Abstract
Stress corrosion cracking (SCC) in low alloyed steels
(LAS) has been extensively investigated during the last
two decades. One finding from recent investigations with
standard 1 CT specimen geometry is that even very small
amounts (2.5 ppb) of chlorides increase tremendously the
cracking susceptibility of LAS. However, no LAS cracking
incidents in real plants have ever been attributed to a
chloride transient. In the present work, the corrosion
potential at the bottom of the crack tip of a 1 CT LAS
specimen was calculated using a mixed-potential model for
the corrosion reaction of low-alloyed steel at the
metal/water interface allowing for active dissolution
(mainly of iron), active-to-passive transition and
dissolution in the passive state. The model was coupled
to equations describing dilute solution transport for all
the ionic and neutral species in the crevice associated
with the crack tip. The chemical and electrochemical
conditions at the bottom of the crevice, as well as an
estimate of the enrichment factor of chloride in it, were
obtained from the calculations. In the experimental part,
the corrosion behavior of LAS in a crevice environment
forming during a 50-ppb bulk water chloride transient was
studied by in-situ electrochemical impedance spectroscopy
(EIS) and mixed potential measurements, coupled to
ex-situ characterization of the oxides by microscopic and
surface analytical techniques as well as corrosion rate
estimation from exposure coupons. The material studied
was 20MnMoNi55 from the reactor coolant line of a German
NPP. The general corrosion rate was found to increase
several times when LAS was exposed to chloride from the
start of the experiment, the effect vanishing after about
150 h. The EIS data revealed that the effect of chloride
transients on an existing oxide film is moderate,
concerns mostly the processes at the inner oxide
layer/water interface and is to a major extent
reversible. The SSRT experiments showed that LAS is
susceptible to SCC in the crevice environment above a
threshold potential of about -0.35 V (SHE). The model
calculations revealed that the corrosion potential at the
crack tip of a 1 CT specimen is about -0.24 V (SHE),
almost irrespective of the crevice geometry. However, the
chloride enrichment was found to depend strongly on the
crevice geometry, increasing as the crevice width or
depth increases. Thus, any limit concentration for
chloride concentration based on 1 CT specimen laboratory
SCC crack growth rate test results should be considered
carefully and bearing in mind the possible differences in
crevice width and depth between the 1 CT specimen and
those of a realistic LAS flaw. Based on all the results
obtained, it can be concluded that chloride transients up
to 50 ppb in high temperature water do not result in any
serious consequences for the corrosion of low alloyed
steel with stainless steel cladding.
| Original language | English |
|---|---|
| Publication status | Published - 1 Jan 2017 |
| Event | 20th International Corrosion Congress & Process Safety Congress 2017, Eurocorr 2017 - Prague, Czech Republic Duration: 3 Sept 2017 → 7 Sept 2017 http://www.prague-corrosion-2017.com/ |
Conference
| Conference | 20th International Corrosion Congress & Process Safety Congress 2017, Eurocorr 2017 |
|---|---|
| Abbreviated title | Eurocorr 2017 |
| Country/Territory | Czech Republic |
| City | Prague |
| Period | 3/09/17 → 7/09/17 |
| Internet address |
Keywords
- low-alloyed steel
- pressure vessel
- stress corrosion cracking
- chloride impurity
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