26 An alternative approach to the evaluation of the slow crack growth resistance of polyethylene resins used for water pipe extrusion.pdf

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J Polym Res (2007) 14:181-189
DOI 10.1007/s10965-006-9095-1
An alternative approach to the evaluation of the slow crack
growth resistance of polyethylene resins used for water
pipe extrusion
Fabiano Moreno Peres
·
Cláudio Geraldo Schön
Received: 8 August 2006 / Accepted: 25 November 2006 / Published online: 23 January 2007
© Springer Science + Business Media B.V. 2007
Abstract High-density polyethylene (HDPE) pipes
have been largely employed in water and gas distrib-
ution systems. In spite of offering significative advan-
tages over other materials, HDPE pipes suffer from
premature failures due to creep fracture. The current
industrial criterium for design and sizing of HDPE
pipes is discussed. The concept of ‘regression curve,’
i.e. of a time-to-failure criterium based in long-term-
hydrostatic strength (LTHS) tests, is criticised and
concluded to be unsatisfactory for this purpose. An
alternative approach is suggested, which is based on
shorter-term tests. This is illustrated by testing five
HDPE resins designed for pipe extrusion and com-
paring with their standard ‘regression curves’. The
obtained results are consistent with the ‘regression
curve’-based analysis, justifying the use of the alterna-
tive approach in the industry.
Introduction
High-density polyethylene (HDPE) is currently used
for the production of plastic pipes for water and gas
distribution systems. This material offers several advan-
tages over its competitors, like flexibility, low cost, en-
vironmental attack resistance and ease of installation.
HDPE pipes for water distribution systems are, in prin-
ciple, designed for long lifetimes in service: current life-
times specified by industrial standards are expected to
be of the order of 50 years [ 1 , 2 ]. In spite of this, HDPE
pipes are known to be subject to premature in-service
failures due to time-dependent (creep) fracture, which
leads to leakage and, consequently, to environmental
and economic costs (water losses and increased main-
tenance costs). The search for improved materials leads
the petrochemical industry to continuous development
of new HDPE resins. Strategies such as increase in
the molecular mass, copolymerization (chain branch-
ing) and molecular mass distribution engineering have
been suggested to improve resistance to failure [ 2 , 3 ],
which is known to occur via a slow crack growth (SCG)
mechanism [ 4 ].
The resistance to in-service failure is usually eval-
uated in long-term hydrostatic strength (LTHS) tests,
in which the pipes are submitted to different inner
hydrostatic pressures, P , at different temperatures, T ,
for long periods of time. When subject to a inner
hydrostatic pressure, the tube wall’s stress state may
be approximated by a plane-stress state with principal
tensile stresses along the tube axis (the so called axial
stress) and along the tube circumference (the so called
circumferential, or hoop, stress,
Key words HDPE pipes
·
slow crack growth
·
water distribution systems
·
regression curve
·
ramp test
Abbreviations
LTHS
Long-term hydrostatic strength
MRS
Minimum required strength
LCL
Lowest confidence level
SCG
Slow crack growth
B
F. M. Peres
)
Department of Metallurgical and Materials Engineering,
Escola Politécnica da Universidade de São Paulo,
Av. Prof. Mello Moraes, 2463, CEP 05508-900
São Paulo, SP, Brazil
e-mail: schoen@usp.br
·
C. G. Schön (
), the magnitude of
the later being approximately twice as larger as the for-
mer [ 5 ]. As a response to this permanent stress state the
σ
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182
F.M. Peres, C.G. Schön
ln
(σ)
from the tests to the praxis, since the pipe is supposedly
tested in the same conditions as in-service. This trans-
ferability, however, must be criticised, since:
ductile
σ c
The LTHS tests are developed in laboratory-
controlled situation (in particular, constant P and
T is observed during the entire test schedule), while
they experiment fluctuations of these conditions in
service;
brittle-like
The failure of a HDPE pipe will be controlled also
by extrinsic factors, like damage introduced during
installation or use, and the lifetime of the installed
pipe will be, eventually, shortened in comparison
with the one obtained in the LTHS tests;
ln(t r )
Fig. 1 A typical ‘regression curve’ as obtained in LTHS tests of
HDPE pipes
Part of the room temperature ‘regression curve’ is
extrapolated from high temperature tests using the
thermo-temporal superposition principle and the
use of this principle in extruded semi-crystalline
polymers should be questioned, since reorienta-
tion of the macromolecules from the initially tex-
tured material, characteristic of the extruded pipe,
is likely to happen during these high temperature
tests [ 8 ].
material deforms by creep and two major failure modes
are identified: a ‘ductile’ mode, characteristic of high
stresses (high P
σ σ c ) – followed by bulging or
ballooning of the tube wall – and a ‘brittle-like’ mode,
characteristic of lower stresses (low or moderate P
σ<σ c ) – followed by negligible macroscopic plastic
deformation, with the development of a small through
longitudinal crack (slit fracture) [ 1 , 2 ]. Service failures,
except in the case of accidents, are brittle-like since the
pipe is designed to withstand the inner pressures which
would lead to ductile fracture.
The results of the LTHS tests are usually evaluated
in terms of a graphic, known in the praxis as ‘regres-
sion curve’: a bi-logarithmic plot of the hoop stress,
σ
The LTHS tests and the ‘regression curve,’ therefore,
cannot be directly related with the life expectation of
the pipe in the water distribution system. However,
indirectly they allow us to compare resins under similar
conditions: a PE-100 resin is expected to have superior
in service performance in comparison with a PE-80 one.
In addition, the determination of the ‘regression curve’
of a polymer requires several long-term creep tests (up
to 10 4 h) and hence the LTHS test are considerably
expensive, becoming in most cases impracticable as
a quality control tool. Finally, the ‘regression curve’
philosophy implies a very long lifetime for the pipes
(50 years), while experience shows that in-service fail-
ures are observed in a much shorter timescale.
The aim of the present work is to suggest an al-
ternative procedure for comparison of different resins
based on the ‘ramp test,’ originally proposed by Zhou
et al. [ 9 ]. This will be tested by comparing the re-
sults obtained in five HDPE resins designed for water
and gas pipe extrusion, obtained from four traditional
suppliers, with the available data on their respective
regression curves.
versus time-to-failure, t r . The results for each of
the above mentioned failure modes in such plots are
linear with negative slopes (See Fig. 1 ). 1
The ductile-
to-brittle transition stress,
σ c is characteristic of a given
formulation (i.e. base resin plus additives) and is not
easily observed in room temperature tests, requiring
extrapolation from results at higher temperatures for
its determination. The LTHS test is also used for the
establishment of a ‘minimum required strength’ (MRS)
at 50 years of lifetime, according to the ISO 9080
Standard [ 6 ], which, in its turn, is used to classify the
material (in form of extruded pipe). For example, a
HDPE formulation which is predicted to fail in the
LTHS tests at 50 years for 8
0 MPa has a
MRS of 8.0 MPa and is designated as PE-80, according
to the ISO 12162 Standard [ 7 ].
The LTHS test, the ‘regression curve’ and MRS
concepts are widely accepted by the water distribution
industry for the specification of HDPE pipes. This is
probably due to the apparent transferability of results
.
0
σ<
10
.
Methodology
The ‘ramp test’ consists in the assessment of the engi-
neering yield stress (
1 In other words, the hoop stress and time-to-failure are power-
law-related, with negative exponents.
σ y ) and engineering draw stress
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Slow crack growth resistance in Polyethylene
183
σ dr ) of standard tensile specimens 2
(
as a function of
index of 0.85 g (190 ºC/5 Kg/10 min) according
to ISO 1133. Extracted data from the ‘regres-
sion curve’ (Fig. 3 ), according to ISO 9080:
LTHS (50 years/20 ºC) = 9.38 MPa, LTHS/LCL
(50 years/20 ºC) = 8.64 MPa (MRS = 8.0 MPa).
MDPE 8818 – Non-pigmented polyethylene com-
pound, supplied by PBBPolisur S. A. (Dow
Latin America), classified as PE-80, according
to ISO 12162, designed (after pigmentation),
for water and natural gas pipe extrusion. The
material has density 0.940 g/cm 3 and melt flow
index 0.77 g (190ºC/5 Kg/10 min) according
to ASTM D 1238. Extracted data from the
‘regression curve’ (Fig. 4 ) of the compound
produced with this resin and a yellow pigment
(MDPE 8818 YW), according to ISO 9080:
LTHS/LCL (50 years/23 ºC) = 8.03 MPa (MRS
= 8.0 MPa).
HP 0155 – Experimental non-pigmented compound,
supplied by Braskem S. A., classified as PE-
100 according to ISO 12162, designed, after
pigmentation for water and natural gas pipe
extrusion. The compound with black pigment
(carbon black) has density of 0.955 g/cm 3 and
melt flow index of 0.3 g (190ºC/5 Kg/10 min).
Extracted data from the ‘regression curve’
(Fig. 5 ) of the black compound, according to
ISO 9080: LTHS (50 years/20ºC) = 10.7 MPa,
LTHS/LCL (50 years/20ºC) - 10.1 MPa (MRS
10.0 MPa).
MP 0240 – Experimental non-pigmented polyeth-
ylene compound, supplied by Braskem S. A.,
designed after pigmentation for water and
natural gas pipe extrusion. The compound
produced with this resin in the yellow colour
has density 0.939 g/cm 3 and melt flow index
0.8 g (190ºC/5 Kg/10 min). Extracted data
from the ‘regression curve’ (Fig. 6 )ofthe
yellow compound, according to ISO 9080:
LTHS (50 years/20ºC) = 8.81 MPa, LTHS/LCL
(50 years/20ºC) = 8.28 MPa (MRS = 8.0 MPa).
ε
the strain rate (
)[ 9 ]. Both functions are linear with
different positive slopes when plotted against the log-
arithm of the strain rate. The intersection of the two
lines, according to the original proposal, corresponds to
the critical stress for the ductile-to-brittle transition (
σ c )
[ 9 ]. In spite of its minimalistic structure, this method
is based on solid hypotheses about the damage mi-
cromechanics of polyethylene (nucleation and growth
of crazes and subsequent rupture of the fibrils) [ 10 ].
The procedure here suggested consists in combining
a limited number of shorter-term hydrostatic strength
tests at ambient temperature, to determine the ductile
wing of the ‘regression curve,’ with the ‘ramp test,’ to
establish the lowest limit of hoop stress (
σ = σ c )for
which the the extrapolation of this ductile wing would
be valid. The procedure for the determination of the
MRS, described in the ISO 12162:1995 Standard [ 7 ]
would be then adopted for classification of the polymer
provided the ductile wing of the curve can be extrapo-
lated to t f
50 years. This suggested methodology will
be, from now on, briefly referred to as “STHS”.
Experimental
Materials
The following HDPE resins have been investigated in
the present work:
GM 5010 T2 – Black polyethylene compound 3 con-
taining 2.2% carbon black, supplied by Ipi-
ranga Petroquímica S/A, classified as PE-80
according to ISO 12162 and designed for wa-
ter pipe extrusion. This is a HDPE resin with
bimodal molecular mass distribution with den-
sity 0.954 g/cm 3 and melt flow index of 0.53 g
(190ºC/5 Kg/10 min) according to ISO 1133. Ex-
tracted data from the regression curve (Fig. 2 ),
according to ISO 9080: LTHS (50 years/20ºC)
= 10.232 MPa, LTHS/LCL (50 years/20ºC) =
9.901 MPa (MRS = 8.0 MPa).
Rigidex PC 002-50R968 – Blue polyethylene com-
pound, supplied by Solvay Indupa do Brasil
S.A., classified as PE-80 according to ISO 12162,
designed for water pipe extrusion. The mate-
rial has density of 0.944 g/cm 3
Test procedure
ASTM D638 Type IV standard tensile specimens have
been extracted from 200
and melt flow
3 mm plates obtained
by compression molding at 190ºC and using 19.6 MPa
closure pressure for 5 min, followed by air cooling.
Tensile tests were performed in a universal mechanical
testing machine at 25
×
200
×
2 In the original proposal, Zhou et al. [ 9 ] extract the tensile
specimens from the pipe, oriented along the extrusion direction.
3 Polyethylene compound, in the present context, corresponds to
the base polyethylene resin plus antioxidants and other additives,
among which, depending on the case, pigments.
2ºC in displacement control
(ramp test) with strain rates ranging from 0.0001 to
0.1 s 1
±
(calculated as an engineering strain rate us-
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184
F.M. Peres, C.G. Schön
Fig. 2 ‘Regression curve’ of
the GM 5010 T2 resin, as
furnished by the supplier
(LPL is an alternative
designation for the lowest
confidence limit, LCL,
obtained in the linear
regression based on the
experimental data)
ing the grip displacement rate). Three samples have
been tested for each resin and value of
Results and discussion
ε
. Average
values of
σ dr have been calculated (as well
as the respective standard deviations). Standard linear
regression has been employed to calculate
σ y and
Figure 7 shows a typical stress-strain curve for the
case of the Rigidex PC002-50R968 resin. As ex-
pected for semi-crystalline polymers like HDPE, yield
point and cold-drawing plateau are easily identified in
Fig. 7 . Nevertheless, some ambiguity in the definition
of drawing stress is possible. In the present work this
quantity is defined as the stress corresponding to 100%
σ y ×
ln
ε
and
σ
lines, from which the stress corresponding to
the intersection (
×
ln
ε
dr
σ c ) has been calculated and compared
with the respective ‘regression curve,’ furnished by the
resin supplier.
Fig. 3 ‘Regression curve’ of
the Rigidex PC 002-50R968
resin, as furnished by the
supplier
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Slow crack growth resistance in Polyethylene
185
100
sion curves”. The ISO9080 Standard requires that the
sample fails in the ductile mode for a valid estimation
of LTHS (50 years/20ºC), hence
T = 23 o C
regression line
LCL (97.5%)
σ c should be lower in
modulus for the resin i.e. the brittle-like fractures occur
at lower stresses and, therefore, after t f
50 years).
In the cases of resins GM5010T2 and PC002-50R968
the values obtained in the “ramp test” are compati-
ble with the ones estimated based on the “regression
curve” (see Fig. 2 ). The suggested STHS methodology
would eventually give the same results as the full LTHS
test, since, according to
=
10
8.03 MPa
σ c obtained in the “ramp test,”
the ductile wing of the 20ºC curve may be extrapolated
safely up to 50 years. For the MDPE 8818 and MP0240
resins, on the other hand, the “ramp test” results clearly
overestimate
50 years
1
1
10
100
1000
10000
100000
time [hours]
Fig. 4 ‘Regression curve’ of the MDPE8818YW resin, drawn
based on the data furnished by the supplier
σ c leading to the erroneous conclusion
that the pipe would fail in the “brittle-like” mode with
t f
50 years, in contradiction with the measured “re-
gression curves”.
The results for the “ramp test” in resin HP0155
suggest that
<
extension of the sample i.e.
1.0). This criterium is
arbitrary and was empirically determined, based on the
observation that at this deformation level all samples
presented a well-developed neck, which extended over
a significative portion of its length.
Figure 8 presents the results for the evaluation of
ε =
σ c is much lower than the values obtained
in the regression curve at ambient temperature, and, in
principle, the STHS method would give a valid estimate
of MRS for this compound, as in the cases of resins
GM5010T2 and PC002-50R968. A closer analysis of the
regression curve of the HP0155 resin (Fig. 5 ), however,
shows that the estimated
σ c
of the resins using the “ramp test” (points are averages
of three tests for each strain rate and error bars repre-
sent the corresponding standard deviations).
Table 1 shows the values of
σ c at 20ºC is too small. In fact,
the data shown for the LTHS tests at 60ºC
present
σ c
8 MPa. The transition at ambient temperature,
therefore, must occur at a higher stress. The measured
“regression curve” indeed “suggests” that
σ c obtained in the “ramp
test” of the investigated resins and the value of LTHS
(50 years/20ºC) obtained from the respective “regres-
σ c would be
Fig. 5 ‘Regression curve’ of
the HP 0155 Black resin,
as furnished by the supplier
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