TY - JOUR
T1 - Numerical simulation of micro-galvanic corrosion in Al alloys
T2 - Effect of geometric factors
AU - Yin, Litao
AU - Jin, Ying
AU - Leygraf, Christofer
AU - Birbilis, Nick
AU - Pan, Jinshan
N1 - Publisher Copyright:
© 2017 The Electrochemical Society. All rights reserved.
PY - 2017
Y1 - 2017
N2 - A finite element model for simulating the propagation of intermetallic particle driven micro-galvanic corrosion in an Al-matrix model system is presented. The model revealed dynamic changes related to localized corrosion, including the moving dissolution boundary, the deposition of reaction products (Al(OH)3), and their blocking effect. Modelling was focused on the effects of key geometric parameters, including the radius of cathodic particle (range 0.5 to 4 μm) and the width of an assumed anodic ring surrounding the particle (range 0.1 to 2 μm). Simulations revealed the dynamic flow of molecular and ionic species, along with influence of geometrical constraints. For ring widths below 0.5 μm, deposition of Al(OH)3 inside the dissolving volume was inhibited due to limited transport of OH− and O2 into a constrained volume − resulting in local acidification. An increase in cathodic particle radius at given ring width resulted in a greater dissolution by providing a larger cathodic area for O2 reduction, quantifying the effect of cathode/anode ratio. The model was also developed to include two cathodic particles to explore any interaction. The present study reveals a physicochemical model that contributes toward a framework for multi-process localized corrosion systems, which can be further adapted to commercial alloy systems.
AB - A finite element model for simulating the propagation of intermetallic particle driven micro-galvanic corrosion in an Al-matrix model system is presented. The model revealed dynamic changes related to localized corrosion, including the moving dissolution boundary, the deposition of reaction products (Al(OH)3), and their blocking effect. Modelling was focused on the effects of key geometric parameters, including the radius of cathodic particle (range 0.5 to 4 μm) and the width of an assumed anodic ring surrounding the particle (range 0.1 to 2 μm). Simulations revealed the dynamic flow of molecular and ionic species, along with influence of geometrical constraints. For ring widths below 0.5 μm, deposition of Al(OH)3 inside the dissolving volume was inhibited due to limited transport of OH− and O2 into a constrained volume − resulting in local acidification. An increase in cathodic particle radius at given ring width resulted in a greater dissolution by providing a larger cathodic area for O2 reduction, quantifying the effect of cathode/anode ratio. The model was also developed to include two cathodic particles to explore any interaction. The present study reveals a physicochemical model that contributes toward a framework for multi-process localized corrosion systems, which can be further adapted to commercial alloy systems.
UR - http://www.scopus.com/inward/record.url?scp=85033696508&partnerID=8YFLogxK
U2 - 10.1149/2.1221702jes
DO - 10.1149/2.1221702jes
M3 - Article
SN - 0013-4651
VL - 164
SP - C75-C84
JO - Journal of the Electrochemical Society
JF - Journal of the Electrochemical Society
IS - 2
ER -