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Effective diffusion coefficient discrete phase

Taylor (T4, T6), in two other articles, used the dispersed plug-flow model for turbulent flow, and Aris s treatment also included this case. Taylor and Aris both conclude that an effective axial-dispersion coefficient Dzf can again be used and that this coefficient is now a function of the well known Fanning friction factor. Tichacek et al. (T8) also considered turbulent flow, and found that Dl was quite sensitive to variations in the velocity profile. Aris further used the method for dispersion in a two-phase system with transfer between phases (All), for dispersion in flow through a tube with stagnant pockets (AlO), and for flow with a pulsating velocity (A12). Hawthorn (H7) considered the temperature effect of viscosity on dispersion coefficients he found that they can be altered by a factor of two in laminar flow, but that there is little effect for fully developed turbulent flow. Elder (E4) has considered open-channel flow and diffusion of discrete particles. Bischoff and Levenspiel (B14) extended Aris s theory to include a linear rate process, and used the results to construct comprehensive correlations of dispersion coefficients. [Pg.135]

In this equation, fis the number of orthogonal directions relevant for the spin diffusion process. Its value depends on morphology and is 1 for lamellar block copolymers, 2 for phases with a cylinder-like morphology in a matrix, and 3 for discrete phases (for example spheres in a matrix). The remaining parameter in Eq. 1 is Deff. the effective spin diffusion coefficient. It can be calculated according to Eq. 2. [Pg.340]


See other pages where Effective diffusion coefficient discrete phase is mentioned: [Pg.76]    [Pg.68]    [Pg.185]    [Pg.185]    [Pg.529]    [Pg.284]    [Pg.117]   


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