Standard Test Method for Measuring Heat Transfer Rate Using a Thin-Skin Calorimeter

SIGNIFICANCE AND USE
3.1 This test method may be used to measure the heat transfer rate to a metallic or coated metallic surface for a variety of applications, including:  
3.1.1 Measurements of aerodynamic heating when the calorimeter is placed into a flow environment, such as a wind tunnel or an arc jet; the calorimeters can be designed to have the same size and shape as the actual test specimens to minimize heat transfer corrections;  
3.1.2 Heat transfer measurements in fires and fire safety testing;  
3.1.3 Laser power and laser absorption measurements; as well as,  
3.1.4 X-ray and particle beam (electrons or ions) dosimetry measurements.  
3.2 The thin-skin calorimeter is one of many concepts used to measure heat transfer rates. It may be used to measure convective, radiative, or combinations of convective and radiative (usually called mixed or total) heat transfer rates. However, when the calorimeter is used to measure radiative or mixed heat transfer rates, the absorptivity and reflectivity of the surface should be measured over the expected radiation wavelength region of the source.  
3.3 In 4.6 and 4.7, it is demonstrated that lateral heat conduction effects on a local measurement can be minimized by using a calorimeter material with a low thermal conductivity. Alternatively, a distribution of the heat transfer rate may be obtained by placing a number of thermocouples along the back surface of the calorimeter.  
3.4 In high temperature or high heat transfer rate applications, the principal drawback to the use of thin-skin calorimeters is the short exposure time necessary to ensure survival of the calorimeter such that repeat measurements can be made with the same sensor. When operation to burnout is necessary to obtain the desired heat flux measurements, thin-skin calorimeters are often a good choice because they are relatively inexpensive to fabricate.
SCOPE
1.1 This test method covers the design and use of a thin metallic calorimeter for measuring heat transfer rate (also called heat flux). Thermocouples are attached to the unexposed surface of the calorimeter. A one-dimensional heat flow analysis is used for calculating the heat transfer rate from the temperature measurements. Applications include aerodynamic heating, laser and radiation power measurements, and fire safety testing.  
1.2 Advantages:  
1.2.1 Simplicity of Construction—The calorimeter may be constructed from a number of materials. The size and shape can often be made to match the actual application. Thermocouples may be attached to the metal by spot, electron beam, or laser welding.  
1.2.2 Heat transfer rate distributions may be obtained if metals with low thermal conductivity, such as some stainless steels, are used.  
1.2.3 The calorimeters can be fabricated with smooth surfaces, without insulators or plugs and the attendant temperature discontinuities, to provide more realistic flow conditions for aerodynamic heating measurements.  
1.2.4 The calorimeters described in this test method are relatively inexpensive. If necessary, they may be operated to burn-out to obtain heat transfer information.  
1.3 Limitations:  
1.3.1 At higher heat flux levels, short test times are necessary to ensure calorimeter survival.  
1.3.2 For applications in wind tunnels or arc-jet facilities, the calorimeter must be operated at pressures and temperatures such that the thin-skin does not distort under pressure loads. Distortion of the surface will introduce measurement errors.  
1.4 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard.  
1.4.1 Exception—The values given in parentheses are for information only.  
1.5 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regula...

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NOTICE: This standard has either been superseded and replaced by a new version or withdrawn.
Contact ASTM International (www.astm.org) for the latest information
Designation: E459 − 05 (Reapproved 2016)
Standard Test Method for
Measuring Heat Transfer Rate Using a Thin-Skin
Calorimeter
This standard is issued under the fixed designation E459; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision.Anumber in parentheses indicates the year of last reapproval.A
superscript epsilon (´) indicates an editorial change since the last revision or reapproval.
1. Scope 1.4.1 Exception—The values given in parentheses are for
information only.
1.1 This test method covers the design and use of a thin
1.5 This standard does not purport to address all of the
metallic calorimeter for measuring heat transfer rate (also
safety concerns, if any, associated with its use. It is the
calledheatflux).Thermocouplesareattachedtotheunexposed
responsibility of the user of this standard to establish appro-
surface of the calorimeter.Aone-dimensional heat flow analy-
priate safety and health practices and determine the applica-
sis is used for calculating the heat transfer rate from the
bility of regulatory limitations prior to use.
temperature measurements. Applications include aerodynamic
heating, laser and radiation power measurements, and fire
2. Summary of Test Method
safety testing.
2.1 This test method for measuring the heat transfer rate to
1.2 Advantages:
a metal calorimeter of finite thickness is based on the assump-
1.2.1 Simplicity of Construction—The calorimeter may be
tion of one-dimensional heat flow, known metal properties
constructedfromanumberofmaterials.Thesizeandshapecan
(density and specific heat), known metal thickness, and mea-
often be made to match the actual application. Thermocouples
surement of the rate of temperature rise of the back (or
may be attached to the metal by spot, electron beam, or laser
unexposed) surface of the calorimeter.
welding.
1.2.2 Heat transfer rate distributions may be obtained if
2.2 After an initial transient, the response of the calorimeter
metals with low thermal conductivity, such as some stainless
is approximated by a lumped parameter analysis:
steels, are used.
dT
1.2.3 The calorimeters can be fabricated with smooth
q 5 ρC δ (1)
p
dτ
surfaces,withoutinsulatorsorplugsandtheattendanttempera-
ture discontinuities, to provide more realistic flow conditions
where:
for aerodynamic heating measurements.
q = heat transfer rate, W/m ,
1.2.4 The calorimeters described in this test method are
ρ = metal density, kg/m ,
relatively inexpensive. If necessary, they may be operated to
δ = metal thickness, m,
burn-out to obtain heat transfer information. C = metal specific heat, J/kg·K, and
p
dT/dτ = back surface temperature rise rate, K/s.
1.3 Limitations:
1.3.1 At higher heat flux levels, short test times are neces-
3. Significance and Use
sary to ensure calorimeter survival.
3.1 This test method may be used to measure the heat
1.3.2 For applications in wind tunnels or arc-jet facilities,
transfer rate to a metallic or coated metallic surface for a
the calorimeter must be operated at pressures and temperatures
variety of applications, including:
such that the thin-skin does not distort under pressure loads.
3.1.1 Measurements of aerodynamic heating when the calo-
Distortion of the surface will introduce measurement errors.
rimeter is placed into a flow environment, such as a wind
1.4 The values stated in SI units are to be regarded as
tunnel or an arc jet; the calorimeters can be designed to have
standard. No other units of measurement are included in this
the same size and shape as the actual test specimens to
standard.
minimize heat transfer corrections;
3.1.2 Heat transfer measurements in fires and fire safety
testing;
This test method is under the jurisdiction of ASTM Committee E21 on Space
Simulation andApplications of SpaceTechnology and is the direct responsibility of
3.1.3 Laser power and laser absorption measurements; as
Subcommittee E21.08 on Thermal Protection.
well as,
Current edition approved April 1, 2016. Published April 2016. Originally
3.1.4 X-ray and particle beam (electrons or ions) dosimetry
approved in 1972. Last previous edition approved in 2011 as E459–05(2011).
DOI: 10.1520/E0459-05R16. measurements.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States
E459 − 05 (2016)
FIG. 1 Typical Thin-Skin Calorimeter for Heat Transfer Measurement
3.2 The thin-skin calorimeter is one of many concepts used niques. This type of thermocouple joint (called an intrinsic
to measure heat transfer rates. It may be used to measure thermocouple) has been found to provide superior transient
convective, radiative, or combinations of convective and ra- response as compared to a peened joint or a beaded thermo-
diative (usually called mixed or total) heat transfer rates. couple that is soldered to the surface (1, 2). The wires should
However, when the calorimeter is used to measure radiative or be positioned approximately 1.6 mm apart along an expected
mixedheattransferrates,theabsorptivityandreflectivityofthe isotherm.Theuseofasmallthermocouplewireminimizesheat
surface should be measured over the expected radiation wave- conduction into the wire but the calorimeter should still be
length region of the source. ruggedenoughforrepeatedmeasurements.However,whenthe
thicknessofthecalorimeterisontheorderofthewirediameter
3.3 In 4.6 and 4.7, it is demonstrated that lateral heat
toobtainthenecessaryresponsecharacteristics,therecommen-
conduction effects on a local measurement can be minimized
dations of Sobolik, et al. [1989], Burnett [1961], and Kidd
by using a calorimeter material with a low thermal conductiv-
[1985] (2-4) should be followed.
ity.Alternatively, a distribution of the heat transfer rate may be
obtainedbyplacinganumberofthermocouplesalongtheback 4.2 Whenheatingstarts,theresponseoftheback(unheated)
surface of the calorimeter. surface of the calorimeter lags behind that of the front (heated)
surface. For a step change in the heat transfer rate, the initial
3.4 In high temperature or high heat transfer rate
response time of the calorimeter is the time required for the
applications, the principal drawback to the use of thin-skin
temperature rise rate of the unheated surface to approach the
calorimeters is the short exposure time necessary to ensure
temperature rise rate of the front surface within 1%. If
survival of the calorimeter such that repeat measurements can
conductionheattransferintothethermocouplewireisignored,
be made with the same sensor. When operation to burnout is
the initial response time is generally defined as:
necessary to obtain the desired heat flux measurements, thin-
ρC δ
skin calorimeters are often a good choice because they are
p
τ 5 0.5 (2)
r
relatively inexpensive to fabricate. k
where:
4. Apparatus
τ = initial response time, s, and
r
4.1 Calorimeter Design—Typicaldetailsofathin-skincalo-
rimeter used for measuring aerodynamic heat transfer rates are
shown in Fig. 1. The thermocouple wires (0.127 mm OD,
0.005 in., 36 gage) are individually welded to the back surface
The boldface numbers in parentheses refer to the list of references at the end of
of the calorimeter using spot, electron beam, or laser tech- this standard.
E459 − 05 (2016)
4.4 Determine the maximum exposure time (6) by setting a
k = thermal conductivity, W/m·K.
maximum allowable temperature for the front surface as
As an example, the 0.76 mm (0.030 in.) thick, 300 series
follows:
stainless steel calorimeter analyzed in Ref (4) has an initial
response time of 72 ms. Eq 2 can be rearranged to show that ρC δ k T 2 T 1
~ !
p max 0
τ 5 * 2 (4)
F G
max
the initial response time also corresponds to a Fourier Number
k qδ 3
(a dimensionless time) of 0.5.
where:
4.3 Conduction heat transfer into the thermocouple wire
τ = maximum exposure time, s,
max
delaysthetimepredictedbyEq2forwhichthemeasuredback
T = initial temperature, K, and
face temperature rise rate accurately follows (that is, within
T = maximum allowable temperature, K.
max
1%) the undisturbed back face temperature rise rate. For a
4.4.1 In order to have time available for the heat transfer
0.127 mm (0.005 in.) OD, Type K intrinsic thermocouple on a
rate measurement, τ must be greater thanτ , which requires
0.76 mm (0.030 in.) thick, 300 series stainless steel
max R
calorimeter, the analysis in Ref (4) indicates the measured that:
temperature rise rate is within 2% of the undisturbed tempera-
k~T 2 T ! 5
max 0
. (5)
ture rise rate in approximately 500 ms. An estimate of the
qδ 6
measured temperature rise rate error (or slope error) can be
obtained from Ref (1) for different material combinations:
4.4.2 Determine an optimum thickness that maximizes
(τ − τ ) (7) as follows:
max R
dT dT αt αt
C TC
2 5 C exp C erfcS C D (3)
S D Œ
1 2 2 2 2
3 k~T 2 T !
dt dt R R
max 0
δ 5 (6)
opt
5 q
where:
4.4.3 Then calculate the maximum exposure time using the
T = calorimeter temperature,
C
T = measured temperature (that is, thermocouple output),
optimum thickness as follows:
TC
C = β/(8/π + β) and C =4⁄(8⁄π + βπ),
1 2
T 2 T
max 0
α = k/ρC (thermaldiffusivityofthecalorimetermaterial),
τ 5 0.48ρC k (7)
p F G
maxopt p
q
β =
=
K/ A ,
4.4.4 When it is desirable for a calorimeter to cover a range
K = k of thermocouple wire/k of calorimeter,
of heat transfer rates without being operated to burn-out,
A = α of thermocouple wire/α of calorimeter,
design the calorimeter around the largest heat-transfer rate.
R = radius of the thermocouple wire, and
This gives the thinnest calorimeter with the shortest initial
t = time.
response time (Eq 2); however, Refs (2, 3, 8, 9) all show the
Using thermal property values given in Ref (4) for the
time to a given error level between the measured and undis-
Alumel (negative) leg of the Type K thermocouple on 300
turbed temperature rise rates (left hand side of Eq 3) increases
Series stainless steel (K=1.73, A=1.56, β=1.39), Eq 3 can
as the thickness of the calorimeter decreases relative to the
be used to show that the measured rate of temperature change
thermocouple wire diameter.
(that is, the slope) is within 5% of the actual rate of
temperaturechangeinapproximately150ms.Forthiscase,the
4.5 In most applications, the value of T should be well
max
time for a 1% error in the measured temperature rise rate is
below the melting temperature to obtain a satisfactory design.
roughly 50 times as long as the initial response time predicted
Limiting the maximum temperature to 700 K will keep
by Eq 2; this ratio depends on the thermophysical properties of
radiation losses below 15 kW/m . For a maximum temperature
the calorimeter and thermocouple materials (see Table 1).
rise (T − T ) of 400 K, Fig. 2 shows the optimum thickness
max 0
4.3.1 When the heat transfer rate varies with time, the
of copper and stainless steel calorimeters as a function of the
thin-skin calorimeter should be designed so the response times
heat-transfer rate.The maximum exposure time of an optimum
defined using Eq 2 and 3 are smaller than the time for
thickness calorimeter for a 400 K temperature rise is shown as
significant variations in the heat transfer rate. If this is not
a function of the heat-transfer rate in Fig. 3.
possible, methods for unfolding the dynamic measurement
errors (1,5) should be used to compensate the temperature
4.6 The one-dimensional heat flow assumption used in 2.2
measurements before calculating the heat flux using Eq 1.
and 4.3–4.4 is valid for a uniform heat-transfer rate; however,
in practice the calorimeter will generally have a heat-transfer
ratedistributionoverthesurface.Refs (9, 10)bothconsiderthe
TABLE 1 Time Required for Different Error Levels in the
effectsoflateralheatconductioninahemisphericalcalorimeter
Unexposed Surface Temperature Rise Rate
on heat transfer measurements in a supersonic stream. For a
Error Level Due to Heat
Conduction into 10% 5%2%1% cosine shaped heat flux distribution at the stagnation-point of
Thermocouple
the hemisphere, Starner gives the lateral conduction error
Negative Leg (Alumel) of 35 ms 150 ms 945 ms 3.8 s
relative to the surface heating as
Type K on 304 Stainless
Negative Leg (Constantan) <1 ms <1 ms 1 ms 4 ms
2αt 8kt
of Type T on Copper
E 5 5 (8)
C 2 2
L
R ρC D
p
E459 − 05 (2016)
FIG. 2 Calorimeter Optimum Material Thickness as a Function of Heat Transfer Rate and Material
where: approach for evaluation of the measured rate of temperature
change. The analysis was developed for laser experiments
E = relative heat-transfer rate ratio,
where only part of the calorimeter surface was exposed to
R = radius of curvature of the body (D/2), and
t = exposure time. heating and the exposure time was long compared to the
thermal penetration time to the edges of the unexposed area
Note the lateral conduction error described in Eq 8 is not a
(penetration time calculation is similar to Eq 2 with L, the
function of the calorimeter skin thickness or the heat-transfer
distance to the edge, substituted for δ, the thickness).
rate; the magnitude of the error is shown in Fig. 4 for copper
and stainless steel. The errors for most other base metal
4.9 A device for recording the thermocouple signals with
calorimeters will fall in between these two lines. While the time is required. The response time of an analog recording
lateral conduction errors can be minimized by using materials system should be an order of magnitude smaller than the
with low thermal diffusivity and short exposure times, these calorimeter response time (see Eq 2). The sampling time of a
mayaggravatesomeoftheotherconstraints,asdescribedinEq digital recording system should be no more than 40% of the
2 and 3. Ref (9) also describes the lateral conduction errors for calorimeter response time; the 3 db frequency of any low-pass
cones and cylinders. filters in the data acquisition system should be greater than
4.7 An approximation of the lateral conduction error can be 1 h
f . 5 (10)
3db
obtainedexperimentallybycontinuingtorecordtheunexposed 2πτ 2πρC δ
p
surface temperature after the heating is removed and calculat-
where:
ing the ratio of the rates of temperature change.
h = estimated heat transfer coefficient for the experiment.
dT
cool down
dt 5. Procedure
?
E; (9)
test
?
dT
5.1 Expose the thin-skin calorimeter to the thermal environ-
dt
ment as rapidly as practical. Operate the recording system for
4.8 When the average heat transfer rate over the exposed several seconds before the exposure to provide data for
area is desired, Wedekind and Beck [1989] (11) give another
evaluating any noise in the calorimeter and data acquisition
----------
...


This document is not an ASTM standard and is intended only to provide the user of an ASTM standard an indication of what changes have been made to the previous version. Because
it may not be technically possible to adequately depict all changes accurately, ASTM recommends that users consult prior editions as appropriate. In all cases only the current version
of the standard as published by ASTM is to be considered the official document.
Designation: E459 − 05 (Reapproved 2011) E459 − 05 (Reapproved 2016)
Standard Test Method for
Measuring Heat Transfer Rate Using a Thin-Skin
Calorimeter
This standard is issued under the fixed designation E459; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A
superscript epsilon (´) indicates an editorial change since the last revision or reapproval.
1. Scope
1.1 This test method covers the design and use of a thin metallic calorimeter for measuring heat transfer rate (also called heat
flux). Thermocouples are attached to the unexposed surface of the calorimeter. A one-dimensional heat flow analysis is used for
calculating the heat transfer rate from the temperature measurements. Applications include aerodynamic heating, laser and
radiation power measurements, and fire safety testing.
1.2 Advantages:
1.2.1 Simplicity of Construction—The calorimeter may be constructed from a number of materials. The size and shape can often
be made to match the actual application. Thermocouples may be attached to the metal by spot, electron beam, or laser welding.
1.2.2 Heat transfer rate distributions may be obtained if metals with low thermal conductivity, such as some stainless steels, are
used.
1.2.3 The calorimeters can be fabricated with smooth surfaces, without insulators or plugs and the attendant temperature
discontinuities, to provide more realistic flow conditions for aerodynamic heating measurements.
1.2.4 The calorimeters described in this test method are relatively inexpensive. If necessary, they may be operated to burn-out
to obtain heat transfer information.
1.3 Limitations:
1.3.1 At higher heat flux levels, short test times are necessary to ensure calorimeter survival.
1.3.2 For applications in wind tunnels or arc-jet facilities, the calorimeter must be operated at pressures and temperatures such
that the thin-skin does not distort under pressure loads. Distortion of the surface will introduce measurement errors.
1.4 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard.
1.4.1 Exception—The values given in parentheses are for information only.
1.5 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility
of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory
limitations prior to use.
2. Summary of Test Method
2.1 This test method for measuring the heat transfer rate to a metal calorimeter of finite thickness is based on the assumption
of one-dimensional heat flow, known metal properties (density and specific heat), known metal thickness, and measurement of the
rate of temperature rise of the back (or unexposed) surface of the calorimeter.
2.2 After an initial transient, the response of the calorimeter is approximated by a lumped parameter analysis:
dT
q 5 ρC δ (1)
p
dτ
where:
q = heat transfer rate, W/m ,
ρ = metal density, kg/m ,
δ = metal thickness, m,
C = metal specific heat, J/kg·K, and
p
This test method is under the jurisdiction of ASTM Committee E21 on Space Simulation and Applications of Space Technology and is the direct responsibility of
Subcommittee E21.08 on Thermal Protection.
Current edition approved Oct. 1, 2011April 1, 2016. Published April 2012April 2016. Originally approved in 1972. Last previous edition approved in 20052011 as
E459 – 05.E459 – 05 (2011). DOI: 10.1520/E0459-05R11.10.1520/E0459-05R16.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States
E459 − 05 (2016)
dT/dτ = back surface temperature rise rate, K/s.
3. Significance and Use
3.1 This test method may be used to measure the heat transfer rate to a metallic or coated metallic surface for a variety of
applications, including:
3.1.1 Measurements of aerodynamic heating when the calorimeter is placed into a flow environment, such as a wind tunnel or
an arc jet; the calorimeters can be designed to have the same size and shape as the actual test specimens to minimize heat transfer
corrections;
3.1.2 Heat transfer measurements in fires and fire safety testing;
3.1.3 Laser power and laser absorption measurements; as well as,
3.1.4 X-ray and particle beam (electrons or ions) dosimetry measurements.
3.2 The thin-skin calorimeter is one of many concepts used to measure heat transfer rates. It may be used to measure convective,
radiative, or combinations of convective and radiative (usually called mixed or total) heat transfer rates. However, when the
calorimeter is used to measure radiative or mixed heat transfer rates, the absorptivity and reflectivity of the surface should be
measured over the expected radiation wavelength region of the source.
3.3 In 4.6 and 4.7, it is demonstrated that lateral heat conduction effects on a local measurement can be minimized by using a
calorimeter material with a low thermal conductivity. Alternatively, a distribution of the heat transfer rate may be obtained by
placing a number of thermocouples along the back surface of the calorimeter.
3.4 In high temperature or high heat transfer rate applications, the principal drawback to the use of thin-skin calorimeters is the
short exposure time necessary to ensure survival of the calorimeter such that repeat measurements can be made with the same
sensor. When operation to burnout is necessary to obtain the desired heat flux measurements, thin-skin calorimeters are often a
good choice because they are relatively inexpensive to fabricate.
4. Apparatus
4.1 Calorimeter Design—Typical details of a thin-skin calorimeter used for measuring aerodynamic heat transfer rates are
shown in Fig. 1. The thermocouple wires (0.127 mm OD, 0.005 in., 36 gage) are individually welded to the back surface of the
calorimeter using spot, electron beam, or laser techniques. This type of thermocouple joint (called an intrinsic thermocouple) has
been found to provide superior transient response as compared to a peened joint or a beaded thermocouple that is soldered to the
FIG. 1 Typical Thin-Skin Calorimeter for Heat Transfer Measurement
E459 − 05 (2016)
surface (1, 2). The wires should be positioned approximately 1.6 mm apart along an expected isotherm. The use of a small
thermocouple wire minimizes heat conduction into the wire but the calorimeter should still be rugged enough for repeated
measurements. However, when the thickness of the calorimeter is on the order of the wire diameter to obtain the necessary response
characteristics, the recommendations of Sobolik, et al. [1989], Burnett [1961], and Kidd [1985] (2-4) should be followed.
4.2 When heating starts, the response of the back (unheated) surface of the calorimeter lags behind that of the front (heated)
surface. For a step change in the heat transfer rate, the initial response time of the calorimeter is the time required for the
temperature rise rate of the unheated surface to approach the temperature rise rate of the front surface within 1 %. If conduction
heat transfer into the thermocouple wire is ignored, the initial response time is generally defined as:
ρC δ
p
τ 5 0.5 (2)
r
k
where:
τ = initial response time, s, and
r
k = thermal conductivity, W/m·K.
4) has an initial response
As an example, the 0.76 mm (0.030 in.) thick, 300 series stainless steel calorimeter analyzed in Ref (
time of 72 ms. Eq 2 can be rearranged to show that the initial response time also corresponds to a Fourier Number (a dimensionless
time) of 0.5.
4.3 Conduction heat transfer into the thermocouple wire delays the time predicted by Eq 2 for which the measured back face
temperature rise rate accurately follows (that is, within 1 %) the undisturbed back face temperature rise rate. For a 0.127 mm (0.005
in.) OD, Type K intrinsic thermocouple on a 0.76 mm (0.030 in.) thick, 300 series stainless steel calorimeter, the analysis in Ref
(4) indicates the measured temperature rise rate is within 2 % of the undisturbed temperature rise rate in approximately 500 ms.
An estimate of the measured temperature rise rate error (or slope error) can be obtained from Ref (1) for different material
combinations:
dT dT αt αt
C TC
2 5 C exp C erfcS C D (3)
S D Œ
2 2
1 2 2
dt dt R R
where:
T = calorimeter temperature,
C
T = measured temperature (that is, thermocouple output),
TC
C = β/(8/π + β) and C = 4 ⁄(8 ⁄π + βπ),
1 2
α = k/ρC (thermal diffusivity of the calorimeter material),
p
β =
K/=A ,
K = k of thermocouple wire/k of calorimeter,
A = α of thermocouple wire/α of calorimeter,
R = radius of the thermocouple wire, and
t = time.
Using thermal property values given in Ref (4) for the Alumel (negative) leg of the Type K thermocouple on 300 Series stainless
steel (K = 1.73, A = 1.56, β = 1.39), Eq 3 can be used to show that the measured rate of temperature change (that is, the slope) is
within 5 % of the actual rate of temperature change in approximately 150 ms. For this case, the time for a 1 % error in the measured
temperature rise rate is roughly 50 times as long as the initial response time predicted by Eq 2; this ratio depends on the
thermophysical properties of the calorimeter and thermocouple materials (see Table 1).
4.3.1 When the heat transfer rate varies with time, the thin-skin calorimeter should be designed so the response times defined
using Eq 2 and 3 are smaller than the time for significant variations in the heat transfer rate. If this is not possible, methods for
unfolding the dynamic measurement errors (1,5) should be used to compensate the temperature measurements before calculating
the heat flux using Eq 1.
The boldface numbers in parentheses refer to the list of references at the end of this standard.
TABLE 1 Time Required for Different Error Levels in the
Unexposed Surface Temperature Rise Rate
Error Level Due to Heat
Conduction into 10 % 5 % 2 % 1 %
Thermocouple
Negative Leg (Alumel) of 35 ms 150 ms 945 ms 3.8 s
Type K on 304 Stainless
Negative Leg (Constantan) <1 ms <1 ms 1 ms 4 ms
of Type T on Copper
E459 − 05 (2016)
4.4 Determine the maximum exposure time (6) by setting a maximum allowable temperature for the front surface as follows:
ρC δ k~T 2 T ! 1
p max 0
τ 5 * 2 (4)
F G
max
k qδ 3
where:
τ = maximum exposure time, s,
max
T = initial temperature, K, and
T = maximum allowable temperature, K.
max
4.4.1 In order to have time available for the heat transfer rate measurement, τ must be greater thanτ , which requires that:
max R
k~T 2 T ! 5
max 0
. (5)
qδ 6
4.4.2 Determine an optimum thickness that maximizes (τ − τ ) (7) as follows:
max R
3 k T 2 T
~ !
max 0
δ 5 (6)
opt
5 q
4.4.3 Then calculate the maximum exposure time using the optimum thickness as follows:
T 2 T
max 0
τ 5 0.48ρC k (7)
F G
maxopt p
q
4.4.4 When it is desirable for a calorimeter to cover a range of heat transfer rates without being operated to burn-out, design
the calorimeter around the largest heat-transfer rate. This gives the thinnest calorimeter with the shortest initial response time (Eq
2); however, Refs (2, 3, 8, 9) all show the time to a given error level between the measured and undisturbed temperature rise rates
(left hand side of Eq 3) increases as the thickness of the calorimeter decreases relative to the thermocouple wire diameter.
4.5 In most applications, the value of T should be well below the melting temperature to obtain a satisfactory design.
max
Limiting the maximum temperature to 700 K will keep radiation losses below 15 kW/m . For a maximum temperature rise
(T − T ) of 400 K, Fig. 2 shows the optimum thickness of copper and stainless steel calorimeters as a function of the
max 0
heat-transfer rate. The maximum exposure time of an optimum thickness calorimeter for a 400 K temperature rise is shown as a
function of the heat-transfer rate in Fig. 3.
4.6 The one-dimensional heat flow assumption used in 2.2 and 4.3–4.4 is valid for a uniform heat-transfer rate; however, in
practice the calorimeter will generally have a heat-transfer rate distribution over the surface. Refs (9, 10) both consider the effects
of lateral heat conduction in a hemispherical calorimeter on heat transfer measurements in a supersonic stream. For a cosine shaped
heat flux distribution at the stagnation-point of the hemisphere, Starner gives the lateral conduction error relative to the surface
heating as
2αt 8kt
E 5 5 (8)
C 2 2
L
R ρC D
p
where:
E = relative heat-transfer rate ratio,
R = radius of curvature of the body (D/2), and
t = exposure time.
Note the lateral conduction error described in Eq 8 is not a function of the calorimeter skin thickness or the heat-transfer rate;
the magnitude of the error is shown in Fig. 4 for copper and stainless steel. The errors for most other base metal calorimeters will
fall in between these two lines. While the lateral conduction errors can be minimized by using materials with low thermal
diffusivity and short exposure times, these may aggravate some of the other constraints, as described in Eq 2 and 3. Ref (9) also
describes the lateral conduction errors for cones and cylinders.
4.7 An approximation of the lateral conduction error can be obtained experimentally by continuing to record the unexposed
surface temperature after the heating is removed and calculating the ratio of the rates of temperature change.
dT
cool down
dt
?
E; (9)
test
?
dT
dt
4.8 When the average heat transfer rate over the exposed area is desired, Wedekind and Beck [1989] (11) give another approach
for evaluation of the measured rate of temperature change. The analysis was developed for laser experiments where only part of
the calorimeter surface was exposed to heating and the exposure time was long compared to the thermal penetration time to the
edges of the unexposed area (penetration time calculation is similar to Eq 2 with L, the distance to the edge, substituted for δ, the
thickness).
E459 − 05 (2016)
FIG. 2 Calorimeter Optimum Material Thickness as a Function of Heat Transfer Rate and Material
4.9 A device for recording the thermocouple signals with time is required. The response time of an analog recording system
should be an order of magnitude smaller than the calorimeter response
...

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