The approximation provides a quantitatively correct description of the effect of the adsorption isotherm for parallel pore and solid diffusion as well as of the effect of a variable adsorbed-phase diffusivity.
The permeability, sorption and diffusivity of these materials are reported, and activation energies of permeation and diffusion as well as heats of sorption for gases CO2, CH4, O2, and N2 of these materials are compared.
In the model, calcium diffusion as well as buffering of calcium by fixed endogenous buffers and diffusible indicator were included and spine and dendrite were respectively modeled as sphere and cylinder (Fig. 3A).
These new interpolation kernels incorporate diffusion as well as remeshing.
Moreover, the construct should facilitate nutrients and oxygen diffusion as well as removal of metabolic waste during tissue regeneration.
This explains regional differences in the diffusion as well as variations in the design and operation of biogas plants.
Specifically, this paper investigates alternative methods for integrating diffusion as well as extending the model to nonhydrostatic flow.
Simple adaptive techniques are employed in solving the adatom diffusion as well as the boundary motion problem.
An improved MLP version (MLPld, low diffusion) as well as an analysis of its capabilities and limitations are given.
Using these data, it was possible to visually discriminate between a film subject only to diffusion and a film subject to diffusion as well as osmotic effects.
Our computations account for grain boundary sliding, grain boundary diffusion, grain boundary migration, and surface diffusion, as well as thermally activated dislocation creep within the grains themselves.
