEL
& CHANNEL
@ CHANNEL
4 CHANNEL
¢ CHANNEL
6 8 18 12
rT
STATIC PRESSURE (N/Me2)
Q 152 329 USO 629 752
TEENIE “GSe
Figure A-7
226
41
42
43
att
4S
46
PRC1-P-1-1
STATIC PRESSURE SENSORS
LEFT REAR WALL
* CHANNEL 41
@ CHANNEL 42
yy @ CHANNEL 43
nfs @ CHANNEL 44
ACHANNEL US
¢CHANNEL 4S
=
‘aul
=o
ae
>
Lu
wo
>
79)
Fp)
Lu
&
—
2)
ae
—
a
-_—
me
-2
<—s .
ae
——— eb
-&
ae
2 159 302 uS@ $00 750 922
TIME (S$)
Figure A-8
227
PRC1-P-1-1
STATIC PRESSURE SENSORS
LEFT REAR WALL
* CHANNEL 41
@CHANNEL 42
BH CHANNEL 43
@CHANNEL 44
4 CHANNEL 4S
CHANNEL 46
Res CN 72)
4 6 8 12 12
STATIC PRESSU
2
Q 159 329 USQ 62g 75 922
TIME “esa
Figure A-9
228
STATIC PRESSURE (N/M2)
PROT <P =1=1
STATIC PRESSURE SENSSDRS
LEFT REAR WALL
* CHANNEL 41
@CHANNEL Ye
wu BCHANNEL 43
aes @CHANNEL 44
ACHANNEL 4S
¢CHANNEL 4S
g
@
©
— y
MN
yp bin
ican FP me
fat}
|
|
|
|
"
9 159 309 use 75Q 300
520
TIME (3S)
Figure A-10
229
ttt
PRC1-P-1-1
STATIC PRESSURE SENSORS
LEFT REAR WALL
* CHANNEL 41
#CHANNEL 42
# CHANNEL 43
@CHANNEL 44
ACHANNEL 45
¢ CHANNEL 46
6 8 12. 12
y
STAT Peer ooURe UN? ie)
Q 150 300 us@ 590
TIME (S$) = =
Figure A-1ll
230
NBSIR 80-2054
The Burning of Wood and Plastic Cribs in an Enclosure: Volume II
Appendices B and C
James G. Quintiere, Bernard J. McCaffrey and Margaret Harkleroad
Center for Fire Research
National Engineering Laboratory
National Bureau of Standards
Washington, D.C. 20234
November 1980
Products Research Committee
Grant No. RP-76-U-2: Assessing the Hazard of Cellular Plastic
‘| Fires in a Room
i Prepared for the \
APPENDIX B
Transient Data
A complete set of the record data over time is tabulated in this section.
It is categorized by test code designation in the order given in table 1. The
data are labeled by channel number and time in seconds. The correspondence
from channel numbers to sensor designation and the units of the measurements
can be obtained from table 3.
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PRC 13-W-2-174 ; PAGE 5
TIME 14 15 16 17 18 19 - 20 al 22 23 24 25 26 27
8. 25.52 25.56 25.30 24.90 25.78 25.22 24.408 24.05 24.45 25.67 25.42 25.92 23.98 23.37
8. 25.67 25.38 25.17 24.85 25.68 25.17 24.25 24.87 24.57 25.65 25.47 23.82 23.75 23.40
6. 25.68 25.32 25.17 24.80 25.50 25.13 24.26 24.85 24.63 25.67 25.45 23.72 23.67 (eH
a. 25.45 25.38 25.07 24.82 25.57 25.18 24.15 23.97 24.45 25.79 25.47 24.15 23.85 23.42
8. 25.35 25.26 24.95 24.95 29,22 25.22 24.22 23.97 24.15 25.82 25.47 23.92 23.47 23.45
8. 25.20 25.13 25.62 25.08 25.10 25.208 24.22 23.98 24.00 25.75 25.47 23.85 23.63 23.45
3. 25.85 25.85 25.75 25.70 25.35 25.r2 a5 24540 24.42 24.42 26.40 26.70 24.13 23.87 25u5
10. 29.83 29.75 Cui bed. tae 26.85 26.79 24.67 24.42 24.65 26.65 2?.10 24.15 24.15 25.55
15. 31.29 31.44 . 30.46 29.62 PLE 25.57 24.05 24.2% 25.00 26.78 27.49 24.42 24.352 23.45
20. 34.38 32.88 31.19 29.70 26.82 25.68 24.60 24.2 34. et) 26.85 27.63 °2.4.05 24.18 23,08) |
25. 37.39 35.76 34.68 30.80 26.65 25.58 25.28 24.49 24.52 26.92 23.15 24.49 23.98 23.50
30. 37.37 37.73 36.54 38.00 26.75 26.88 25.67 24.68 24.25 27.05 28.47 24.59 23.65 23.57
35. 38.17 37.93 36.62 31.61 29.76 23.25 2d.20 24.75 24.50 2a 28.82 24.15 24.13 23.5¢
40. 39.85 38.80 38.37 34.58 30.10 29.00 25.82 24.63 24.55 27.30 29.00 23.97 24.50 23.63
45. 46.93 39.17 38.90 3329 38.6! 23.35 25.72 24.86 24.65: 27.48 29.508 24.42 24.45 23.62
38. 45.12 43.85 42.15 36.34 32.83 28.82 25.82 24.62 24.55 27.60 29.46 er 24.26 23.02
95. 47.58 47.61 46.07 39.49 31.07 23.595 29595 24.92 24.07 27.€0 29.37 24.82 24.35 2Stans
60. 51.46 48.51 4? .37 42.44 32.108 29.38 26.55 24.95 2556 oto 30.73 24.88 24.70 23.87
65. 56.10 54.58 51.41 46.17 34.66 30.00 27.05 25.28 25.30 28.35 31.61 24.67 24.42 23.82
70. 56.85 57.17 95.54 49.93 Rha) oP 30.43 27.50 25.82 25.22 28.77 $5.59 24.98 24.65 25.62
7s. 61.86 99.57 59.52 54.80 39.15 32.29 29.82 27.80 25.42 29.50 35.10 25.27 25.20 CRT
80. 74.90 67.12 61.88 93.93 41.33 3.66 28.90 26.95 25.70 29.78 36.66 25.50 25.42 24.008
85. 82.59 79.63 73.908 51.76 42.71 36.09 25.97 Zee 26.32 31.02 39.00 9.65 25.70 24.13
90. 95.24 89.59 81.90 55.37 413.93 33.22 29.98 27.20 26.45 32.71 42.17 26.20 25.85 24.3
95. 116.85 101.51 86.45 Sto 43.63 49.93 3iese2 28.05 Cane 53,05 44.63 26.63 26.30 24.60
100. 117.88 110.22 102.60 72.05 50.83 41.34 31.41 tere 27.¢5 36.15 wa0ee 27.30 26.65 24.85
105. 144.12 135.20 108.98 82.12 53.69 44.38 32.85 26.32 28.60 38.80 56.05 27 .c 28.02 25.15
110. 163.35 143.82 138.92 89.62 55.44 49.41 34.80 29,50 29.i0 42.49 60.19 2f vas 27.57 25.23
115. 195.47 176.20 162.20 112.88 53.99 ep 35.61 20.83 30.15 47.32 74.83 29.2 29.82 29.009
120. 197.67 193.13 161.35 113.46 70.98 55.76 39.441 SLez 31.10 51.80 61.69 29.708 29.41 26.02
125. 229.37 224.02 204.58 139.77 63.89 59.93 40.85 32.66 32.15 58.63 87.43 rps Nhe 38.68 26.57
130. 235.34 218.55 191.60 139.39 69.76 60.36 42.99 34.34 33.49 62.74 95.71 31.3 S156F 27 okt)
135. 262.39 235.39 200.85 137.60 67.21 63.998 42.78 24.68 34.56 70.54 106.24 31.63 31.66 27.¢0
149. 276.76 255.95 226.67 124.46 rag 67.59 42.65 35.7 35.98 76.85 1135.66 23.58 33.44 28.37
145. 264.05 241.88 221.42 147.40 (sun Vz AA. 32 37.3 37.63 79.79 120.07 $35.03 33.86 29.07
158. 276.49 237.76 206.85 151.22 72.3: F 44.37 50.39 SO5ID 83.55 122.89 JANUS 34.09 29.07
155. 480.525 ~25flf 226,82 154.65 77.90 7‘ Da2 45.85 40,46 38.0: 87.81 129.68 5.51 $3.09 29.70
168. ehagdm § colwat — ecoent 143.65 73.32 73.98 49.56 41.58 | 49.40 90.12 126.47 37.05 37.19 30.37
165. 296.19 265.08 234,15 MERI fe 79.24 73.91 53.76 $9335 41.93 94.17 142.65 3?.10 30.79
170. 289.66 262.54 224.52 159.82 65.50 85.12 93.76. 41.88 40.51 55.83 145.65 37.83 31.44 °
175. 234.22 266.58 229.39 154.85 69.14 85.26 95.24 44,05 4li22 102.05 145. 2h 37.91 32.02
138. 290.32 271.66 232.49 153.60 SGsne 33.7 54.93 42.63 44.10 105.51 HO EC S56 32.63
135. 291.66 266.61 230.88 160.97 65.91 89.05 595.95 46.35 43.935 1039.17 153.20 38.108 33.07
190. 302.71 273.07 231.85 158.27 99.25 88.2 55.76 46.28 44.635 109.37 157.60 AL.71 33.56
195. 291.4 § 282.32 259.76 151.39 69.935 £5.36 55.88 4? .83 Saar 113.19 160.77 39.07 34.22
200. 289.73 259.85 231.42 156.35 91.85 86.93 60.59 49.15 44.76 110.54 161.50 40.12 34.58
205. 2986.19 275°:41 236.12 144,95 65.57 59 .a¢ 93.43 48.24 43.40 109.76 163.52 41.76 34.90
210. 280.54 269.27 245.39 159.83 81.71 83.38 59.24 47.58 46.24 1180.39 166.65 43.44 35.54
215. 291.31 261.22 230.54 159.27 62.88 90.31 61.21 8.85 45.98 116.95 167.60 43.88 35.95
220. 292.36 281.27 249.76 155.90 91.69 9409 62.09 49.88 45.44 111.98 169.¢7 41.61 36.45
PRC 13-Wr2-174
14
293.82
294.598
298.98
295.29
297.51
298.15
296.34
293.58
293.76
297.46
293.43
292.78
289.98
292.07
285.34
284.66
292.34
290.68
297.85
297.46
286.009
279.22
297.19
292.89
297.05
284.63
289.88
287.87
294.19
295.54
284.83
279.37
288.61
287.56
280.49
287.63
238.32
302.18
284.93
292593
294.15
$83.22
386.22
303.17
284.12
289.46
292.85
286.12
293-935
293.86
1S
279.39
276.93
262.22
265.88
272.49
261.85
270.46
270.95
277.4
280.61
235.44
270.41
268.95
272.85
264.58
265.12
269.83
285.83
278.46
284.85
263.98
267.76
262.17
267.44
273.2
262.61
264.78
266.44
263.00
269.98
263.78
fea.
2738.44
269.18
258.12
262.15
276.29
268.76
266.17
72.02
271.54
277.68
283.00
280.83
263.01
272.12
274.66
264.54
271.67
273.46
16
246.98
248.78
229.58
240.34
236.22
229.90
256.32
233.22
, a4. 30
232.51
240.34
231.46
231.52
233.83
230.32
229.78
227.898
259.71
244.76
251.88
245.29
246.39
231.67
247 .93
252.24
235.58
231.34
230.49
238.44
236.46
234.34
251.76
259.49
243.51
234.93
229.80
249.88
Pile Y=
245.61
245.02
259.95
257.46
248.88
241.12
249.39
241.88
251.83
243.66
251.83
249.29
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169.95
175.15
159.67
167.75
159.9
163.32
165.30
164.85
154.92
160.55
159.77
170.05
161.13
157.92
152.45
158.07
156.20
163.47
165.17
164.13
149.27
170.32
171.00
167.85
159.82
156.05
159.22
168.15
156.13
158.07
178.57
162.33
167.70
174.57
169.45
167.05
161.52
169.92
177.12
180.02
169.35
180.72
177.52
183.60
168.47
170.08
179.82
194. 42
186.90
195.07
18
95.67
101.12
101.07
94.05
6.02
89.69
85.59
989.45
69.93
101.22
102.39
102.05
91.43
95.83
100.07
107.39
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105.17
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103.76
109.29
103.44
107.29
111.89
105.9
105.62
109.83
104.51
94.99
111.63
115.66
114.19
114.58
112.63
111.85
115.45
115.73
165.68
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117.61
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105.44
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112.63
114.85
116.93
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119.34
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93.81
92.49
91.86
93.31
95.81
96.36
7.12
7.62
92.09
92.95
105.68
101.39
95.48
95.09
101.56
91.39
92.21
89.45
924,93
95.64
95.49
24.76
30.62
99.59
94.76
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105.12
104.39
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63.21
62.50
59.24
59.087
61.43
65.75
65.31
65.62
61.95
60.05
635.21
65.21
63.62
65.02
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63.29
63.86
64.59
64.17
65.79
65.43
66.19
64.57
61.39
65.26
64.43
65.95
70.41
74.12
64.98
65.40
64.74
64.29
67.64
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65.83
69.56
64.45
65.07
71.61
67.81
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73.76
74.39
70.41
72.29
76.54
73.45
73.78
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45.357
48.07
49.34
50.44
53.56
51.56
51.05
91.29
$2.61
53.58
47.63
47.90
52.58
54.12
54.12
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51.32
56.3
55.34
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55.56
56.29
53:63
56.37
52.76
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57.32
59.34
53.24
59.96
57.34
57.86
58.54
59.02
58.61
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55.39
59.05
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50.68
59.45
61.48
99.52
36.63
59.93
98.95
of .66
59,59
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PAGE
22
47.17
46.00
47.29
48.12
50.68
50.85
50,49
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49.78
49.76
43.10
60.52
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115.63
117.44
116.12
119,00
117.76
120.95
122.73
118.58
118.58
120.61
120.73
122.18
124.60
124.71
125.66
125.41
124.61
125.93
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133.82
126.83
128,93
127.89
123.61
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128.44
129.12
128.12
129.46
135.02
137.57
134.80
133.65
138.25
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138.47
141.85
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128.70
141.42
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139.65
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170.57
172.38
175.05
177.682
174.35
176.92
160.17
102.77
101.67
101.80
101.52
104.77
186.00
187.07
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185.32
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166.00
168.07
190.05
188.50
169.67
190.25
192.20
192,42
190.63
192.92
193.80
194.00
194,00
194.32
194.07
193.70
195.25
196.70
198.02
199.52
199,52
199,13
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200.50
202.50
202.55
1938.63
281.82
198.73
201.41
199.98
200.54
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44.05
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47.16
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49.02
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51.19
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50.19
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45.56
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44.56
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