We describe a new vector discrete ordinate radiative transfer model with a full linearization facility.
The problem is solved using a three-dimensional conjugate heat transfer model with counterflow between upper and lower channels.
The melt depth and duration are predicted with a transient, two-dimensional axisymmetric heat transfer model with temperature-dependent material properties.
A heat transfer model with a cylindrical surface heat source has been developed under the assumption of the keyhole per thin layer being cylindrical.
A previously validated one-dimensional pressure drop and heat transfer model, with water as the working fluid, is employed as the objective function.
The DFT results are compared with predictions of an analytical single electron transfer model with quadratic reactant and product free energy surfaces.
A linear driving force mass transfer model with a variable lumped-resistances coefficient was found to provide an acceptable fit to the experimental data.
A combined kinetic mass transfer model with concentration-dependent diffusion (parabolic form) has been developed and successfully applied on the dissolved oxygen adsorption system at high surface coverage.
The results indicate that the commonly-used linear mobile immobile transfer model with its transfer rate coefficient proportional to water content cannot fit the memory function calculated at any saturation.
Hole mobilities in the amorphous phase were evaluated for 12 kinds of molecules using the novel successive conduction (SC) model based on the simple sequential transfer model with no adjustable parameter.
