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Dynamic equilibrium steels

Fig. 9.3.15 Analysis nf a section from a conveyor bell with steel cords by the CPMG method starting from thermodynamic equilibrium and from dynamic equilibrium corresponding to partial. saturation, (a) Sketch of the sample and positions of measurements, (b) The transverse relasaiion times for one side of the belt reveal homogeneous matcriat. (c) The transverse relaxation limes for the other side indicate considerable inhomogeneity. Fig. 9.3.15 Analysis nf a section from a conveyor bell with steel cords by the CPMG method starting from thermodynamic equilibrium and from dynamic equilibrium corresponding to partial. saturation, (a) Sketch of the sample and positions of measurements, (b) The transverse relasaiion times for one side of the belt reveal homogeneous matcriat. (c) The transverse relaxation limes for the other side indicate considerable inhomogeneity.
W. Rudszinski, W. A. Steele, G. Zgrablieh, eds. Equilibrium and Dynamics of Gas Adsorption on Heterogeneous Solid Surfaces. Amsterdam Elsevier, 1997. [Pg.477]

The following five chapters deal with problems associated with solid phases, in some cases involving surface and interfacial problems. In Chapter 14, Steele presents a review of physical adsorption investigated by MD techniques. Jiang and Belak describe in Chapter 15 the simulated behavior of thin films confined between walls under the effect of shear. Chapter 16 contains a review by Benjamin of the MD equilibrium and non-equilibrium simulations applied to the study of chemical reactions at interfaces. Chapter 17 by Alper and Politzer presents simulations of solid copper, and methodological differences of these simulations compared to those in the liquid phase are presented. In Chapter 18 Gelten, van Santen, and Jansen discuss the application of a dynamic Monte Carlo method for the treatment of chemical reactions on surfaces with emphasis on catalysis problems. Khakhar in... [Pg.78]

The rate of corrosion process will depend on the conductivity of electrolyte and the difference of potential between the anode and cathode. Particularly the oxygen access, necessary for the cathodic reaction, can be the factor limiting the rate of corrosion [98]. Simultaneously, as a result of corrosion current, the polarization of electrodes occurs (their potentials increase in respect to the equilibrium potential values) and the dynamically maintained potential value has the deciding effect on the corrosion rate. In the case of steel in paste environment strong polarization of anodic microareas occurs, which increase anodic potential, decreasing the difference of potential in respect to cathode therefore, as it results from the curves in E -pH system, the passivation of steel due to the oxides film occurs [98]. [Pg.481]

MacElroy, J. M. D., Seaton, N. A., and Friedman, S. P. (1997) Sorption rate processes in carbon molecular sieves. In Equilibrium and Dynamics of Gas Adsorption on Heterogeneous Solid Surfaces. (W. Rudzinski, W. A. Steele, and G. Zgrablich, ed ). Studies in Surface Sci. and Catal., Col. 104. Elsevier, Amstedam, The Netherlands. [Pg.126]

Equations (7) and (10) generalize the Kirkwood-Frohlich equilibrium theory to the dynamic situation. The correlation function approach to dielectric relaxation was first made by Glarum (37) and was extended by Cole (38) and by Steele (39). [Pg.245]

Corrosion of steel in water above about pH 6.0 is due to the presence of dissolved oxygen, which depolarizes the cathodic reaction and increases corrosion. Neutral water of low salt content in equilibrium with air at 21 °C (70 °F) will contain about 8 ppm of dissolved oxygen. The concentration of oxygen decreases with increasing salt concentration and increasing temperature. Only 0.1 ppm of oxygen is required to increase corrosion rates seriously in a dynamic system. [Pg.132]


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See also in sourсe #XX -- [ Pg.233 , Pg.235 ]




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