Abstract
Stress corrosion cracking (SCC) is commonly observed to form a colony of closely spaced multiple cracks. Four stages of SCC colony evolution are discussed. The first is the colony initiation stage (CIS), which is associated with formation of corrosion pits randomly distributed over a certain domain of the surface exposed to an aggressive environment. Electrochemical processes play a leading role in CIS. The individual crack growth (ICG) driven by a combination of mechanical stresses and electrochemical processes constitutes the second stage. At the end of the second stage, the individual cracks reach certain proximity of one another resulting in much crack interaction. This becomes a transition to the third, strong crack interaction and clusters formation, stage. Cluster growth and individual crack or a cluster instability leading to the ultimate failure constitute the final, fourth stage of the SCC evolution process. In this article, we present observations and a general approach to modeling the first two stages of SCC, i.e., CIS and ICG, that together constitute the major part of the total lifetime of an engineering structure serving under SCC conditions. A computer simulation of individual SC crack growth is developed and compared with a large set of SCC observation data.
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Acknowledgment
The authors express deep gratitude to Ilhyun Kim and Yongjian Zhao for their technical help.
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Manuscript submitted January 28, 2010.
Appendix A
Appendix A
1.1 Representation of the concentration of hydrogen at the crack tip
The distribution of the concentration of hydrogen, C(x, t), satisfies the diffusion equation
The vector flux of hydrogen is \( \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{q} (x,t)_{|x = 0} = \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{q} (t) = \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{q} \cdot \underset{\raise0.3em\hbox{$\smash{\scriptscriptstyle-}$}}{e}_{1} , \) and the boundary and initial conditions are defined as
where C max stands for the saturated hydrogen density and the coefficient k depends on the stress ratio and time. In addition, the solution of Eq. [A1] can be expressed as a standard form:
We can define C(0, t) = C 0(t); thus, Eq. [A3] represents the shape of the distribution in time. Green’s function for density C(x, t) due to unit mass concentrated at (ξ, τ) can be represented as
For τ domain and x = 0, i.e., hydrogen diffused only from the crack tip,
where
Plugging Eq. [A6] into Eq. [A5] leads to
Plugging Eq. [A7] into Eq. [A6] leads to
For \( \left. {C(x,t)} \right|_{x = 0} = C_{0} (t), \) Eq. [A8] can be rewritten as
So, Eq. [A9] can be expressed as an integral equation as
Equation [A10] is a known special kind of integral equation, i.e., Volterra type of the second kind, so Eq. [A10] can be solved by using Laplace transforms and inverse Laplace transforms. The solution of the integral equation is as follows:
Finally, Eq. [A11] can be expressed simply as
The general solution of C(x, t) can be obtained by plugging Eq. [A12] into Eq. [A8] as follows, and can be solved by numerical approaches:
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Choi, BH., Chudnovsky, A. Observation and Modeling of Stress Corrosion Cracking in High Pressure Gas Pipe Steel. Metall Mater Trans A 42, 383–395 (2011). https://doi.org/10.1007/s11661-010-0384-2
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DOI: https://doi.org/10.1007/s11661-010-0384-2