ASTM D3364-99(2019)
(Test Method)Standard Test Method for Flow Rates for Poly(Vinyl Chloride) with Molecular Structural Implications
Standard Test Method for Flow Rates for Poly(Vinyl Chloride) with Molecular Structural Implications
SIGNIFICANCE AND USE
5.1 This test method is useful for quality-control tests on PVC compounds having a wide range of melt viscosities. Measurements are made at shear rates close to 1 s−1.
5.2 In addition to the properties mentioned in Test Method D1238, this technique is sensitive to plasticizer content, polymer molecular weight, polymer stability (both thermally and rheologically), shear instability, and general composition. The sensitivity of the material to temperature necessitates slightly tighter controls than those stated in Test Method D1238.
5.3 The sensitivity of this test method makes it useful for correlating with processing conditions and as an aid in predicting changes in processing. However, as a one-point measure of flow relative to shear rate, its one drawback is that the same PVC melt flow values can be obtained for materials having different processibility; the chance of this happening is minimized, however, if the compounds are similar in composition.
5.4 Correlations with a wide range of processing conditions have supported the conclusions that little or no change in composition occurs during the test. Thus, this test is able to detect and follow profound changes which occur during extrusion, injection molding, milling, or mixing. These changes are due to three types of measured instability in polymers:
5.4.1 Thermal instability due to temperature effect.
5.4.2 Shear instability due to breaking of polymer bonds.
5.4.3 Rheological instability due to nonuniform distributions of widely different viscosity or molecular weight elements.
5.4.4 Thus, implications with respect to PVC molecular structural changes can be detected and predicted.
SCOPE
1.1 This test method is an extension of Test Method D1238 specific to the measurement of flow rates of poly(vinyl chloride) (PVC) compounds while detecting and controlling various polymer instabilities associated with the flow rate.
1.2 The values stated in SI units are to be regarded as standard. The values given in parentheses are mathematical conversions to inch-pound units that are provided for information only and are not considered standard.
1.3 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, health, and environmental practices and determine the applicability of regulatory limitations prior to use.
Note 1: There is no known ISO equivalent to this standard.
1.4 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
General Information
Relations
Standards Content (Sample)
This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the
Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
Designation: D3364 − 99 (Reapproved 2019)
Standard Test Method for
Flow Rates for Poly(Vinyl Chloride) with Molecular
Structural Implications
This standard is issued under the fixed designation D3364; 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 Determine the Precision of a Test Method
1.1 This test method is an extension of Test Method D1238
3. Terminology
specific to the measurement of flow rates of poly(vinyl
3.1 Definitions—For definitions related to plastics, see Ter-
chloride) (PVC) compounds while detecting and controlling
minology D883.
various polymer instabilities associated with the flow rate.
3.2 Definitions of Terms Specific to This Standard:
1.2 The values stated in SI units are to be regarded as
3.2.1 See Test Method D3835, Sections 5.1, 5.2, and 5.3.
standard. The values given in parentheses are mathematical
3.2.2 Flow is the reciprocal of the viscosity; therefore, the
conversions to inch-pound units that are provided for informa-
flow is defined as the volumetric displacement through a
tion only and are not considered standard.
controlled orifice and is expressed as shear rate over shear
1.3 This standard does not purport to address all of the
stress.
safety concerns, if any, associated with its use. It is the
NOTE 2—Since PVC obeys the power law function, the above relation-
responsibility of the user of this standard to establish appro-
ship can be expressed as follows:
priate safety, health, and environmental practices and deter-
1−N
(Viscosity) (Shear Rate) =(shear stress) in which the shear rate is
mine the applicability of regulatory limitations prior to use. 3
expressed as 4Q/πR and depends on the power law exponent N.
Since Qisthevolumetricflowrateintermsofcubicmillimetres/second
NOTE 1—There is no known ISO equivalent to this standard.
and R is the radius of the die, it follows that the flow rate varies much
1.4 This international standard was developed in accor-
faster than the viscosity as a result of N.This means that the flow is much
more sensitive to change than the viscosity. For PVC, N varies from 0.1
dance with internationally recognized principles on standard-
to 0.33.
ization established in the Decision on Principles for the
Development of International Standards, Guides and Recom- 3.2.3 Flow rate by this test method is the rate in milligrams/
mendations issued by the World Trade Organization Technical
minute at which polymer flows through a specific die (see Fig.
Barriers to Trade (TBT) Committee.
1) with a total load on the ram of 20 kg at a temperature of
175°C.
2. Referenced Documents
4. Summary of Test Method
2.1 ASTM Standards:
4.1 Conditions:
D883Terminology Relating to Plastics
4.1.1 In order to test a wide variation of flow rates covering
D1238Test Method for Melt Flow Rates of Thermoplastics
semirigid as well as nonrigid PVC compounds, the following
by Extrusion Plastometer
standard conditions are used:
D3835Test Method for Determination of Properties of
Temperature 175°C (347°F)
Polymeric Materials by Means of a Capillary Rheometer
Total load on piston 20 000 g
E177Practice for Use of the Terms Precision and Bias in
Approximate pressure 2758 kPa (400 psi)
ASTM Test Methods
Charge 2.15 ± 0.05 g
E691Practice for Conducting an Interlaboratory Study to Plugged orifice with 120° entrance angle
4.2 Basis Principles:
4.2.1 Thelowertemperature(relativeto190°C)ischosento
ThistestmethodisunderthejurisdictionofASTMCommitteeD20onPlastics
minimize thermal decomposition, maximize sensitivity of the
and is the direct responsibility of Subcommittee D20.30 on Thermal Properties.
flow rate to structural changes in the PVC compound, and to
Current edition approved May 1, 2019. Published May 2019. Originally
allow a wide latitude of useful conditions associated with the
approved in 1974. Last previous edition approved in 2011 as D3364-99 (2011).
DOI: 10.1520/D3364-99R19.
load on the piston.
For referenced ASTM standards, visit the ASTM website, www.astm.org, or
4.2.2 Modern extrusion plastometers have been redesigned
contact ASTM Customer Service at service@astm.org. For Annual Book of ASTM
to accommodate much higher loads. Current research for
Standards volume information, refer to the standard’s Document Summary page on
the ASTM website. multi-weight testing has reached levels of 50 kg and these are
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States
D3364 − 99 (2019)
NOTE 1—Specify material when ordering.
FIG. 1 Die Used for Test Method D3364
particularlygoodforrigidPVC.Previously,flowratesforrigid flow relative to shear rate, its one drawback is that the same
PVC were limited to 190°C. Recent research has shown that PVC melt flow values can be obtained for materials having
rigid PVC can be run at 150°C and 50 kg loads.This weight is different processibility; the chance of this happening is
effective for all semirigid PVC and even some nonrigid minimized, however, if the compounds are similar in compo-
compounds. For flow rates in excess of 10 g/10 min (1000 sition.
mg/min), lower weights are used, for example, color concen-
5.4 Correlations with a wide range of processing conditions
trates used in PVC extrusion may have flow rates in excess of
have supported the conclusions that little or no change in
100g/10min(10 000mg/min)andwillrequirea5-kgloadon
composition occurs during the test. Thus, this test is able to
the piston.
detect and follow profound changes which occur during
4.2.3 When the flow rates become very small as in the case
extrusion, injection molding, milling, or mixing. These
of the stiffest semirigid containing 25 parts of plasticizer (flow
changes are due to three types of measured instability in
rates below 15 mg/min), it may be desirable to use the die (flat
polymers:
entry 8 mm (0.315 in.) long) in Test Method D1238. The flow
5.4.1 Thermal instability due to temperature effect.
is so slow that little rheological instability exists. By changing
5.4.2 Shear instability due to breaking of polymer bonds.
the die, approximately a tenfold increase in flow is achieved.
5.4.3 Rheological instability due to nonuniform distribu-
4.2.4 The charge size is important. Many PVC compounds
tions of widely different viscosity or molecular weight ele-
are elastic in nature, causing a severe loss in pressure from the
ments.
bottom of the piston through the material to the orifice of the
5.4.4 Thus, implications with respect to PVC molecular
die. Evidence indicates that the force to extrude may be
structural changes can be detected and predicted.
reduced by as much as 67% using a 9-g charge and 4.14 MPa
(600 psi) on the piston.
6. Apparatus
4.2.5 The plugged orifice should be used in all PVC
6.1 Plastometer—The apparatus is identical to that used in
compound work since the amount of charge is limited and
Test Method D1238 except for the die.An alternative thermo-
since the plugging for various times has been observed to give
regulator is suggested for improved temperature control.
significant variations in the flow rate.
6.2 Die:
5. Significance and Use
6.2.1 Thedieisapproximatelythreetimesaslongastheone
used in Test Method D1238, a major factor in controlling any
5.1 This test method is useful for quality-control tests on
rheological instability in the polymer. If instability still occurs,
PVC compounds having a wide range of melt viscosities.
−1
particularly at high flow rates, dies 2 in. or longer can be used
Measurements are made at shear rates close to 1 s .
toimprovethe L/Dratio.Thedimensionsoftheregulardieare
5.2 In addition to the properties mentioned in Test Method
shown in Fig. 1.
D1238, this technique is sensitive to plasticizer content,
6.3 Thermoregulator—Although a thermoregulator identi-
polymer molecular weight, polymer stability (both thermally
cal to that used in Test Method D1238 may be used (provided
and rheologically), shear instability, and general composition.
it regulates to 175 6 0.1°C), a unit coupled with a 90° angle
The sensitivity of the material to temperature necessitates
thermometer, divided into 0.1°C is suggested for improved
slightly tighter controls than those stated in Test Method
D1238.
5.3 The sensitivity of this test method makes it useful for
The “Thermo Watch” unit, manufactured by Instruments for Research and
correlating with processing conditions and as an aid in predict-
Industry, 103 FranklinAve., Cheltenham, PA19012, has been found satisfactory for
ingchangesinprocessing.However,asaone-pointmeasureof this purpose.
D3364 − 99 (2019)
TABLE 1 Time Requirements for Cutting Specimens TABLE 2 Measurement Conversion to Milligrams per Minute
Flow Rate Factor for Obtaining Flow Rate
Time Interval Time Interval, min
Range, in mg/min Multiply By
Between Cuts Typical Type
mg/min 4 0.25
15 to 30 4 min semirigid 2 0.50
30 to 50 2 min semirigid 1 1.00
50 to 100 1 min semirigid
0.50 (30 s) 2.00
100 to 500 30 s nonrigid 0.25 (15 s) 4.00
400 to 1500 15 s nonrigid 0.167 (10 s) 6.00
1000 to 2000 10 s soft
7.12 Weigh and record the results to the closest 1 mg.
reproducibility. Most regulators designed for Test Method
Average the five successive most stable values near the end of
D1238 cannot control better than 60.2°C. The sensitivity of
the run and express as milligrams per minute. This average
this test m
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