Document 3VjvBRrN90MxYQN9QX5KDM0
Benjamin/Clarke Associates, Inc.
10605 Concord Street, Suite 501
Kensington, Maryland 20895
(301) 949-1414
Af?pCnc(i
A
Dr. Roy T. Gottesman The Vinyl Institute Wayne Interchange Plaza II 155 Route 46 West Wayne, NJ, 07470
Dear Dr. Gottesman,
December 4, 1989
The enclosed report, prepared at the request of the Vinyl Institute Technical Committee, contains a fairly detailed analysis of the test method for Toxic Hazard, developed under the auspices of the National Institute for Building Sciences (NIBS).
In brief, we think that the hazard concept advanced by the method, the so called IT,_0 concept, has three big flaws:
1. The significant differences it shows among products (except, perhaps, those associated with PTFE-coated wire) are due almost entirely to experimental conditions which suppress the amount of carbon monoxide formed to levels well below those one would expect under the full-scale conditions the method tries to duplicate. If more realistic test conditions could be employed, most of the differences observed among products would disappear.
2. The contribution
IT5o cannot predict toxic hazard, or the of any single product to toxic hazard, if more
than one product is burning.
3. The IT5q errors of the
scale is compressed and thus the experimental measurements are a sizeable fraction of the
apparent differences found between products.
SPI-11014
B/C
2- -
We do not believe these flaws in the IT5Q can be corrected
without sacrificing some of the method's other desirable features -
notably that conditions.
which exposes all products to the same thermal
Even without the IT5Q, however, the radiant apparatus used
offers an attractive alternative to existing methods.
Besides
permitting uniform exposure conditions, in a well designed apparatus,
it uses a radiant heat source and can be used for assembled end-use
products in addition to single materials. Finally, it can be used to
measure ignition time and mass loss rate as well as toxic potency.
These three properties are Key elements of toxic hazard, even though
the form in which they are used implicitly in the present version of
the test - the IT,_Q - is not a good one.
In view of the foregoing facts, we recommend the following:
1. That the Vinyl Institute support the NIBS test apparatus as the basis for an eventual ASTM test method for obtaining some of the component measurements needed for toxic hazard;
2. That the Vinyl Institute oppose inclusion of the IT5Q in any submission to ASTM or in any subsequently-developed ASTM procedure;
3. That the Vinyl Institute participate actively in the proceedings leading to the final development of the test method.
Very truly yours
Dr.' Frederic B. Clarke ____ Benjamin/Clarke Associates
D-r-.- :--Marcelo M. H*i'r*-s'* cvh- --l-e- > r-
BFGoodrich
SP1-H015
NIBS Toxicity Test
Frederic B. Clarke and Marcelo M. Hirschler
I. Introduction and Background
The basic philosophical background behind the proposed NIBS test
was that smoke toxic potency tests should not be used in isolation to
regulate the fire performance of materials or products. Standard
toxic potency tests measure the toxicity of the smoke from small
amounts of materials, burnt under conditions which are different for
each material, being based on the characteristics of the material.
This means
that they suffer
from,
at least, three major
shortcomings.
These are: (1) the characteristics which enhance the
fire performance of a material, e.g. very low ignitability, are
ignored; (2) such tests are not, generally, designed to allow for the
testing of products in their final use form? and (3) the conditions
under which the test is carried out may produce a spectrum of
products with toxicity quite different from those formed under real
full-scale conditions.
It has become widely accepted that smoke intoxication in a real fire scenario is based on at least three factors. These are: (1) the mass loss rate, or the concentration of airborne combustion products.
-1-
SPI-H016
generated by a burning item, (2) the time to ignition (i.e. the time until such combustion products are being generated) and (3) the toxic potency of the smoke under the fire conditions of interest.
\ The NIBS toxicity test was intended to incorporate, implicitly or
explicitly, the three factors cited above as essential for smoke
toxicity and to remedy the three major objections to toxic potency
tests.
This document was prepared to examine how well the current
version of the test succeeds in meeting these expectations.
The NIBS test was developed by a Working Group which decided to
simulate post flashover conditions, because fire statistics indicate
that most fire victims die in fires which are known to have left the
room of origin.
The NIBS test approaches the estimate of potential
toxic
hazard by an implicit combination of the three factors
mentioned earlier. This implicit estimate has been designated as the
median sample irradiation time needed to kill 50% of the exposed
animals, or IT5Q-
The chosen test conditions are a radiation level
2 of 5 W/cm , and a relatively high (>16%) oxygen content.
Irradiation is ended when sufficient smoke has been produced to kill
animals by the end of the 30 minute total exposure (and 14 days
post-exposure).
Alternative proposals to the IT^q concePt have been made which identify means for making such a combination by explicit measurements of each factor [1,2].
-2-
SPI-11017
II. Analysis
A. Carbon Monoxide
The principal toxicant in fires is carbon monoxide, which is responsible for the overwhelming majority of fire fatalities. Therefore, a smoke toxicity test needs to be able to produce the yield of carbon monoxide, or the carbon monoxide/carbon dioxide ratio, accurately in order to be able to represent real fire scenarios.
It is possible to calculate the C0/C02 ratios (r) determined in
many of the products tested in the NIBS apparatus, using the present
protocol.
They are shown in Table 1.
(The basis for the
calculation, including assumptions made, are explained in detail in
Appendix A).
Most flashover fires occur in ventilation-limited
scenarios where there is excess fuel. In such full scale tests, or
fires, there is a significant volume of work which reports CO yields
or C0/C02 ratios. Some examples of CO yields are shown in Table 2.
A comparison of the results of Tables 1 and 2 shows that the majority of the NIBS tests yield C0/C02 ratios which are lower than 0.05, while the full scale tests yield values ranging from 0.15-0.8. This indicates that the NIBS test produces only 1/3 to 1/15 of the CO that flashover fires would produce.
-3-
SPI-H018
This discrepancy is particularly important in light of the fact that, in such scenarios, the production of CO is affected mainly by variables such as geometry, ventilation, configuration and mixing, and only somewhat (second order) by the chemical composition of the product being burned [3], The most important aspect of CO production which is related to the fuel is its volatilization rate.
Experience also shows that in full scale tests where flashover is achieved, as the flux passes 4 W/cm2, the oxygen level in the room
(coming out the door) is near zero. This is the rule, rather than
the exception, and such conditions differ both qualitatively and
quantitatively from those under which the NIBS test is being run.
The oxygen is too high and the CO produced is too low to simulate
flashover.
This is unlikely to make much difference in materials
whose smoke toxicity depends on gases such as HCl, HF or HCN, but it
severely understates the relative hazard of CO producers, and thus
overstates the effects of those products that generate other gases.
Table 3 presents a calculation of the range of fractional effective dose (FED) of the smoke from the NIBS tests, based on the assumption (reasonable estimate) that 30 rag/L is a lethal dose for 30 min exposure times. Table 4 contains an estimate of the lethal smoke dose, which can be calculated from the data supplied by the NIBS Working Group together with the only 12 NIBS product test results released to date (for details of the calculations see Appendix B).
-4-
SPI-11019
It is clear from Tables 3 and 4 that the NIBS smoke, especially
for CO producers, is much less toxic than most smokes are known to be
near flashover (and as measured by other tests)*
This is a
consequence of the intense burning conditions, which cause relatively
complete combustion of many of the products, thus decreasing the
toxicity of their smoke when compared to that in real fires.
B. Methodological Problems
It is instructive to estimate the effect of potentially lower
values of toxic potency on the IT5Q. Table 5 contains a tabulation
of "A", the IT5o value if the lethal smoke dose, the L(Ct *50 were one third of the observed value (calculated in Table 4). Such lower
values are, by no means, extreme.
They range from a low of 210
mg-min/L, for painted mineral fibreboard to a high of 1500 mg-min/L
for formica/particle board.
For comparison, the toxic potency of
Douglas fir is generally taken to be 900 mg-min/L (the reported
LC value for a 30 minute exposure; this same value was used for
all products in the calculations of Table 4). The value for Douglas
fir calculated for Table 5 (after dividing by 3 the observed value
from the NIBS test) is quite close to this: 830 mg-min/L.
-5-
SP1-U020
Inspection of Table 5 shows that substituting a more toxic smoke
for the smoke measured in the NIBS test compresses the values of the
IT50 of all 12 samples into a range of less than 4 minutes. The
experimental value of the IT^q has a precision of not less than l
minute, so that the uncertainty of the measurement is half the range
of all the values into which the measurement can reasonably be
expected to fall.
This is not a robust or highly-discriminatory
decision-making tool.
The analytical expression for IT5Q (see Appendix B) contains,
but the IT5q ky itself is not, a readily understandable index of
hazard.
It has two major shortcomings. First, its scale is more
compressed where products are more hazardous, i.e. where toxic dose
is low and mass loss is high. A disproportionate share of the range
of the IT5Q is applicable only to relatively inert products. This
can be seen in Figure 1, where (IT5Q - t^) is plotted against X,
the ratio of the L(Ct)5Q to the mass loss rate: the lower the value
of X the more hazardous the product (assuming a constant ignition
time, t^).
It should also be clear that reducing the incident radiant flux
in the test method, and thereby the mass loss rate, will move a
number of the better-performing products off the scale, to the right
(i.e. towards low toxicity).
This is not, strictly speaking, a
misleading result, because it indicates that the toxicity threat from
such products in many real fires is negligible.
-6-
SPI-U021
It is unlikely, however, to satisfy those who are searching for a scale which will accommodate the toxic hazard of the full range of common products-
\
The second shortcoming is an outgrowth of the fact that the IT50, to the extent that it has any applicability at all, aims to provide an index of hazard under intense fire conditions, where virtually everything combustible exposed will burn. A reasonable gauge of toxic hazard under such conditions would be the rate of generation of the lethal toxic dose of the total smoke from the burning compartment. This can be calculated as:
dF/dt = SN (Aj
= Z (Aj/Xj)
in which the summation is made over all N combustibles, each of them with an exposed surface area A^ and a value of the X ratio X ^. Thus, while the summation of the X values of all combustibles can yield the toxic hazard of the total smoke, the IT5Q, by contrast, cannot readily be rendered into a form proportional to Xj. It does not, therefore, lend itself either to prediction of the total room fire hazard or to any give product's relative contribution to that hazard.
7- -
SPM1022
III. Discussion and Conclusions
The development of the NIBS test was fueled, in large measure, by
shortcomings in toxic potency tests, especially when the latter are
used alone as a basis for regulation.In particular, the NIBS test
sought
to: (l) expose all products to the same thermal conditions;
(2) work well for products in their assembled, or composite form; (3)
provide at least a heuristic measure of toxic hazard, i.e. take
account of the product's other fire properties besides toxic potency
which bear on the threat from its smoke in a real fire. The method
produced has, consequently, a unique set of features, but it also has
its own set of resulting flaws. Among those flaws afflicting the
method itself are the following:
1. The post-flashover
conditions aspired to have not been
attained.
The thermal conditions of flashover can be
duplicated but the ventilation conditions of flashover cannot
readily be duplicated by this test in its present design.
2. The test produces conditions under which carbonaceous materials generate only a fraction of the carbon monoxide they would produce under real flashover conditions, making them look better than they should, in comparison to materials whose toxic potency is relatively unaffected by ventilation.
-B-
SPI-11023
Among those flaws associated with the IT50 are the following:
1- The comparatively low toxic potency of smoke from products
whose
principal toxic agent is carbon monoxide is the
principal
reason
that
there
is any significant
differentiation of products by IT5Q. Calculating the
IT50 using toxic potencies characteristic of what would be
observed if the products were exposed to the low oxygen
levels
associated
with
flashover
causes
almost
all
significant differences in IT5Q to disappear.
2. The
concept is a compressed scale of performance? the
imprecision of measurement is so large in comparison to the
magnitude of the quantity being measured that the IT5Q is a
poor predictor of hazard.
3. The
IT5o formulation is necessarily based on flashover
conditions, which means that everything combustible in the
compartment is burning. To gauge the contribution of a given
product to the overall toxic threat in such a scenario, the
index used should be capable of additivity, i.e. the index of
each component product should be summable to the index of the
complete fire. The IT5Q lacks this property.
-9-
SPM1024
The foregoing facts make clear, the authors believe, that more work is needed if the NIBS test is to approach the expectations which led to its development.
To be sure, the IT5Q concept, which attempts to account for
fire properties beyond toxic potency, depends for much of the utility
it was expected to have upon an inherently unrealistic set of
combustion conditions.
The second anticipated advantage of the NIBS
test, exposure of all materials to the same thermal conditions, has
not yet been convincingly demonstrated.
Indeed, the penalty the
method extracts for exposing all products to the same conditions is
that those conditions are necessarily contrived, and the results
misleadingly favor one group of products, the CO producers, over
another.
Making the conditions more realistic will have another set
of penalties, as yet unexplored.
There might be some merit in using the NIBS apparatus in an
alternative operating manner.
For example, the toxic potency could
be measured by varying the amount of material exposed (rather than
the irradiation time) and this accompanied by measurements of the
time to ignition and the mass loss rate. Such results could then be
used *for an explicit calculation of a potential toxic hazard
parameter replacing the IT5Q.
This approach is being investigated
at the Center for Fire Research at NIST.
-10-
SPI-11025
The correct way to compare the fire performance of products is#
of course, fire hazard assessment, which may require toxicity data as
input.
The IT50 parameter cannot be employed as an explicit input
into fire hazard or fire risk assessment procedures or models; its
only foreseeable application is for control of materials or products
based on toxicity, and for this purpose it has been found flawed. On
the other hand, the explicit calculation of a toxic hazard parameter
has the advantage that the individual properties measured can be used
for fire hazard assessment.
Stripped of the special features intrinsic in the present operating manner, the NIBS test is simply an apparatus, employing a radiant combustion source, for the determination of toxic potency. There is a good deal of sentiment favoring such an apparatus as an alternative to most of the other existing methods, since it can accommodate assembled products and is thought to offer a more realistic method of heating the sample. It should be noted, however, that considerable data must be developed before such an apparatus can be expected to be widely adopted or to have much utility for standards making organizations.
-11-
SP1-11026
References
1. M.M. Hirschler, J. Fire Sci. 5, 289 (1987). 2. V. Babrauskas, Int. Conf. "FIRE: control the Heat - Reduce the
Hazard," Fire Research Station, October 24-25, 1988, London, UK, paper 7. 3. V. Babrauskas, R.H. Harris, R.G. Gann, B.C. Levin, B.T. Lee, R.D. Peacock, M. Paabo, W. Twilley, M.F. Yoklavich and H.M. Clark, "Fire Hazard Comparison of Fire-Retarded and Non-Fire-Retarded Products," NBS Special Publ. 749, July 1988, National Bureau of Standards, Gaithersburg, MD.
-12-
SPI-11027
I
Table 1
Value of CO/CO. ratio. z
t.
for NIBS test samoles
# Sample
Test ID
Minimum value
Maximum
1 PVC conduit
1.1
2 PVC wire
2.5
4 Form/Part brd
4.2
4 Form/Part brd
4.3
5 Ptd Min Fibrbrd
5.3
6 Nylon carpet/PU
6.1
7 Wool carpet/felt
7.1
7 Wool carpet/felt
7.3
8 Cotton Polyureth.
8.2
9 Cotton/FR PU 9 Cotton/FR PU
9.3 **
9.4
10 Cotton/1iner/PU
10.1
11 ABS cabinet
11.3
11 ABS cabinet
11.2
12 FR Douglas fir
12.2
12 FR Douglas fir
12.3
13 D fir plywood panel 13.2
13 D fir plywood panel 13.3
1.8 0.15 0.027 0.16 0.24 0.034 0.023 0.063 0.032 NA 0.42 0.21 0.038 0.059 0.21 0.83 0.035 0.059
*
No flame
Light cotton
1.8 0.19 0.028 0.17
* 0.24 0.36 0.026 0.068 0.035 0.137 0.46 0.22 same 0.061
* 0.21
* 0.83 0.037 0.067
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SP1-11028
Table 2 CO yields or CO/CC>2 ratios
CO Yield C0/C02 ratio g/g
Reference
Flashover-
limited ventilation FRCA/NBS study NBS basement tests
0.10
0.18-0.23 0.18-0.21 0.26-0.34
Wood post-flashover
fires
0.3-0.36 0.27-0.5
Simulation of Sharon, PA, nursing home fire Cable tray fires
0.1-0.4 0.1-0.5
Post-flashover model 0.3
0.5
PMMA enclosure fire 1.2
0.75
Natural gas enclosure 0.6
0.6
BSI Babrauskas et Clarke
Beyler
NIST Hirschler et Mulholland Beyler Zukoski
1988
-14-
SPI-11029
Lethality Product
Table 3
of NIBS Smoke and Fractional Effective
(FED Based on LC-n of 30 mg/L)
Smoke cone.
FED
Deaths
mg/L
-- (out of
Dose
1 PVC conduit PVC conduit
11-8 47.8
0.4-0.4 1.6-1.7
3 6
2 PVC wire PVC wire PVC wire
40.1 42.9 64.5
1.3-1.5 1.4-1.6 2.2-3.0
0 0 6
4 Form/Part brd Form/Part brd Form/Part brd
75.4 108.4 170.1
2.5-2.8 3.6-4.2 5.7-6.7
0 0 6
5 Ptd Min Fibrbrd Ptd Min Fibrbrd Ptd Min Fibrbrd
24.0 29.4 28.9
0.8-1.0 1.0-1.3 1.0-1.3
0 0 2
6 Nylon carpet/PU Nylon carpet/PU
31.4 59.9
1.0-1.1 2.0-2.1
0 6
7 Wool carpet/felt Wool carpet/felt Wool carpet/felt
131.4 90.7
107.3
4.4-4.8 3.0-3.4 3.6-4.1
6 2 6
8 Cotton Polyureth. Cotton Polyureth. Cotton Polyureth. Cotton Polyureth.
78.1 100.4 101.1 104.7
2.6-2.9 3.3-3.9 3.4-4.0 3.5-4.2
0 6 3 6
9 Cotton/FR PU Cotton/FR PU Cotton/FR PU Light Cotton/FR PU
66.3 81.0 96.9 89.4
2.2-2.4 2.7-2.9 3.2-3.6 3.0-3.3
0 1 5 6
10 Cotton/1iner/PU
65.3
2.2-2.4
1
11 ABS cabinet ABS cabinet
47.6 71.3
1.6-1.7 2.4-2.6
3 6
12 FR Douglas fir FR Douglas fir FR Douglas fir
88.4 128.3 130.4
2.9-3,. 2 4.3-4.8 4.3-5.0
0 1 6
13 Plywood panel Plywood panel Plywood panel
89.5 89.3 91.2
3.0-3.2
3.0-3.2
3.0-3.4
----------- ---
0 0 6
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SPI-11030
Table 4 Results of Calculations Using Data from the NIBS Test
Product 9
Test ID
NIBS Tet Data
t. (min)
TT50. (mm)
m
m (g/min)
L (mg-min/L)
1 2 4 5 6 7 8 9 10 11 12 13
PVC conduit PVC wire Form/Part brd Ptd Min Fibrbrd Nylon carpet/PU Wool carpet/felt Cotton Polyureth. Cotton/FR PU Cotton/liner/PU ABS cabinet FR Douglas fir D fir plywood panel
1.1 2.5 4.3
5.3
6.1
7.1
8.2 9.3
10.1 11.2
12.3 13.3
0.6 1.3
1*3 0 1.2 0.5 0.5 0.5 0.6
2*9 0 0.5
1.5
15.0 7.5
>15.0 2.5 6.0
9.0
4.5 4.5 3.5 7.0 6.0
8.0 1.0
5-2** 0.4 6.7 3.3 2.2 3.9 3.2 7.1** 3.5 3.0
1400 1500 4500
630 1700 2900 2600 2700 1900 2100 3400 2500
* Estimated from animal lethality
no ignition observed; m is somewhat overstated.
9 Product
Table 5 Effect of Lower Toxic Potency on the IT_n
Test ID
Z (min)
**
IT50 (min)
L/3 (mg-min/L)
1 PVC conduit
1.1
2 PVC wire
2.5
4 Form/Part brd
4.3
5 Ptd Min Fibrbrd
5.3
6 Nylon carpet/PU
6.1
7 Wool carpet/felt
7.1
8 Cotton Polyureth.
8.2
9 Cotton/FR PU
9.3
10 Cotton/liner/PU
10.1
11 ABS cabinet
11.2
12 FR Douglas fir
12.3
13 D fir plywood panel 13.3
0.9 13.7
6.1 >15.0
1.3 5.5 8.5 4.0 3.9 1.5 7.0 5.5
1.5 15.0
7.5 >15.0
2.5 6.0 9.0 4.5 4.5 3.5 7.0 6.0
470 500 1500 210 570 970 870
900 630 700 1130 830
* Z =f.IT^,,. - Time to Iqnition; see Table 4. Estimated from animal lethality.
A (min)
1.0 4.8 3.4 3.7 1.8 2.6 3.3 2.1 1.9 2.7 2.3 2.4
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SPI-11031
Appendix A Estimate of C0/CC>2 ratios in the NIBS test
Assumptions
\
1* CO production in the NIBS test looks like one of the curves in
Figure 1.
It begins at t^ and stops at tc.
The time of
cessation of CO production. t
,.
^ ' c, lies
and IT, time when irradiation is stopped.
.. between
. ..
, fo
flameout time, t
2. The system is leak-free: CO and C02, once produced, do not escape.
As a consequence of assumption 1, the minimum value of S, the final CO level, is [C0]1# and the maximum value is [CO]2, with the value somewhat in between:
C0^1 < B < [CO]2
The area under the CO production curve is measured and reported as the CO 30 minute Ct product. The integration (of [CO] dt) is carried out between time = t^ and 30 min, along curve 1 or curve 2. Assuming no leaks, each curve is a trapezoid, with an area of:
Area = 0.5 (b^ + b2) * h,
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SPr-11032
where h is the final CO concentration. Thus;
[CO]1 = 2 * Ct/[(30 - ti) + (30 - tfQ)] and
[CO]2 = 2 * Ct/[(30 - tL) + (30 - tIT)]
Since
the
chamber
does
not
leak, the measured maximum
concentration of C02 is also its final concentration and;
[C0]1/([C02] max) < B/([C02] max) < [C0]2/([C02) max).
The calculated range of r, using this approach, is reported in Table 1 for each of the 12 NIBS products with sufficient reported results*
-18-
SPI-U033
Appendix B Mathematical aspects of the NIBS test
1. Analytical expression of IT5Q
The *T5o is the sura of the time required for the sample to burn appreciable mass loss (t^) and the time required to produce a lethal level of smoke (Z).
IT 50
t. 1
+
Z.
The lethal smoke concentration is produced during the irradiation
period and exposure is continued for the balance of the 30 min
exposure.
Hence, the lethal concentration-time product, over a 30
min period starting at t^, can be expressed as:
L(Ct)5Q == L = Integral (between 0 and Z)[c(t)dt] + [c(Z)(30-Z)]
Assuming that the mass loss rate is constant with time, between t^ and IT, with V the volume:
c = (m*t)/V L = (l/V)[^*m*Z2 + m*(30S - Z2)]
-- 19-
SPI-U034
The resulting quadratic equation can be solved, for the unknown Z, yielding:
Z = 30 - J{900 - E(2LV)/m])
(since the other root is greater then 30 min, and is, thus, impossible) and
IT50 = ti + 30 " 7(900 - [(2LV)/m])
2. Estimates of toxic potency
The values of IT50 (rough) and t^ and data to calculate m, are all available for the 12 products for which full NIBS results have been reported The foregoing expression can, thus, be evaluated for L.
Z = IT50 "
L = (1/2V)*[m*Z*(60-Z)].
It was assumed for this that: m = (increase m m)/Z, and that no appreciable mass loss occurred before, t^ or after irradiation was stopped (when the communication from exposure to combustion chamber is closed). The calculated values of L are listed in Table 4.
-20-
SPI-11035
Time
o o
SPI-11036
FIGURE 2
Dependence Of IT50 on Toxic Potency and Mass Loss Rate in the NIBS test (xLCt50/mdot)
!TSG i--gnition time, ti, (min)
0.0
4-00*0
800.0
1200.0
1600.0
C/3 x (mg -- min/l/g/min)
*0 t-+Jl
-22-
THE CORROSIVITY OF FIRE GASES
D.D. Drysdale & A.J.R. MacMillan Unit of Fire Safety Engineering University of Edinburgh
TT *T>
Su.
SPI-11038
rfa__________________
' ............ ......... ......... MATERIALS
1. Douglas Fir 2. Fire Retarded ABS 3. Nylon 4. Noryl 5. Rigid PVC (CIM) Compound 6. Standard PVC Mire and Cable Compound 7. Low Flammability PVC Mire and Cable Compound 8. Fire Retarded Polypropylene
ft
SPI-11039
, ----- -------------
-
~: "
-- ~`
_ : -------U
I
Chamber measures 13.5 mj in volume. Exposure lasted 1 h. Targets were copper mirrors, 500 A thick, 1 in x 0.25 in. Post-exposure was carries out at room temperature ft 75% RM. Resistance measurements were made after 1h, 24h, 48h and 72h.
_/
S W -II040
EXPOSURE CONDITIONS F Free burning 0 Enclosed sample, with open air access R Enclosed sample, with restricted air access
SPI-11041
w ln d y w
SPI-11042
h C r.
SPM1043
SPI-11044
. <i, .
v.
I- *
T PVChe samples produced more corrosivity than the other
SAMPLES, BUT THE DIFFERENCES WERE NOT VERY LARGE: ALL HERE IN THE SAME BALL-PARK.
AT HIGHER AMBIENT TEMPERATURES, TNI NYLON SMOKE CORRODED MUCH
MORE HEAVILY THAN THE PVC SAMPLES: ALL MIRRORS HERE TOTALLY
CORRODED LONG BEFORE THE END OF THE EXPOSURE.
tr. :: !
SPI-11045
ft
Experiments mere done in which nylon mas tested with the
CHAMRER AT ELEVATED TEMPERATURE (UP TO 100* C).
The INCREASE IN TEMPERATURE CAUSED A DRAMATIC EFFECT IN THE CORROSIVITY OF NYLON SMOKE.
f^O ".
/
SPJ-11047
A
.I., *i -4*' . **- v..-i.*o, ,
-
SPI-11048
To: R.T Gottesman/C.N. Bush From: Marcelo M. Hirschler
December 5, 1989
NIST Center for Fire Research 1989 Fire Research Conference
This conference is the forum for NIST (ex NBS) researchers and their grantees to explain the research they have done over the last year. The research usually runs the gamut of very fundamental theoretical work to quite applied programs. This year's meeting had an additional feature: it contained three panel discussions on relevant wide-interest issues.
The programs of interest to the Vinyl Institute were probably mostly
in the area of smoke toxicity.
It was stated very clearly that
small-scale toxicity tests are mostly useful as screening tests to
identify any (very rare) products which give off smoke of unusual
toxicity, either in terms of it being higher than the norm or in terms
of it being different from the norm. This can only, of course, be done
by using animals.
As far as using toxicity results for fire hazard
assessment, the consensus at NIST is that small scale tests can tell you
something about the generation of toxicants other than CO, but in order
to get the CO contribution it is essential to carry out full scale
tests.
Moreover, there is virtually no effect (or at most only a
minimal one) of fuel (combustible) structure on CO generation in full
scale fires where there is no excess of air present. Therefore,
toxicity contributions of any particular smoke in a specific scenario
should be calculated from a combination of two parts: (a) a small scale
test that measures all gases other than CO, (b) a model that predicts CO
formation in the scenario in question, independent of the product being
considered.
NIST is working on developing that model. The tests being
carried out by NIST on full scale rooms will help guide the NIST work in
that direction, but the overall model is not expected to be ready for
ca. 5 years.
The only exception to this toxicity concept is Yves Alarie (UPITT),
who has combined his mice and exposure chamber with the output from the
cone calorimeter, to get a time to toxic effect from burning the top
layer of materials.
This is unlikely to result in either good science
or practical testing technology.
NIST sees it as a "last chance" for
the concept of flow through technology to demonstrate relevance.
The other important results presented are the measurement, at SwRl, of the toxicity of HBr and of combinations of HC1 and HCN and of HC1, HCN and CO, in rats. HBr appears to be roughly as toxic as HC1 (maybe 10% more, which is statistically indistinguishable), while the lethal effects of the combinations are all additive (or even perhaps slightly less) within a 20% error.
One issue of importance raised in the discussions is the fact that the fire hazard model HAZARD I may be too easy to use, so that the user (who can then claim to be an expert witness in litigation) might not understand the implications of the results he is generating. This is a novel idea, which merits a lot of thought.
SPl-11049