Designation: F1249 – 06 (Reapproved 2011)
Standard Test Method for
Water Vapor Transmission Rate Through Plastic Film and
Sheeting Using a Modulated Infrared Sensor1
This standard is issued under the fixed designation F1249; 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 a procedure for determining the
rate of water vapor transmission through flexible barrier
materials. The method is applicable to sheets and films up to 3
mm (0.1 in.) in thickness, consisting of single or multilayer
synthetic or natural polymers and foils, including coated
materials. It provides for the determination of (1) water vapor
transmission rate (WVTR), (2) the permeance of the film to
water vapor, and (3) for homogeneous materials, water vapor
permeability coefficient.
NOTE 1—Values for water vapor permeance and water vapor perme-
ability must be used with caution. The inverse relationship of WVTR to
thickness and the direct relationship of WVTR to the partial pressure
differential of water vapor may not always apply.
1.2 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 appro-
priate safety and health practices and determine the applica-
bility of regulatory limitations prior to use.
2. Referenced Documents
2.1 ASTM Standards:2
D374 Test Methods for Thickness of Solid Electrical Insu-
lation
D1898 Practice for Sampling of Plastics3
E96/E96M Test Methods for Water Vapor Transmission of
Materials
E104 Practice for Maintaining Constant Relative Humidity
by Means of Aqueous Solutions
E178 Practice for Dealing With Outlying Observations
E691 Practice for Conducting an Interlaboratory Study to
Determine the Precision of a Test Method
3. Terminology
3.1 Definitions:
3.1.1 water vapor permeability coeffıcient—the product of
the permeance and the thickness of the film. The permeability
is meaningful only for homogeneous materials, in which case
it is a property characteristic of bulk material.
3.1.1.1 Discussion—This quantity should not be used unless
the relationship between thickness and permeance has been
verified in tests using several thicknesses of the material. An
accepted unit of permeability is the metric perm centimeter, or
1 g/m2 per day per mm Hg·cm of thickness. The SI unit is the
mol/m2·s·Pa·mm. The test conditions (see 3.1) must be stated.
3.1.2 water vapor permeance—the ratio of a barrier’s
WVTR to the vapor pressure difference between the two
surfaces.
3.1.2.1 Discussion—An accepted unit of permeance is the
metric perm, or 1 g/m2 per day per mm Hg. The SI unit is the
mol/m2·s·Pa. Since the permeance of a specimen is generally a
function of relative humidity and temperature, the test condi-
tions must be stated.
3.1.3 water vapor transmission rate (WVTR)—the time rate
of water vapor flow normal to the surfaces, under steady-state
conditions, per unit area.
3.1.3.1 Discussion—An accepted unit of WVTR is g/m2 per
day. The test conditions of relative humidity and temperature
where the humidity is the difference in relative humidity across
the specimens, must be stated.
4. Summary of Test Method
4.1 A dry chamber is separated from a wet chamber of
known temperature and humidity by the barrier material to be
tested. The dry chamber and the wet chamber make up a
diffusion cell in which the test film is sealed. Water vapor
diffusing through the film mixes with the gas in the dry
chamber and is carried to a pressure-modulated infrared sensor.
This sensor measures the fraction of infrared energy absorbed
by the water vapor and produces an electrical signal, the
amplitude of which is proportional to water vapor concentra-
tion. The amplitude of the electrical signal produced by the test
1 This test method is under the jurisdiction of ASTM Committee F02 on Flexible
Barrier Packaging and is the direct responsibility of Subcommittee F02.10 on
Permeation.
Current edition approved Aug. 1, 2011. Published November 2011. Originally
approved in 1989. Last previous edition approved in 2006 as F1249 – 06. DOI:
10.1520/F1249-06R11.
2 For referenced ASTM standards, visit the ASTM website, www.astm.org, or
contact ASTM Customer Service at service@astm.org. For Annual Book of ASTM
Standards volume information, refer to the standard’s Document Summary page on
the ASTM website.
3 Withdrawn. The last approved version of this historical standard is referenced
on www.astm.org.
1
Copyright © ASTM International, 100 Barr Harbour Dr. P.O. box C-700, West Conshohocken, Pennsylvania 19428-2959, United States
film is then compared to the signal produced by measurement
of a calibration film of known water vapor transmission rate.
This information is then used to calculate the rate at which
moisture is transmitted through the material being tested.
5. Significance and Use
5.1 The purpose of this test method is to obtain reliable
values for the WVTR of plastic film and sheeting.
5.2 WVTR is an important property of packaging materials
and can be directly related to shelf life and packaged product
stability.
5.3 Data from this test method is suitable as a referee
method of testing, provided that the purchaser and seller have
agreed on sampling procedures, standardization procedures,
test conditions, and acceptance criteria.
6. Apparatus
6.1 This method utilizes water vapor transmission appara-
tus4 (Fig. 1) comprised of the following:
6.1.1 Diffusion Cell—An assembly consisting of two metal
halves which, when closed upon the test specimen, will
accurately define a circular area. A typical acceptable diffusion
cell area is 50 cm2. The volume enclosed by each cell half,
when clamped, is not critical; it should be small enough to
allow for rapid gas exchange, but not so small that an
unsupported film that happens to sag or buckle will contact the
top or bottom of the cell. A depth of approximately 6 mm
(0.250 in.) has been found to be satisfactory for 50-cm2 cells.
6.1.1.1 Diffusion Cell O–Ring—An appropriately sized
groove machined into the humid chamber side of the diffusion
cell retains a neoprene O–ring. The test area is considered to be
the area established by the inside contact diameter of the
compressed O–ring when the diffusion cell is clamped shut
against the test specimen.
6.1.1.2 Diffusion Cell Sealing Surface—A flat rim around
the dry side of the diffusion cell. This is a critical sealing
surface against which the test specimen is pressed; it shall be
smooth and without radial scratches.
6.1.1.3 Diffusion Cell Air Passages—Two holes in the dry
half of the diffusion cell. This is necessary only in the earlier
model WVTR instruments that have a separate conditioning
rack and testing chamber. These shall incorporate O–rings
suitable for sealing the diffusion cell to the test chamber
pneumatic fittings for the introduction and exhaust of air
without significant loss or leakage.
NOTE 2—Use of Multiple Diffusion Cells—Experience has shown that
arrangements using multiple diffusion cells are a practical way to increase
the number of measurements that can be obtained in a given time. A
separate conditioning rack (Fig. 2) may be used that contains a manifold
which connects the dry-chamber side of each individual diffusion cell to
a dry-air source. Dry air is continually purging the dry chamber of those
cells that are connected to the conditioning rack while the humid chamber
side is held at a specific relative humidity by distilled water or a
saturated-salt solution. It is desirable to thermostatically control the
temperature of the conditioning rack as described in 6.1.3.
6.1.2 Test Chamber—A cavity into which the diffusion cell
is inserted. Again, this is necessary only in the earlier model
WVTR instruments that have a separate conditioning rack and
testing chamber. The test chamber shall incorporate means for
clamping the diffusion cell in accurate registration with pneu-
matic system openings to the dry-air source and the infrared
detector. The chamber shall also provide a thermometer well
for the measurement of temperature.
6.1.3 Diffusion Cell Temperature Control—It is desirable to
thermostatically control the temperature of the diffusion cell to
within 61°F. A simple resistive heater attached to the station in
such a manner as to ensure good thermal contact is adequate
for this purpose. A thermistor sensor and an appropriate control
circuit will serve to regulate the temperature unless measure-
ments are being made close to ambient temperature. In that
case it may be necessary to provide cooling coils to remove
some of the heat.
6.1.4 Flowmeter—A means for regulating the flow of dry
air within an operating range of 5 to 100 cc/min is required.
6.1.5 Flow-Switching Valves, for the switching of dry-gas
flow streams of the water vapor transmission apparatus.
4 The sole source of supply of the apparatus known to the committee at this time
is Mocon/Modern Controls, Inc., 7500 Boone Avenue North, Minneapolis, MN
55428. If you are aware of alternative suppliers, please provide this information to
ASTM International Headquarters. Your comments will receive careful consider-
ation at a meeting of the responsible technical committee,1 which you may attend.
FIG. 1 Measuring System
FIG. 2 Conditioning System
F1249 – 06 (2011)
2
6.1.6 Infrared Sensor—A water vapor detector capable of
sensing 1 µg/L of water, or, in other terms, 1 ppm by volume,
or 0.002 % relative humidity at 37.8°C.
6.1.7 Recording Device—A multirange strip chart recorder
or other appropriate instrument for measuring the voltage
developed by the signal amplifier.
6.1.8 Desiccant Drying System, shall be capable of reducing
the concentration of water vapor in the gas source down to less
than 0.5 ppm by volume or 0.001 % relative humidity at
37.8°C. In earlier model WVTR equipment, a separate desic-
cant drying system is needed for the conditioning rack and test
chamber.
6.1.9 Flow-Metering Valve—A fine-metering valve capable
of controlling the dry-gas flow rate to the test cell when the
apparatus is in the “measure’’ mode of operation.
7. Reagents and Materials
7.1 Desiccant,4,5 for drying gas stream.
7.2 Absorbent Pads (not critical), such as filter pads of 30
to 75 mm in diameter. Necessary only in earlier model WVTR
equipment that utilizes distilled water or saturated salt solu-
tions to generate the desired relative humidity.
7.3 Distilled Water, for producing 100 % relative humidity,
or various saturated salt solutions to produce other relative
humidities as described in Practice E104. Newer WVTR
equipment does not require saturated salt solutions. Refer to
the manufacturer’s instructions for generating relative humid-
ity.
7.4 Reference Film, known WVTR material for system
calibration.
7.5 Sealing Grease, a high-viscosity, silicone stopcock
grease or other suitable high-vacuum grease is required for
lubrication of O–rings and to seal the specimen film in the
diffusion cell.
7.6 Nitrogen Gas, shall be dry and contain not less than
99.5 % nitrogen. Needed only with certain WVTR instruments.
8. Sampling
8.1 Select material for testing in accordance with standard
methods of sampling applicable to the material under test.
Sampling may be done in accordance with Practice D1898.
Select samples considered representative of the material to be
tested. If the material is of nonsymmetrical construction, the
orientation should be noted.
9. System Calibration With Reference Film
9.1 Follow the manufacturer’s instructions for calibrating
the WVTR instrument with a reference film.
10. Test Procedure
10.1 Preparation of Apparatus (Fig. 1)—If preceding tests
have exposed the apparatus to high moisture levels, outgas the
system to desorb residual moisture.
10.2 Number of Specimens Tested—Test enough specimens
to characterize package permeation rates but never less than
three per sample.
10.3 Preparation of Test Samples:
10.3.1 Cut the test specimen to approximately 10 cm by 10
cm (4 in. by 4 in.).
10.3.2 Measure specimen thickness at four equally spaced
points within the test area and at the center in accordance with
guidelines described in Test Method D374.
10.3.3 Lightly grease the cell sealing surface and the cell
O–ring.
10.3.4 For earlier model WVTR systems that require the use
of distilled water or saturated salt solutions, insert one to three
absorbent pads into the lower half-cell and dampen with
distilled water or a desired salt solution. Otherwise, for newer
WVTR instruments, follow the manufacturer’s instructions for
generating the desired relative humidity.
10.3.5 Affix the test film to the diffusion cell following the
manufacturer’s instructions. Fig. 3 shows the type of diffusion
cell used in earlier model WVTR equipment that consisted of
a separate conditioning rack and testing chamber. Diffusion
cells in newer WVTR equipment are similar to the lower half
of the cell displayed in Fig. 3.
10.3.6 If using a separate conditioning rack, clamp the
assembled cell in the conditioning rack. Allow the film to
condition in the diffusion cell until steady state has been
attained. If unfamiliar with the material being tested, the
operator should investigate the effect of conditioning time to be
certain that sufficient time has been allowed for the material to
equilibrate under the test conditions (see Note 3).
10.4 Measure the WVTR of the film specimen following the
manufacturer’s instructions.
NOTE 3—When testing materials for which the operator has no previous
history, additional time must be allowed to assure that true equilibrium has
been reached. When in doubt, retest after an additional conditioning
interval of several hours.
10.5 Record temperature of each test with reference to a
thermometer or thermocouple installed in the test chamber
thermometer well. Temperature is a critical parameter affecting
the measurement of WVTR. During testing, monitor the
temperature, periodically, to the nearest 0.5°C. Report the
average temperature and the range of temperatures observed
during the test.
10.6 Standby and Shutoff Procedures:
10.6.1 Follow the manufacturer’s instructions for putting
the instrument in standby when not being used.
5 Linde Molecular Sieve, Type 4A or Type 5A, in the form of 1⁄8 in. pellets as may
be obtained from the Union Carbide Co., Linde Division, Danbury, CT 06817-0001.
FIG. 3 Film Diffusion Cell
F1249 – 06 (2011)
3
10.6.2 When the system is not to be used for an extended
period and there are no films that require conditioning, the
electrical power may be turned off.
11. Calculation
11.1 WVTR—If using a recorder, calculate water vapor
transmission rate using the formula:
WVTR 5 C ~ES 2 EO!
where:
C = a calibration factor expressing rate as a function of
voltage (or mV). The value of C is derived from tests
of a known reference film (Section 9),
EO = permeation system zero level voltage, and
ES = equilibrium voltage obtained with the test specimen.
Newer computer-controlled systems will automatically cal-
culate the WVTR.
11.2 Permeance—Calculate sample permeance (if required)
using the following relationship:
Metric Perms 5
WVTR
Pw
5 g/m2 · day · mm Hg
where:
WVTR = Specimen water vapor transmission rate, g/m2·d,
and
Pw = Water vapor partial pressure gradient across the
test specimen, mmHg.
11.3 Permeability Coeffıcient—Calculate the water vapor
permeability coefficient (if required) using the following rela-
tionship:
Permeability 5 metric perms · t
where:
t = the average thickness of the specimen, mm. Note:
Permeability calculations are meaningful only in cases
where materials have been determined to be homoge-
neous.
12. Report
12.1 Report the following information:
12.1.1 A description of the test specimen. If the material is
nonsymmetrical (two sides different), include a statement as to
which side was facing the high humidity,
12.1.2 The humidity environment on each side of the test
film and means by which it was obtained,
12.1.3 The test temperature (to nearest 0.5°C),
12.1.4 The values of WVTR and, if desired, values of
permeance and permeability. These entries should be rounded
off to three significant figures or less, as may be consistent with
the operator’s estimate of precision or bias,
12.1.5 A statement of the means used to obtain the calibra-
tion factor,
12.1.6 The effective area exposed to permeation and a
description of how it was defined,
12.1.7 The time to reach steady-state after introduction of
the diffusion cell into the test chamber, and
12.1.8 A description of the conditioning procedure.
13. Precision and Bias
13.1 Precision:
13.1.1 Four different film materials cut and distributed in
accordance with Practice E691 were evaluated by eight labo-
ratories. The number of laboratories and materials in this study
does not meet the minimum requirements for determining
precision prescribed in Practice E691. Of the total eight
laboratories that participated in this round robin, one did not
report results for the PET sample. Due to equipment limita-
tions, only five laboratories were able to measure the water
vapor transmission rate of the EVOH material. Of these five
labs, the data from two laboratories were determined to be
outliers in accordance with Practice E178. In addition, due to
the type of equipment used, two of the laboratories participat-
ing in the round robin actually measured all of the samples at
90 % RH and converted the results to 100 % RH driving force
by multiplying by 1.11.
Precision, characterized by repeatability Sr and r, and repro-
ducibility SR and R, has been determined for the following
materials to be:
Materials No. of Labs Average† Sr SR r R
PET 7 14.0 0.3 2.0 0.8 5.7
PE 8 29.8 2.3 4.6 6.3 12.9
EVOH 3 239.6 26.7 177.6 74.7 497.3
PP 8 4.1 0.2 0.6 0.5 1.7
† Editorially corrected.
13.2 Bias—Measured values are derived from comparisons
with known-value reference films. The accuracy of this method
is therefore dependent upon the validity of the values assigned
to these reference films. This information should be available
from the manufacturer of the reference films.
F1249 – 06 (2011)
4
APPENDIX
(Nonmandatory Information)
X1. TESTING POOR BARRIERS
X1.1 Normal procedures as described for the modulated
infrared permeation system are considered suitable for testing
barrier materials having rates up to 100 g/m2–day. Above that
level, a different approach may be required in order to keep the
sensor output within design limits.
X1.2 In general, the testing of a “high transmitter” requires
that means be employed to reduce the concentration of water
vapor in the sensor. This may be accomplished in two ways:
X1.2.1 By increasing the flow of dry gas (possible in earlier
model WVTR equipment), or
X1.2.2 By reducing the area of the test film.
X1.3 Alternatively, apply foil masks with die-cut apertures.
These may be applied to both sides of a barrier to reduce the
sample area. Metal masks utilizing a neoprene O-ring are yet
another alternative.
X1.4 Each of these methods, when used alone or in
combination, serves to reduce the vapor concentration of the
air stream.
NOTE X1.1—The precision and bias of results obtained with reduced-
area masked samples has not been established.
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in this standard. Users of this standard are expressly advised that determination of the validity of any such patent rights, and the risk
of infringement of such rights, are entirely their own responsibility.
This standard is subject to revision at any time by the responsible technical committee and must be rev
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