Analogies between heterogeneous catalysis on solid-gas interfaces and electrochemical kinetics on solid-liquid interfaces are discussed. The surface potential of a solid-gas interface corresponds to the Galvani potential difference of a solid-liquid interface. These potentials depend to a first approximation linearly on the number of adsorbed potential-determining particles. A corresponding linear variation adsorption energy is explained on the basis of electrostatic or induced interaction between adsorbed particles. This behavior is coherent with a logarithmic dependence of the number of adsorbed particles on the bulk concentration or pressure in the liquid or gaseous phase (Temkin isotherm) and a linear dependence of the activation energy of adsorption on the number of adsorbed particles (Becker-Zeldovich equation). It is shown that the Temkin isotherm corresponds to Nernst's formula for electrode potentials and the Becker-Zeldovich equation to Volmer's equation for the rate of electrochemical reactions, and that these equations follow immediately from the theory of charge-transfer adsorption or electrostatic interaction between (activated) potential-determining species or complexes. This treatment leads to a new interpretation of the charge-transfer coefficient and of the influence of the electronic properties of the electrode material and of specifically adsorbed foreign species on hydrogen overvoltage, oxygen overvoltage, and metal deposition overvoltage.The kinetics and thermodynamics of electrochemical phenomena at solid-liquid interfaces and of catalytic phenomena at solid-gas interfaces are closely related. It is the object of this paper to point out correspondences between the two fields and to derive the fundamental laws of electrochemical thermodynamics and kinetics, in particular the Nernst equation and the Volmer-Tafel equation, from these considerations.
Adsorption and InteractionThe relation between the number of adsorbed species on a solid-gas or solid-liquid interface and bulk concentration (or pressure) of the adsorbable species is described by isotherms. The Langmuir isotherm is derived on the assumption that adsorption occurs at fixed sites and that the energy of adsorption is independent of the number of particles adsorbed. Fixed site adsorption is, however, unlikely for many reactions proceeding on electrodes and catalysts. The energy of adsorption usually decreases with increasing number of adsorbed particles. The Freundlich isotherm is therefore more likely to be obeyed since it allows for the latter effect. However, very few experimental results suggest a logarithmic decrease of the energy of adsorption with increasing number of adsorbed species, as derived from the Freundlich isotherm. Very often the energy of adsorption decreases nearly linearly with the number of adsorbed particles. Such a behavior is accounted for by the Temkin isotherm. The latter can be derived for intermediate ranges of coverage from a fixed site Langmuir-type isotherm by allowing for a linear variation in adsorpt...