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Effect of the strain rate on stress corrosioncrack velocities in face-centred cubic alloys.
A mechanistic interpretation
S.A. Serebrinsky, J.R. Galvele*
Comisioon Nacional de Energa Atoomica, Departamento Materiales, Instituto de Tecnologia, Avda.
Libertador 8250, 1429 Buenos Aires, Argentina
Received 28 August 2002; accepted 2 July 2003
Abstract
Constant extension rate tests on smooth samples, with strain rate (SR) values from 106 s1
up to 20 s
1
, were used to study stress corrosion cracking (SCC) systems in face-centred cubicalloys. It was found that by increasing the SR a monotonic increase of the log CPR (crack
propagation rate) takes place. It was also observed that the slope a in log CPR vs. log SR plots
had different values for different SCC morphologies. Intergranular SCC is more steeply ac-
celerated by SR, aIG 0:50.7, than transgranular SCC, aTG 0:20.3. The differences foundbetween intergranular SCC and transgranular SCC were analysed under the light of the
available SCC mechanisms.
2003 Elsevier Ltd. All rights reserved.
Keywords: A. Stainless steel; Silver; Brass; C. Stress corrosion; Effects of strain
1. Introduction
Numerous variables have a strong effect on the stress corrosion cracking (SCC)
process in metals and alloys, the strain rate (SR) being one of them [1,2]. In a recent
publication Serebrinsky et al. [3] studied the effect of SR on the crack propagation
rate (CPR) for a variety of alloyenvironment systems. In their study the authors
covered a wide range of SR values, going from 106 s1 up to 20 s1. They found
that, while an increase in the SR produced an increase in the CPR, the effect was
*Corresponding author. Tel.: +54-11-6772-7390; fax: +54-11-6772-7404.
E-mail address: [email protected] (J.R. Galvele).
0010-938X/$ - see front matter 2003 Elsevier Ltd. All rights reserved.
doi:10.1016/S0010-938X(03)00172-0
www.elsevier.com/locate/corsci
Corrosion Science 46 (2004) 591612
http://mail%20to:%[email protected]/http://mail%20to:%[email protected]/http://mail%20to:%[email protected]/7/31/2019 Serega Lv 04
2/22
more significant for intergranular SCC than for transgranular SCC. The results
showed that the slope a in log CPR vs. log SR plots was aIG 0:50.7 for inter-granular cracking, while it only reached values of aTG 0:20.3 for transgranular
cracking. This difference in behaviour between transgranular cracking and inter-granular cracking, was confirmed by Alvarez et al. [4]. Alvarez et al. compared single
crystals of Ag10Au alloy with polycrystalline samples of the same alloy. These
authors strained the samples in both a 1 M HClO4 solution and a 1 M KCl solution,
and found slopes similar to those reported by Serebrinsky et al. [3].
In the present work a systematic study was made of all the cases studied by Ser-
ebrinsky et al. [3] in their preliminary work. Only homogeneous face-centred cubic
(fcc) alloys were considered in this study, assuming that similar plastic behaviour
would be found when straining the different fcc alloys. The previously reported
slopes for both intergranular and transgranular SCC were confirmed. An analysis
was made of the experimental results, under the scope of the available SCC mech-
anisms [5,6], and it was concluded that the surface mobility SCC mechanism ac-
counted for the experimental observations.
2. Experimental method
2.1. Materials
Only homogeneous alloys, with an fcc structure, were used in the present work.The samples were 0.8 mm diameter wires. All the samples were degreased in acetone
and subjected to a thermal treatment, as described below. Before each test, the
samples were again degreased with acetone. The alloys used were identified by their
commercial name, except for the silver alloys, which were identified by their nominal
atomic % composition. The analytical composition of the alloys used, in wt.%, were:
type AISI 304 stainless steel (Cr 16.9, Ni 8.0, Si 0.7, Mo 0.4, C 0.08, S 0.03, Fe
balance), Ag15Pd (Pd 15.5, Pb < 0.01, Cd < 0.01, Cu 0.030.1, Al 0.003, Si 0.001, Fe
0.01, Mg 0.01, Pt < 0.005, Au < 0.005, Rh < 0.15, Ir < 0.015, Ag balance), and yellow
brass (Al 0.002, Si < 0.02, Fe 0.05, Ti 0.02, Mg 0.0002, Mn 0.0005, Sn 0.02, Pb 0.02,
Cr 0.0050.02, Ni 0.050.2, Zn 34.8 0.1, Cu balance). The composition of the alloysAgxAu, where x 2, 5 and 15 at.% is given in Table 1. In the present work thesealloys are referred to as AISI 304, AgPd, AgAu and brass, respectively.
Table 1
Chemical composition of the AgAu alloys used
Alloy
(at.%)
Element (wt.%)
Au Al Cu Pt Si Fe Mg Ag
Ag2Au 3.99
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All the thermal treatments were carried out in argon atmospheres. The AISI 304
was annealed for 30 min at 1100 C, and water quenched. The AgPd and AgAu
alloys were annealed at 800 C for 1 h, and air-cooled. Brass was annealed for 24 h at454 C and water-quenched. No traces of b phase were detectable in the annealed
brass samples.
The mechanical properties of all the alloys were measured at strain rates ranging
from 105 s1 up to 1 s1. The properties measured were: the conventional flow stress
for 0.2% plastic strain (r0:2), the ultimate tensile strength (UTS) and the true strain to
rupture (er). For all the alloys the three parameters either increased slightly with SR,
or remained constant. In general the variation of UTS with SR was slightly higher
than that of r0:2. No measurements of mechanical properties were made in the range
120 s1. Since the change of the mechanical properties with SR, in the measured
range was small and smooth, it was assumed that the same should be expected for
the SR values not covered during the mechanical properties measurements. Table 2
shows the mechanical property values found at 105 s1.
2.2. Environments
All the solutions used were prepared with analytical grade reagents and triply
distilled water with a minimum resistivity of 18.2 MX cm. AISI 304 was tested in an
11.8 M LiCl solution at 130 C. In this case the temperature was kept constant within
1
C. All the other systems were tested at room temperature. The AgPd alloy wastested in aqueous 1 M KCl and 1 M KI solutions. The AgAu alloys were tested in
aqueous 1 M HClO4 solution. Brass was tested in 1 M NaNO2 solution and in a
solution with the following composition: 0.05 M CuSO4 + 1 M (NH4)2SO4, the pH of
the solution was adjusted to 6.5 with NH4OH. In the text this last solution is referred
to as Mattsons solution.
2.3. Polarization curves
Anodic polarization curves were measured in a conventional three-electrode glass
cell, with a potential scanning rate of 0.5 mV s1. The solutions were deaerated withprepurified nitrogen [7], in a scrubber connected to the cell. After a 60 min deaer-
ation, the solution was transferred to the cell. The samples were allowed to reach a
Table 2
Mechanical properties of the alloys used, at 105 s1
Alloy r0:2 (MPa) UTS (MPa) er (%)
AISI 304 206 885 34.5Ag15Pd 113 321 26.6
Ag2Au 55 182 18.8
Ag5Au 55 178 15.9
Ag15Au 53 180 16.4
Brass 95 495 40.0
No significant differences were observed when varying the strain rate.
S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612 593
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steady potential, and then the potential was scanned, beginning at a potential 100
mV below the corrosion potential. The reference electrodes used were: for AISI 304
in the LiCl solution a calomel saturated reference electrode, for brass in aqueous
NaNO2 solution, as well as for AgPd alloy in KI solution and for AgAu alloys inHClO4 solution a mercurous sulphate reference electrode, for AgPd in KCl, a silver
chloride reference electrode, prepared according to [8]. In the case of brass in
Mattsons solution a pure copper wire was used as a reference electrode. All the
potentials are reported in the standard hydrogen electrode (SHE) scale, with the only
exception of brass in Mattsons solution, where the potential applied in the straining
experiments was the equilibrium potential of copper in the solution.
2.4. Stress corrosion tests
The SCC tests were carried out at constant strain rate. For convenience, the ex-
periments were divided in three strain rate ranges: slow strain rate tests (SSRT) for
SR values in the range of 106104 s1, intermediate strain rate tests (ISRT) for SR
values in the range of 1041 s1, and ultrafast strain rate tests (UFSRT) for SR
values higher than 1 s1. For SSRT and ISRT the machines used were conventional
constant crosshead speed straining machines, and the cell used was described in [9].
The total length of the sample, between grips, was 120 mm, and the part of the
samples exposed to the corrosive solutions had an initial area of 0.8 mm 2. The
UFSRT were performed in a drop weight apparatus described in [10], and the cell
was similar to that for SSRT, but arranged for vertical straining. In the UFSRT thefailure time tr was calculated by detecting the starting point and the end of the test
with two switches wired to a Tektronix TDS-210 digital oscilloscope. With the fixed
image in the oscilloscope tr ttotDLr=DLtot was calculated, ttot and DLtot being thetotal time and length of the mobile grip displacement, and DLr the elongation to
rupture.
The electrode potentials were measured through a Luggin capillary and were kept
constant with a LYP M7 potentiostatgalvanostat. The procedure for loading the
solution into the cell as well as the reference electrodes used were those described for
the polarization curves. After the samples reached a steady potential, the chosen
potential was applied. The samples were kept at constant potential for a short time,and then the straining of the samples was started. The exposure at constant potential
pointed to obtaining a reproducible initial surface, but without allowing for excessive
surface corrosion. Typical exposure time values, at constant potential, were the
following: for AISI 304 and AgPd, 10 min, for AgAu, between 15 s and 10 min,
depending on the current density and for brass in Mattsons solution, 3 min. The
potentials applied for each experiment, are described in the next section.
The samples were strained to fracture. Afterwards the fracture surface and lateral
surfaces of the samples were observed with a Phillips 500 scanning electron mi-
croscope (SEM). Then the samples were mounted for metallographic sectioning and
observation. The crack propagation rate was calculated by dividing the crack lengthLf by the failure time tf. The former was found either by measuring the maximum
radial length of the brittle part on the fracture surface observed by SEM, or by
594 S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612
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measuring the maximum crack length on the mounted section. In those cases where
both measurements were taken into consideration, the former observations were
identified as SEM values, and the latter ones as MET values.
3. Experimental results
3.1. Polarization curves
3.1.1. AISI 304 in LiCl
The polarization curve of AISI 304 in 11.8 M LiCl solution at 130 C shows a
passive range was observed between the corrosion potential, Ecorr 0:5 VSHE, and
)0.1 VSHE. The passive current density was of the order of 10
5
A/cm2
. At potentialsabove Ep 0:1 VSHE, pitting corrosion started, and the current density rose untilohmic drop limitations appeared. The results obtained were similar to those reported
by Wilde [11], and by Duffoo et al. [12].
3.1.2. AgPd in halides
Fig. 1 shows the polarization curves for pure silver and for Ag15Pd in a 1 M KCl
solution. The arrows indicate the potential values used in the present work for the
stress corrosion tests. The curves found were similar to those reported by Duffoo and
Galvele [13]. A detailed analysis of the polarization curves was reported by these
authors. According to Duffoo and Galvele, for Ag15Pd, in 1 M KCl solution, be-tween 0.2 and 0.4 VSHE selective dissolution of silver was taking place. No traces of
Pd were detected by them in the solution after exposing the alloy for 22 h at 0.4 VSHE.
On the other hand, above 0.45 VSHE the increase in the current density was
0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.810
-3
10-2
10-1
100
101
102
103
1M KClAg 99.99%Ag - 15Pd
I(A/m2
)
E(V/SHE)
Fig. 1. Polarization curves of Ag15Pd and Ag 99.99% in 1 M KCl solution. The arrows show the po-
tentials applied in stress corrosion tests.
S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612 595
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accompanied by simultaneous dissolution of Ag and Pd. At 0.6 VSHE the amount of
Pd found by them in the solution indicated a quasi-stoichiometric dissolution of the
alloy.
3.1.3. AgAu in HClO4The polarization curves for pure silver and for AgxAu (x 2; 5; and 15 at.%)
alloys in a 1 M HClO4 solution were similar to those reported by Maier et al. [14].
These authors measured the dissolution rate of the alloys in 1 M HClO4 solution, at
constant potential, and calculated the rate of formation of dealloyed films on the
metal surface.
3.1.4. Brass in Mattsons solution
No measurements were made for the polarization curve in this system. The SCC
tests in this system were made at the equilibrium potential of pure copper in the
corrosive solution. This choice was based on the observations published by Montoto
et al. [15].
3.1.5. Brass in NaNO2For the SCC tests in this system the polarization curves published by Alvarez
et al. [16] were used.
3.2. Stress corrosion tests
3.2.1. AISI 304 in LiCl
Under the experimental conditions chosen, the fracture surface of AISI 304 was
always transgranular (TG). The experimental conditions were selected to disfavour
intergranular (IG) cracking. In this way the complications in the interpretation of the
results due to mixed cracking morphology were avoided. As shown by Galvele et al.
for hot MgCl2 [17] and LiCl [12] solutions, when increasing the potential the TG
fraction in the cracks increased. The fracture surfaces of the samples strained in the
present work showed typical features of TG cracking, such as river patterns and fan-
shaped marks starting from the initiation points. The longest cracks were usually
observed to initiate at large pits. For the lowest SR (2.4 106
s1
), usually there wasonly one, passing-through, crack. Sometimes, tiny cracks appeared in the region
close to the main crack. When SR increased, up to about 5 103 s1, a higher
number of cracks, with a length similar to the longest one, was found. For higher SR
the number of cracks decreased again, but this fact should be associated to a limi-
tation in the detection of cracks rather than to their absence. For example, for the
highest SR value in the ISRT (0.044 s1) pitting was still effective in inducing
cracking, but no cracks were detectable in the UFSRT, at 18 s1.
Scanning electron microscopy (SEM) and metallographic mounting (MET) usu-
ally gave comparable values of CPR. Fig. 2 shows crack propagation rates versus
strain rate. In the same figure the lower detection limit of the constant strain ratetechnique is shown. This limit is defined as the length of the smallest detectable crack
Lfis;min (here taken conservatively as 4 lm) divided by the largest cracking time tr;max.
596 S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612
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As mentioned in a previous publication [3] and confirmed in the present work,
there is a significant difference in the slope, a, of the loglog plot when intergranular
SCC is compared with transgranular SCC. The slope a of the loglog plot is defined
as
a o logCPR
o logSR; 1
and in the case of AISI 304 in LiCl it was 0.31. An extrapolation of this linear re-
lationship to a SR of 18 s1 showed that the expected crack propagation rate was
below the detection limit, even when the expected CPR was as high as 2 105 m s1.
If cleavage cracks, longer than 4 lm were produced, they should have been detect-
able. Nevertheless, in the present work no such cracks were found for transgranular
SCC of AISI 304 in LiCl solution.
3.2.2. AgPd in halides
This system has been previously studied with SSRT [13]. It was found that the
CPR generally increased with the potential, from the potential of formation of the
silver halide up to an overpotential of %300 mV. For higher potentials the CPRreached a plateau [13].
As reported by Duffoo and Galvele [13], fracture morphology was always IG in
both KI and KCl solutions, with no traces of TG cracking. The fracture surfaces
were covered with AgI and AgCl, respectively, as identified by EDAX. For low
potentials in KCl, the coverage was incipient, and only a small number of crystals
were observed. On the other hand, for high potentials a dense coverage with manysilver halide crystals was found. Similarly as in AISI 304, for low SR there was only
one, passing-through, crack. Small number of cracks were also observed for high
10
-6
10
-5
10
-4
10
-3
10
-2
10
-1
10
0
10
110
-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
CPR
(m/s)
Strain Rate (s-1)
Lower Det. Lim.
NF
2 tests
AISI 304 in 11.8M LiCl
SEM
MET
Fig. 2. Effect of strain rate on crack propagation rates of AISI 304 strained in a 11.8 M LiCl solution at
)0.1 VSHE and 130 C. The lower detection limit expected for the experimental technique used is shown.
NF indicates that no cracks were detected at the end of the experiment.
S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612 597
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potentials. When SR increased, or the potential decreased, a larger number of cracks
with similar length appeared. A characteristic feature, quite common in intergran-
ular stress corrosion fracture surfaces, was the presence of shallow pits or vacancy
clusters, as previously reported by Maier et al. [14].
Unlike to what was observed with AISI 304 in LiCl, AgPd alloy in halide so-
lutions gave measurable cracks for UFSRT. The cracks in a sample strained in 1 MKI at 5 s1 were about 100 lm in size. The samples strained in KCl showed shorter
cracks, but still above the detection limit of the experimental technique. The slopes a
in the logarithmic plot of Fig. 3 were clearly steeper than those found for AISI 304 in
LiCl solution. The values measured for a were between 0.5 and 0.65, and were listed
in Table 3. One important observation was that, as shown in Fig. 4, in the UFSRT,
the cracks measured at 5 s1 were always longer than those measured at 18 s1. This
observation was important because if the cracks produced at 5 s1 were due to a
single pseudo-cleavage type event, the same crack length should have been expected
for the experiments at 18 s1.
Fig. 5 shows the effect of electrode potential on the crack propagation rate atvarious strain rate values, for Ag15Pd in 1 M KCl solution. It was observed that an
increase in the potential (E) produced an increase in CPR, up to an overpotential of
about 300 mV, where a plateau was reached. The shape of the curves of CPR in
function of E was similar for all strain rates tested, but the curves were shifted to
higher CPR values as the SR increased. The present results could lead to introduce in
Eq. (1) the effect of the potential:
log CPRSR;E fE a log SR 2
suggesting that the effects of the electrochemical variable (E) and the mechanical
variable (SR) could be independent. The slope a remained fairly independent of E.According to the measurements of Yu and Parkins, Eq. (2) is also valid for brass in
nitrites [18]. The inverse slopes p of the ascending part of the CPRE curves were
10-6
10-5
10-4
10-3
10-2
10-1
100
101
10-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
Lower Det. Lim.
1M KCl 0.322VSHE 0.522VSHE0.372V
SHE0.572V
SHE
0.422VSHE
0.622VSHE
0.472VSHE
1M KI-0.15V
SHE
Ag-15Pd
CPR(m/s)
Strain Rate (s-1)
Fig. 3. Effect of strain rate on crack propagation rates of Ag15Pd in 1 M KI and KCl solutions.
598 S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612
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approximately 75 mV/decade, close to the value of 100 mV/decade reported by Galvele
et al. for low-gold AgAu alloys in 1 M potassium halide solutions at SSRT [19].
3.2.3. AgAu in HClO4
This system has been previously studied by Maier et al. [14] at SSRT, and byDuffoo and Galvele [20] and by Kelly et al. [21] at UFSRT. The experimental results
from the present work are shown in Figs. 6 and 7.
Table 3
Compilation of the slopes in log CPRlog SR plots from the present work
Alloy Environment Potential (VSHE) Morph. a a0
AISI 304 11.8 M LiCl,130 C
)0.10 TG 0.31 0.31
Ag15Pd 1 M KI 0.15 IG 0.65 0.52
Ag15Pd 1 M KCl 0.32 IG 0.59
Ag15Pd 1 M KCl 0.37 IG 0.63 0.58
Ag15Pd 1 M KCl 0.42 IG 0.53
Ag15Pd 1 M KCl 0.47 IG 0.53 0.51
Ag15Pd 1 M KCl 0.52 IG 0.55 0.47
Ag15Au 1 M HClO4 0.90 IG 0.59 0.50
Ag15Au 1 M HClO4 1.00 IG 0.57
Ag15Au 1 M HClO4 1.15 IG 0.62 0.48
Ag5Au 1 M HClO4 0.90 IG 0.45
Ag2Au 1 M HClO4 0.90 IG 0.40
a-brass Mattsons sol.a (0.0 VCu0=Cu ) IG 0.54 0.44
a-brass 1 M NaNO2 0.20 TG 0.19 0.19
The a0 values were calculated excluding the measurements for SR higher than 1 s1.a 0.05 M CuSO4 +1 M (NH4)2SO4 + NH4OH adjusted to pH 6.5.
100 1010
10
20
30
40
50
60
Lower Det. Lim.
Strain Rate (s-1)
Lfis
(m)
0.372VSHE0.472VSHE0.522V
SHE0.572VSHE0.622VSHE
Ag-15Pd in 1M KCl
Fig. 4. Crack lengths measured at 5 s1 and at 18 s1 for Ag15Pd in 1 M KCl solutions. By increasing the
SR, in the UFSRT region, the crack lengths were found to decrease.
S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612 599
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The fracture surfaces found were always intergranular, though small isolated
transgranular patches were also detected. Vacancy clusters or shallow pits, as de-
scribed by Maier et al. [14], were also present in this system. The effect of the po-
tential and strain rate on the number and length of the cracks was the same as for
Ag15Pd in KCl, i.e. few and long cracks, with one much longer than the others, was
the situation favoured by high potentials and low SR.In this system a comparison was made on the effect of SR on CPR as a
function of alloy composition, Fig. 6, and also for one alloy at different potentials,
300 350 400 450 500 550 600 65010
-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
Strain Rate:
Ag-15Pd in 1M KCl
2.3 E-61/s8.8 E-61/s
7.3 E-51/s1.8 E-31/s4.4 E-21/s5.01/s18 1/s
CPR(m/s)
E(mV/SHE)
Fig. 5. Effect of potential on the crack propagation rate at various strain rate values, for Ag15Pd in 1 M
KCl solution.
10-6
10-5
10-4
10-3
10-2
10-1
100
101
10-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
Lower Det. Lim.
Ag-2AuAg-5AuAg-15Au
Ag-xAu in 1M HClO4, 0.9VSHE
CPR(m/s
)
Strain Rate (s-1)
Fig. 6. Effect of strain rate on crack propagation rates of AgAu alloys in 1 M HClO4, at one potential
0.9 VSHE.
600 S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612
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Fig. 7. The effect of SR was the same as found with AgPd alloy, the slopes a
were higher than those found with AISI 304. The a values found were between 0.4
and 0.65.
Fig. 7 shows the effect of the electrode potential on the SR versus CPR for Ag
15Au in 1 M HClO4. When the potential was increased it was found that the CPRalso increased. The inverse slopes pwere about 230 mV/decade, for SSRT, ISRT and
UFSRT. These results were very close to the value of ca. 200 mV/decade for Ag
2Au, Ag5Au, Ag10Au and Ag15Au at SSRT reported by Galvele et al. [19]. In
the present system no plateau velocity was reached, possibly due to the very high
dissolution rate at high potentials. The effect of increasing SR was again to shift the
CPRE curves upwards, while keeping the shape of the curves. Here again Eq. (2)
was applicable.
3.2.4. Brass in Mattsons solutionThis system showed intergranular stress corrosion cracks on the fracture surfaces,
with occasional transgranular patches. The variation of the number and distribution
of the length of cracks with strain rate was similar to that described in the previous
systems, including the decrease in the number of cracks at UFSRT observed in AISI
304. Fig. 8 shows the logarithmic plot of CPRSR, where a slope a of 0.54 was
found.
3.2.5. Brass in 1 M NaNO2 solution
The fracture surfaces in this system were transgranular, as described by Alvarezet al. [16] and by Rebak et al. [22]. The results of the straining experiments are shown
in Fig. 9, and the slope for a was 0.19 [3].
10-6 10-5 10-4 10-3 10-2 10-1 100 10110
-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
0.9VSHE
1VSHE1.1V
SHE
1.15VSHE
Ag-15Au in 1M HClO4
CPR(m/s)
Strain Rate (s-1)
Lower Det. Lim.
Fig. 7. Effect of the electrode potential on the SR versus CPR for Ag15Au in 1 M HClO4.
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4. Discussion
4.1. Difference between IG and TG cracking
The analysis of the experimental results described above indicates that there is aclear and consistent difference in the values of the logarithmic slope a, Eq. (1), when
intergranular SCC systems are compared with transgranular SCC systems. It was
10
-6
10
-5
10
-4
10
-3
10
-2
10
-1
10
0
10
110
-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
Lower Det. Lim.
CPR(m/s)
Strain Rate (s-1)
Brass in Mattson's solution
Fig. 8. Effect of strain rate on crack propagation rates of brass in Mattsons solution (0.05 M CuSO4 + 1
M (NH4)2SO4 + pH 6.5 adjusted with NH4OH) at 0 VCu.
10-6
10-5
10-4
10-3
10-2
10-1
100
101
10-9
10-8
10-7
10-6
10-5
10-4
10
-3
10-2
10-1
CPR - UTS
CPR - 0.2
Lower Det. Lim.
CPR(m/s)
Strain Rate (s-1)
Brass in 1M NaNO2solution
Fig. 9. Effect of strain rate on crack propagation rates of brass in 1 M NaNO2 solution at 25 C and 0.2
VSHE. The meaning of the CPR lines will be considered in Section 4.
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always found that the slope for intergranular SCC was higher than that for trans-
granular SCC:
aIG > aTG: 3
Table 3 shows the values for a found in the present work. Since the values of CPR
could not be measured in some systems for UFSRT, Table 3 also includes the values
for a0, defined by the same Eq. (1) but taking into account the measurement for SR
up to 1 s1 (i.e. neglecting UFSR tests).
The data in Table 3 shows that Eq. (3), either for a or a0, is satisfied in all the
systems studied. One objection that could be raised is that different systems were
compared. In support of the conclusion reached in Eq. (3) the following facts should
be taken into account. (a) Only fcc alloys were considered. Thus systems with similar
deformation mechanisms were compared. (b) One same alloy, from the same batch
(brass), was subjected in the present work to IGSCC (Mattsons solution) and
TGSCC (1 M NaNO2 solution) and the results were compared. The values found,
for the same alloy in two different environments, were aIG 0:54 and aTG 0:19,which confirms Eq. (3). (c) Alvarez et al. [4] studied one single alloy system (AgAu
alloy) in the same environment, and produced IGSCC and TGSCC. For this purpose
these authors compared AgAu single crystals with AgAu poly-crystals. The studies
were made in 1 M HClO4 solution and in 1 M KCl solution. As shown in Table 4,
and discussed below, Alvarez et al. were able to confirm the validity of Eq. (3).
To further confirm the validity of Eq. (3), values of a published in previous
publications were collected in Table 4. As mentioned above, a major point in the
analysis of the present results is provided by the work of Alvarez et al. [4]. Theseauthors strained single crystals of Ag10Au in 1 M HClO4 and 1 M KCl solutions.
As for the gold contents x, Maier et al. [14] showed that for x between 2.2 and 15
at.% Au there was no noticeable effect of the alloy composition on CPR, in experi-
ments made at a slow strain rate. In the present work it was found that this
observation is correct also when measurements are made with the ISRT. As a
consequence, the measurements made by Alvarez et al. [4] can be compared with
those reported in the present work. Alvarez et al. found for TGSCC aTG 0:22,while for IGSCC they found aIG 0:48. In the present work the lowest value for
Table 4Compilation of the slopes a in logCPRlog SR plots from previous publications
Alloy Environ-
ment
Reference Potential
(VSHE)
Morph. a a0
Ag20Au 1 M HClO4 [20] 1.20 IG 0.60
Ag20Au 1 M KCl [20] 0.70 IG 0.63 0.69
Ag15Au 1 M KCl [4] 0.50 IG 0.68
Ag15Au 1 M HClO4 [4] 0.90 IG 0.48
Ag10Au
single crystal
1 M KCl [4] 0.50 TG 0.30
Ag10Au
single crystal
1 M HClO4 [4] 0.90 TG 0.22
IG: Intergranular SCC; TG: Transgranular SCC. The a0 values exclude measurements for SR higher than
1 s1.
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IGSCC (a0 for Ag2Au) was aIG 0:4, all the other a values being higher. When themeasurements were made in KCl solution, the difference between IGSCC and
TGSCC was maintained. Alvarez et al. measured for TGSCC aTG 0:30 and for
IGSCC aIG 0:68. Duffoo and Galvele [20] reported for IGSCC of Ag20Au in 1 MKCl aIG 0:63 and in 1 M HClO4 aIG 0:60.
Finally, it is important to point out that in the present work, in the case of
TGSCC of stainless steels in hot concentrated chloride solutions, as well as brass in
nitrite solutions, no cracks were detected after UFSRT. On the other hand, no
reference was found in the literature of detection of any incipient transgranular
cracks after an UFSRT. If there were any cracks, they were smaller than the de-
tection limit of the technique used in the present work.
4.2. Mechanistic interpretation
The above results will be analysed within the scope of the surface mobility SCC
mechanism. When appropriate, references to the film induced cleavage SCC mech-
anism [5], and the anodic dissolution SCC mechanism [5] will be made. Since the
above analysis involves the use of the equations developed for the surface mobility
SCC mechanism, a brief review of those equations will be made.
The surface mobility mechanism [5,23,24] is based on the assumption that the
environment acts by increasing the surface mobility of the alloy, and that the cracks
propagate by capture of vacancies at the tip of the stressed crack. This mechanism
was used to quantitatively explain numerous cases of SCC [5,6,10,24,25]. The fol-lowing equation was developed for the crack propagation rate [23,24]:
CPR DS
Lexp
rTa3
kT
1
; 4
DS being the surface self-diffusion coefficient at the crack walls, L the diffusion dis-
tance of the vacancies, rT the elastic stress at the tip of the crack, a the atomic size,
k the Boltzmann constant, and T the temperature in K.
Since measured DS values, for the conditions of interest for SCC, are very scarce
two different approaches can be used to calculate the value ofDS. When a solid film,with a known melting point, contaminates the crack surface, an empirical equation,
based on the work of Gjostein [26] and Rhead [27,28] can be used to calculate DS[23]:
DS m2 s1 740 104 exp126Tm=RT 0:014 10
4 exp54Tm=RT;
5
R being the molar gas constant (R 8:314 J mol1 K1), T the absolute temperaturein K, and Tm the melting point of the surface film in K.
On the other hand, when no surface films are formed, but the SCC process isspecifically affected by the concentration of cations of the noble metal of the alloy, as
in the case of AgCd alloy in AgNO3 solution, Galvele and Duffoo [29] developed an
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equation for the calculation ofDS, based on the alloy composition and the exchange
current density of the noble metal.
4.3. Transgranular stress corrosion cracking
4.3.1. AISI 304 in LiCl
The crack propagation rate values measured with SSRT for AISI 304 in LiCl
solution at 130 C, Fig. 2, are very close to those found by Speidel [30] using fracture
mechanics techniques. This coincidence in the measured CPR values proved that the
SSRT is a valid technique for measuring crack propagation rates in the present
system.
As mentioned by Duffoo et al. [12] for this SCC system, assuming that the surface
mobility SCC mechanism was operative, the analysis of the temperature dependenceof CPR showed that DS at 130 C was approximately 3 10
15 m2 s1. For SSRT the
predicted CPR values, with the stress rT equal to r0:2 (206 MPa, Table 2), agreed
very well with the present experimental results. When increasing the strain rate, the
samples fractured with noticeable plastic deformation. Then it is reasonable to as-
sume that the value of rT will increase, eventually reaching the UTS value (885 MPa,
Table 2). As shown in Fig. 10, using these two rT values (Table 2) the extreme CPR
values predicted by the surface mobility mechanism contain the experimentally
measured values.
There is no information about the exact values rT will have at different strain
rates. Nevertheless, in SSRT the samples fracture with very small plastic deforma-tion; consequently it is reasonable to assume that the stress at the tip of the crack will
be close to r0:2. On the other hand, under high strain rates, where cracks propagate
while the samples are undergoing strong plastic deformation, the first assumption
would be that the maximum value reached by the stress at the tip of the crack would
be that given by the UTS. The results in Fig. 10 suggest that the surface mobility
SCC mechanism could give a good account for the correlation found between CPR
and SR for transgranular SCC. No equations were found in the literature for a
similar analysis from the point of view of the film induced cleavage SCC mechanism,
or the anodic dissolution SCC mechanism. Consequently, from Fig. 10 no conclu-
sions can be drawn either supporting or disqualifying these two mechanisms.
4.3.2. Brass in NaNO2The reactions taking place at the tip of the crack, during SCC of brass in NaNO 2
solutions are only ambiguously known. Newman and Burstein [31] suggested that
decomposition of nitrite ions could lead to the formation of ammonia, with subse-
quent stability of copper ions by complex formation. On the other hand Rebak et al.
[22] concluded that passivity breakdown was the step previous to SCC of brass in
NaNO2 solution. For any of these alternatives, the environment at the crack tip
would be a solution with a high concentration of copper ions, providing a highexchange current density i0 of Cu$Cu
. In this case, surface diffusion would be
associated with the exchange current density, as in the model of Galvele and Duffoo
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[29]. Giordano et al. [32] and Montoto et al. [15] confirmed the validity of this hy-
pothesis.
When the value of DS is not known, but experimental CPR values are available
for a given experimental condition, Eqs. (4) and (5) can be used to predict the CPR
value at a different condition. This was done, for example, to predict CPR values foralloy 600 at different temperatures [25]. In the present case it will be assumed that in
a SSRT the value of rT is equal to r0:2 and with the CPR value measured at SSRT,
plus Eqs. (4) and (5), a DS value fitting these results can be calculated. Assuming that
this value does not change with the SR, and also assuming, as done above, that the
maximum stress value at the tip of the crack will be the UTS, the maximum CPR
expected can be calculated. Fig. 9 shows that, as it was the case with AISI 304 in LiCl
solution, the CPR values measured at different SR for SCC of brass in NaNO 2solutions fall between the extreme values predicted by the surface mobility SCC
mechanism.
4.4. Intergranular stress corrosion cracking
4.4.1. Brass in Mattsons solution
Speidel [33], using fracture mechanics techniques, for brass, of a composition
equal to that used in the present work and exposed to a NH 4OH solution, reported
CPR values very close to those found in the present work, with SSRT (Fig. 8). As
mentioned above for AISI 304, this observation gives support to the validity of the
CPR values measured with SSRT.
The same procedure used for brass in NaNO2 solutions, was applied to the CPRresults measured for brass in Mattsons solution. As before, the value of DS fitting
the SSRT results was calculated. Then with the DS value found, the CPR for rT equal
10-6 10-5 10-4 10-3 10-2 10-1 100 10110
-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
Lower Det. Lim.
NF2 tests
AISI 304 in 11.8M LiCl
SEM CPR - 0.2MET CPR -
UTS
CPR(m/s)
Strain Rate (s-1)
Fig. 10. Crack propagation rates of AISI 304 in 11.8 M LiCl at 130 C. Comparison of measured values
with the predicted range of the surface mobility SCC mechanism.
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to the UTS was calculated. As shown in Fig. 11, contrary to what was found for
transgranular SCC, Figs. 9 and 10, the extreme values of CPR predicted by the
surface mobility SCC mechanism were not the limits for the experimentally found
CPR for intergranular SCC. As shown in Fig. 11, when the strain rate increased, the
measured crack propagation rates exceeded the values predicted by surface mobility,if as done before, the maximum stress rT acting at the tip of the crack was considered
to be the UTS. A calculation of the maximum stress rT required by Eq. (4) to fit the
CPR measured in UFSRT gave a value of 2.7 GPa, which was about five times larger
than the UTS. The stress values required by Eq. (4) to fit the experimental CPR
values are shown in Fig. 12.
One possible reason for the different effect on SR, between intergranular and
transgranular SCC, could be the fact that grain boundaries act as barriers for the free
movement of dislocations, leading to dislocation pileups [34]. At an atomic level, at
the tip of the crack, this process will lead to an increase in the value of rT well above
the externally applied stress. As discussed below, the dislocation pileups could ac-count for the required stress values mentioned in Fig. 12. A very crude calculation of
the formation rate of dislocations, at different strain rates, can be attempted by using
the equations developed by Van Bueren [35]. Fig. 13 shows the results of such cal-
culations for copper. It is interesting to point out the similarity between Fig. 13 and
Figs. 7 and 8. If the role of dislocations was to produce a surface slip step, where
corrosion would be localised, as it is assumed in the slip-step anodic dissolution SCC
mechanism [5], an increase in the strain rate should produce an increase in the crack
propagation rate, as found in the present work. Nevertheless, the anodic dissolution
SCC mechanism does not predict a difference in behaviour between IGSCC and
TGSCC. On the other hand, any mechanism based on the elastic stresses at the tip ofthe crack will be able to explain the difference between IGSCC and TGSCC, because
of the higher stress values induced by the dislocation pileups at the grain boundaries.
10-6
10-5
10-4
10-3
10-2
10-1
100
101
10-9
10-8
10-7
10-6
10-5
10-4
10-3
10-2
10-1
CPR - UTS
CPR - 0.2
CPR(m/s)
Brass in Mattsons solution
Strain Rate (s-1)
Fig. 11. Comparison of crack propagation rates of brass in Mattsons solution (0.05 M CuSO4 + 1 M
(NH4)2SO4 + pH 6.5 adjusted with NH4OH) at 0 VCu, measured and predicted by surface mobility.
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4.4.2. AgPd in halides
The same procedure used above was applied to the CPR results measured for Ag
Pd in halide solutions. As before, the values ofDS fitting the SSRT were calculated.
Then, with the DS values found, the CPR for values rT equal to the UTS were
calculated.
For potassium iodide environment, with the calculated value ofDS, results similar
to those in Fig. 11 were found. The relation of rT=UTS required to fit the measuredCPR had a maximum value of 4.5, very close to the value %5 indicated in Fig. 12.This observation supports the same assumptions made above for IGSCC.
10-6 10-5 10-4 10-3 10-2 10-1 100 1010
500
1000
1500
2000
2500
3000
Stress(MPa)
0.2
UTS
required
Strain Rate (s-1)
Brass in Mattson's solution
Fig. 12. Stresses rT of Eq. (4) required to fit the measured crack propagation rates of brass in Mattson s
solution (0.05 M CuSO4 + 1 M (NH4)2SO4 + pH 6.5 adjusted with NH4OH) at 0 VCu.
10-6
10-5
10-4
10-3
10-2
10-1
100
101
104
105
106
107
108
109
1010
1011
1012
Disloc.
Density(cm
s
)
-2
-1
Strain Rate (s-1)
Fig. 13. Rough estimate of the rate of production of dislocations, in copper, at various strain rates, based
on Van Buerens equations [35].
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For potassium chloride environment a range of potentials was applied, and more
data is available. The polarization curve, Fig. 1, shows a noticeable discontinuity at
about 0.45 VSHE, related to the change in the mode of dissolution of the alloy.
Nevertheless, as reported by Duffoo and Galvele for SSRT [13], and confirmed in thepresent work with different SR values, no discontinuities were observed in CPR at
any SR, Figs. 3 and 5. These observations suggest that, at least for IGSCC of Ag
15Pd in 1 M KCl solution, the dissolution mode of the alloy had no effect on the
SCC process.
As regards Eq. (2), and following the predictions of the surface mobility SCC
mechanism, the present results suggest the following: apparently, if Eq. (4) is taken
into account, the effect of SR is concentrated mainly on the mechanical variable rT,
while the potential Eacts mainly by changing the value ofDS (and possibly to some
extent L).
4.4.3. AgAu in HClO4Due to the high solubility of AgClO4 in water, 26.9 moles per litre of water [36], it
is probable that during dissolution, an acid concentrated AgClO4 solution will be
present next to the alloy interface, but no surface compounds will be expected. No
measurements are available at present of the DS value expected in this system. Vela
et al. [37] reported that the rate of step movement on pure Ag surfaces, in 1 M
HClO4 solution, was an order of magnitude higher than in vacuum. On the other
hand, Duffoo and Galvele [20] reported that SCC of Ag20Au alloy was faster in 1 M
AgClO4 solution than in 1 M HClO4 solution. While the operating mechanism is stillnot clear, it is safe to assume that the DS value in this system is high.
Using the same approach applied in the above discussed SCC systems, it was
found again that with the calculated value ofDS, results similar to those in Fig. 11
were found. The relation rT=UTS required to fit the measured CPR was very close tothat shown in Fig. 12.
These are two facts that should be pointed out. The first one is that the effect of
potential and SR on the CPR can be described by Eq. (2), as it was the case with Ag
Pd in halides. The second one is that Alvarez et al. [4] found that the inverse slope p
from a log CPREplot is the same for both IGSCC and TGSCC. These observations
indicate that there is an association between SR and rT, as well as for a with the SCCmorphology and also an association between E and DS, if the surface mobility
mechanism is considered, Eq. (4). As a further contribution to this point, Alvarez
et al. [38] have recently found that the activation energy for IGSCC of AgAu alloy
was equal to that for TGSCC for the same alloy, and that there was a coincidence
between the activation energy predicted by the surface mobility SCC mechanism and
the experimental results.
As for the film induced cleavage (FIC) mechanism, Maier et al. [14] showed that
there was no relation between the rate of dealloyed film formation and the CPR, as
should be expected if the FIC mechanism was operative. The supporters of the FIC
[39] attributed particular importance to the critical potential for selective dissolution(Ec) in alloys like AgAu. Maier et al. [14] found that changes in the nature of the
selective dissolution process had no effect on the CPR. This observation was
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particularly evident for Ag15Au, Ag25Au and Ag40Au alloys 1 M HClO4 so-
lution [14]. No breaks were found in the CPR vs. Ecurve when the potential crossed
the critical potential value. These results showed that SCC of AgAu alloys in
HClO4 solution was independent of the Ec value, and that there was no experimentalevidence correlating the SCC with that critical potential value. A similar observation
regarding Ec was reported by Lichter et al. [40] for CuAu alloys.
4.5. Mechanistic considerations
The above observations indicate that the slope in Eq. (1) is higher for IGSCC than
for TGSCC, Eq. (3). Besides the numerous considerations made above, the in-
volvement of SCC mechanisms, other than the surface mobility mechanism, will be
further considered.In the case of the film rupture, or slip step anodic dissolution mechanism, it
should be expected that, as found in the present work, an increase in the strain rate
will lead to an increase in the SCC rate. Nevertheless, as mentioned above, the effect
should be the same for IGSCC and for TGSCC. In the literature of slip step anodic
dissolution mechanism no explanation was found for the observation indicated by
Eq. (3).
As for the FIC SCC mechanism, as mentioned above, numerous contradictions
were found by various authors between the predictions of this mechanism and the
experimental results. On the other hand, the literature published on this mechanism
does not give, so far, any clue for the observation indicated by Eq. (3). Besides, in thepresent work, Fig. 4, longer cracks were found for 5 s1 than for 18 s1. From the
descriptions given for the FIC mechanism, a single event of crack propagation
should be expected at both strain rates, and no difference in the crack length should
be observed. Unfortunately no further quantitative comparisons can be made for
this mechanism at the present state of development of the FIC model.
5. Conclusions
The following conclusions can be drawn from the present work:
An increase of the strain rate generally accelerates the crack propagation process
according to the relation (1), or equivalently
log CPR / alog SR: 6
The slope a is different for transgranular and intergranular cracking. The values are
aTG 0:20.3 and aIG 0:40.7.The effect of potential can be incorporated as an additional term fE in Eq. (6),
not having a noticeable effect on the SR-dependent term.
No information was found in the anodic slip step dissolution mechanism, thatcould explain the present experimental results. The FIC mechanism requires further
development to account for the differences found between IGSCC and TGSCC.
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The surface mobility SCC mechanism can account for the dependence of crack
propagation rate on strain rate. With an increasing strain rate, the stress at the crack
tip zone will increase due to the formation of dislocation pileups, which is equivalent
to say that the driving force for the movement of surface vacancies increases.The surface mobility SCC mechanism can account for the separate effect of strain
rate and potential on crack propagation rates, according to Eq. (2). The strain rate
affects the stress at the tip of the crack, as indicated above, and the potential affects
the surface diffusion coefficient.
The absence of transgranular cracks, when very high strain rates are used, favours
a continuous crack propagation model and sheds doubts on any mechanism based
on very fast and discontinuous crack propagation events.
Acknowledgements
The present research has been supported by the Consejo Nacional de Investi-
gaciones Cientficas y Teecnicas, Argentina, and by the FONCYT, Secretara de
Ciencia y Tecnologa, Argentina.
References
[1] J.C. Scully, D.T. Powell, Corros. Sci. 10 (1970) 719.[2] R.H. Jones, R.E. Eicker, in: R.H Jones (Ed.), Stress Corrosion Cracking, ASM International, Ohio,
1992, p. 4.
[3] S.A. Serebrinsky, G.S. Duffoo, J.R. Galvele, Corros. Sci. 41 (1999) 191.
[4] M.G. Alvarez, S.A. Fernaandez, J.R. Galvele, Corros. Sci. 42 (2000) 739.
[5] J.R. Galvele, in: R.E. White, J.OM. Bockris, B.E. Conway (Eds.), Modern Aspects of Electrochem-
istry, vol. 27, Plenum Press, New York, 1995, p. 233.
[6] J.R. Galvele, in: R.H. Jones (Ed.), Chemistry and Electrochemistry of Stress Corrosion Cracking,
TMS, Warrendale, PA, 2001, p. 27.
[7] D. Gilroy, J.E.O. Mayne, J. Appl. Chem. 12 (1962) 382.
[8] G.J. Janz, in: D.J.G. Ives, G.J. Janz (Eds.), Reference electrodesTheory and practice, Academic
Press, New York, NY, 1961, p. 179.
[9] J.R. Galvele, S.M. de De Micheli, I.L. Muller, S.B. de Wexler, I.L. Alanis, in: R.W. Staehle, B.F.Brown, J. Kruger, A. Agrawal (Eds.), Localized Corrosion, NACE, Houston, 1974, p. 580.
[10] J.R. Galvele, in: S.M. Bruemmer, E.I. Meletis, R.H. Jones, W.W. Gerberich, F.P. Ford, R.W. Staehle
(Eds.), Parkins Symposium on Fundamental Aspects of Stress Corrosion Cracking, The Minerals,
Metals & Materials Society, Warrendale, PA, 1992, p. 85.
[11] B.E. Wilde, J. Electrochem. Soc. 118 (1971) 1717.
[12] G.S. Duffoo, I.A. Maier, J.R. Galvele, Corros. Sci. 28 (1988) 1003.
[13] G.S. Duffoo, J.R. Galvele, Corros. Sci. 30 (1990) 249.
[14] I.A. Maier, S.A. Fernaandez, J.R. Galvele, Corros. Sci. 37 (1995) 1.
[15] M.L. Montoto, G.S. Duffoo, J.R. Galvele, Corros. Sci. 43 (2001) 755.
[16] M.G. Alvarez, C. Manfredi, M. Giordano, J.R. Galvele, Corros. Sci. 24 (1984) 769.
[17] C. Manfredi, I.A. Maier, J.R. Galvele, Corros. Sci. 27 (1987) 887.
[18] J. Yu, R.N. Parkins, Corros. Sci. 27 (1987) 159.
[19] J.R. Galvele, I.A. Maier, S.A. Fernaandez, Corrosion 52 (1996) 326.
[20] G.S. Duffoo, J.R. Galvele, Metall. Trans. A 24 (1993) 425.
S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612 611
7/31/2019 Serega Lv 04
22/22
[21] R.G. Kelly, A.J. Frost, T. Shahrabi, R.C. Newman, Metall. Trans. A 22 (1991) 531.
[22] R.B. Rebak, R.M. Carranza, J.R. Galvele, Corros. Sci. 28 (1988) 1089.
[23] J.R. Galvele, Corros. Sci. 27 (1987) 1.
[24] J.R. Galvele, Corros. Sci. 35 (1993) 419.
[25] J.R. Galvele, J. Nucl. Mat. 229 (1996) 139.
[26] N.A. Gjostein, in: J.J. Burke, N.L. Reed, V. Weis (Eds.), Surfaces and Interfaces-I, Syracuse
University Press, 1967, p. 271.
[27] G.E. Rhead, Surf. Sci. 15 (1969) 353.
[28] G.E. Rhead, Surf. Sci. 22 (1970) 223.
[29] J.R. Galvele, G.S. Duffoo, Corros. Sci. 39 (1997) 605.
[30] M.O. Speidel, Metall. Trans. A 12 (1981) 779.
[31] R.C. Newman, G.T. Burstein, J. Electrochem. Soc. 127 (1980) 2527.
[32] C.M. Giordano, G.S. Duffoo, J.R. Galvele, Corros. Sci. 39 (1997) 1915.
[33] M.O. Speidel, in: M.O. Speidel, A. Atrens (Eds.), Corrosion in Power Generating Equipment, Plenum
Press, New York, 1984, p. 85.
[34] J.P. Hirth, J. Lothe, in: Theory of Dislocations, Krieger Publishing Co., Malabar, FL, 1992, p. 764.[35] H.G. Van Bueren, in: Imperfections in Crystals, North-Holland Publishing Co, Amsterdam, 1960,
p. 156.
[36] R.C. Weast (Ed.), CRC Handbook on Chemistry and Physics, 54th ed., CRC Press, Cleveland, 1973,
p. B-134.
[37] M.E. Vela, G. Andreasen, R.C. Salvarezza, A. Hernaandez-Creus, A.J. Arvia, Phys. Rev. B 53 (1996)
10217.
[38] M.G. Alvarez, S.A. Fernaandez, J.R. Galvele, Corros. Sci. 44 (2002) 2831.
[39] F. Friedersdorf, K. Sieradzki, Corrosion 52 (1996) 331.
[40] B.D. Lichter, W.F. Flanagan, J.B. Lee, M. Zhu, in: R.P. Gangloff, M.B. Ives (Eds.), Environment-
Induced Cracking of Metals (NACE-10), NACE, Houston, TX, 1990, p. 251.
612 S.A. Serebrinsky, J.R. Galvele / Corrosion Science 46 (2004) 591612