Porter's approach
The Porter approach , named after Alfred William Porter (1863–1939), is the simplest model for calculating activity coefficients and can be derived exactly from the Gibbs-Duhem equation . It has the advantage that it only requires a single parameter A.
G E = RTAx1x2
However, it has the disadvantage that it represents a symmetrical function and has no meaning in reality because it is too imprecise. After all, this model can even be used for two liquid phases, i.e. H. Segregation, represent.
literature
- Alfred William Porter: The Vapor-Pressures of Mixtures , Trans. Faraday Soc. 16 (1920), p. 336
- Alfred William Porter: Thermodynamics , Methuen (1931)
- Dorothea Lüdecke, Christa Lüdecke: Thermodynamics: Physico-chemical basics of thermal process engineering. Jumper; Berlin, Heidelberg 2000, p. 506. ISBN 9783540668053
Individual evidence
- ^ Library of Congress: Albert William Porter .