𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Physicochemical processes and mathematical modeling of concrete chlorination

✍ Scribed by Vagelis G. Papadakis; Michael N. Fardis; Constantinos G. Vayenas


Publisher
Elsevier Science
Year
1996
Tongue
English
Weight
761 KB
Volume
51
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

✦ Synopsis


Corrosion of steel bars in concrete may start when the concentration of free chlorine ions in the liquid phase of the pores exceeds a certain threshold level causing depassivation of the bars. The physicochemical processes of diffusion of CI-in the aqueous phase of the pores, their adsorption and binding in the solid phase of concrete and their desorption therefrom are described by a nonlinear partial differential equation for the concentration of Cl in the aqueous phase, from which that of Cl bound in the solid phase can be computed algebraically. A simple yet accurate enough approximate analytical solution is also proposed, based on the assumption of the formation of a "chlorination front" where all the absorption and binding of C1-takes place, and beyond which no effects of the ingress of Cl-from the environment are felt. Model parameters are identified through fitting to experimental results, Parametric studies allow identification of the relative importance of the various geometric, physicochemical and environmental exposure parameters.


πŸ“œ SIMILAR VOLUMES


Mathematical modeling of fluidized-bed c
✍ L. Zhou; H. Y. Sohn πŸ“‚ Article πŸ“… 1996 πŸ› American Institute of Chemical Engineers 🌐 English βš– 884 KB

A mathematical model was formulated to describe the reaction rate and the particle size distribution of solids in a Puidized bed for the chlorination of rutile by a CO/CI, mixture. The bubble assemblage model was applied to describe the gas behaLRor in the bed. The particle-size distribution in the

Mathematical modelling of electrochemica
✍ C. Andrade; J.M. Diez; A. AlamΓ‘n; C. Alonso πŸ“‚ Article πŸ“… 1995 πŸ› Elsevier Science 🌐 English βš– 815 KB

Equations to calculate the duration of electrochemical chloride 8! extraction have been proposed and solved for the case of a constant z chloride concentration in the concrete or for a concentration following the error function trend. In the case of constant initial chloride content, both potentiost