Review the basic principles of electrochemical reactions
Compare anodic and cathodic processes
Discuss the importance of surface area ratio between anodic and cathodic processes
Describe Faraday’s Law and discuss its relation to corrosion rate measurements
This Module consists of six Web pages of required reading. The pagination is visible at the bottom of each page with direct links to adjacent pages.
Additional information can be found in sections 3.1, 3.2, 3.3, 3.4 and 3.5 of the reference textbook (Corrosion Engineering: Principles and Practice).
While corrosion can take any one of the several forms, the mechanism of attack in aqueous environments will involve some aspect of electrochemistry. There will be a flow of electrons from certain areas of a metal surface to other areas through an environment capable of conducting ions.
Ulick R. Evans, the British scientist who is considered by many as the "Father of Corrosion Science", has said that "Corrosion is largely an electrochemical phenomenon, [which] may be defined as destruction by electrochemical or chemical agencies...".
Corrosion in an aqueous environment and in an atmospheric environment is an electrochemical process because corrosion involves the transfer of electrons between a metal surface and an aqueous electrolyte solution. It results from the overwhelming tendency of metals to react electrochemically with oxygen, water, and other substances in the aqueous environment. In this context, the term anode is used to describe that portion of the metal surface that is actually corroding while the term cathode is used to describe the metal surface that consumes the electrons produced by the corrosion reaction. (reference)
An electrochemical reaction is defined as a chemical reaction involving the transfer of electrons. It is also a chemical reaction which involves oxidation and reduction. Since metallic corrosion is almost always an electrochemical process, it is important to understand the basic nature of electrochemical reactions. The discoveries that gradually evolved in modern corrosion science have, in fact, played an important role in the development of a multitude of technologies we are enjoying today. These principles are illustrated with the use of
These principles are illustrated with the use ofa Daniell cell in which copper and zinc metals are immersed in solutions of their respective sulfates. The Daniell cell was the first truly practical and reliable electric battery that supported many nineteenth century electrical innovations such as the telegraph.
The fact that corrosion consists of at least one oxidation and one reduction reaction is not always as obvious as it is in batteries. The two reactions are often combined on a single piece of metal as illustrated schematically here for a piece of steel and in the following Figure for a piece of zinc immersed in an acidic solution.
and in the following Figure for a piece of zinc immersed in an acidic solution.
Electrochemical reactions occurring during the corrosion of zinc in air-free hydrochloric acid
In this Figure, a piece of zinc immersed in hydrochloric acid solution is undergoing corrosion. At some point on the surface, zinc is
These equations illustrate the nature of an electrochemical reaction for zinc. During such a reaction, electrons are transferred, or, viewing it another way, an oxidation process occurs together with a reduction process. The overall corrosion processes are summarized in the following equation:
Briefly then, for corrosion to occur there must be a formation of ions and release of electrons at an anodic surface where oxidation or deterioration of the metal occurs. There must be a simultaneous acceptance at the cathodic surface of the electrons generated at the anode. This acceptance of electrons can take the form of neutralization of positive hydrogen ions, or the formation of negative ions. The anodic and cathodic reactions must go on at the same time and at equivalent rates. However, corrosion occurs only at the areas that serve as anodes.
|(previous)||Page 1 of 6||(next)|
See also CCE 513: Corrosion Engineering