Chemistry | | | | | | | | | | | | | | | |
Moisture Transport | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Nernst-Planck Equations | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Reacting Pipe Flow | | | | | | | | | | | | | | | |
Add-on for Multiple-Species User Interface | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Reaction Engineering | | | | | | | | | | | | | | | |
Stationary Plug Flow | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Surface Reactions | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Transient | | | | | | | | | | | | | | | |
Transport of Concentrated Species | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Transport of Diluted Species | | | | | | | | | | | | | | | |
Add-on for Multiple-Species User Interface | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Transport of Diluted Species in Pipes | | | | | | | | | | | | | | | |
Add-on for Multiple-Species User Interface | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Transport of Diluted Species in Porous Media | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Laminar Flow | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time dependent | | | | | | | | | | | | | | | |
Turbulent Flow, k-epsilon | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Turbulent Flow, k-omega | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Turbulent Flow, Low-Re k-epsilon | | | | | | | | | | | | | | | |
Stationary with Initialization | | | | | | | | | | | | | | | |
Transient with Initialization | | | | | | | | | | | | | | | |
Turbulent Flow, SST | | | | | | | | | | | | | | | |
Stationary with Initialization | | | | | | | | | | | | | | | |
Transient with Initialization | | | | | | | | | | | | | | | |
Concentrated Species | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Diluted Species | | | | | | | | | | | | | | | |
Stationary | | | | | | | | | | | | | | | |
Time Dependent | | | | | | | | | | | | | | | |
Laminar Flow1 | | | | | | | | | | | | | | | |
Frozen Rotor1 | | | | | | | | | | | | | | | |
Time Dependent1 | | | | | | | | | | | | | | | |
Turbulent Flow, k-epsilon1 | | | | | | | | | | | | | | | |
Frozen Rotor1 | | | | | | | | | | | | | | | |
Time Dependent1 | | | | | | | | | | | | | | | |
Turbulent Flow, k-omega1 | | | | | | | | | | | | | | | |
Frozen Rotor1 | | | | | | | | | | | | | | | |
Time Dependent1 | | | | | | | | | | | | | | | |
Turbulent Flow, Low-Re k-epsilon1 | | | | | | | | | | | | | | | |
Frozen Rotor with Initialization1 | | | | | | | | | | | | | | | |
Transient with Initialization1 | | | | | | | | | | | | | | | |
Turbulent Flow, SST1 | | | | | | | | | | | | | | | |
Frozen Rotor with Initialization1 | | | | | | | | | | | | | | | |
Transient with Initialization1 | | | | | | | | | | | | | | | |
Axial Symmetry | | | | | | | | | | | | | | | |
Concentration | | | | | | | | | | | | | | | |
Continuity | | | | | | | | | | | | | | | |
Current Density | | | | | | | | | | | | | | | |
Current Discontinuity | | | | | | | | | | | | | | | |
Electric Insulation | | | | | | | | | | | | | | | |
Electric Potential | | | | | | | | | | | | | | | |
Electrochemical Reactions | | | | | | | | | | | | | | | |
Flux | | | | | | | | | | | | | | | |
Flux Discontinuity | | | | | | | | | | | | | | | |
Mass Fraction | | | | | | | | | | | | | | | |
Mass Outflow | | | | | | | | | | | | | | | |
Moisture Content | | | | | | | | | | | | | | | |
Moisture Flux | | | | | | | | | | | | | | | |
Moisture Source | | | | | | | | | | | | | | | |
No Flux | | | | | | | | | | | | | | | |
Open Boundary | | | | | | | | | | | | | | | |
Outflow | | | | | | | | | | | | | | | |
Periodic Condition | | | | | | | | | | | | | | | |
Reacting Boundary | | | | | | | | | | | | | | | |
Surface Equilibrium Reaction | | | | | | | | | | | | | | | |
Surface Properties | | | | | | | | | | | | | | | |
Symmetry | | | | | | | | | | | | | | | |
Thin Diffusion Barrier | | | | | | | | | | | | | | | |
Thin Impermeable Barrier | | | | | | | | | | | | | | | |
Thin Moisture Barrier | | | | | | | | | | | | | | | |
Volatilization | | | | | | | | | | | | | | | |
Inflow | | | | | | | | | | | | | | | |
Danckwerts Inflow Condition | | | | | | | | | | | | | | | |
Inflow with Mixture Specification | | | | | | | | | | | | | | | |
Densities | | | | | | | | | | | | | | | |
Mass Fractions | | | | | | | | | | | | | | | |
Molar Concentrations | | | | | | | | | | | | | | | |
Mole Fractions | | | | | | | | | | | | | | | |
Number Densities | | | | | | | | | | | | | | | |
Flux | | | | | | | | | | | | | | | |
Line Mass Source | | | | | | | | | | | | | | | |
Point Mass Source | | | | | | | | | | | | | | | |
Mixture properties, CAPE-OPEN standard | | | | | | | | | | | | | | | |
Parameter estimation1 | | | | | | | | | | | | | | | |
CHEMKIN file import of thermo- transport- and kinetic data | | | | | | | | | | | | | | | |
Surface CHEMKIN | | | | | | | | | | | | | | | |
Volume CHEMKIN | | | | | | | | | | | | | | | |
1D, 2D, Axisymmetric, and 3D Formulations | | | | | | | | | | | | | | | |
Convection and Diffusion | | | | | | | | | | | | | | | |
Electrochemical Reactions | | | | | | | | | | | | | | | |
Equilibrium Reaction | | | | | | | | | | | | | | | |
Free Flow | | | | | | | | | | | | | | | |
Generate Space-Dependent Model | | | | | | | | | | | | | | | |
Infinite Domain Modeling with Infinite Elements | | | | | | | | | | | | | | | |
Initial Values | | | | | | | | | | | | | | | |
Isotropic and Anisotropic Diffusion | | | | | | | | | | | | | | | |
Mass Based Concentrations | | | | | | | | | | | | | | | |
Migration in Electric Field | | | | | | | | | | | | | | | |
Moisture Transport in Porous Medium | | | | | | | | | | | | | | | |
Multiple-Species User Interface | | | | | | | | | | | | | | | |
Reactions | | | | | | | | | | | | | | | |
Reactive Pellet Bed | | | | | | | | | | | | | | | |
Species Source | | | | | | | | | | | | | | | |
Species, Chemical Reaction Engineering | | | | | | | | | | | | | | | |
Turbulent Mixing | | | | | | | | | | | | | | | |
Wall Mass Transfer | | | | | | | | | | | | | | | |
Effective Mass Transport Parameters | | | | | | | | | | | | | | | |
Bruggeman | | | | | | | | | | | | | | | |
User Defined | | | | | | | | | | | | | | | |
Partially Saturated Porous Media | | | | | | | | | | | | | | | |
Convection, Diffusion, Adsorption, Dispersion, and Volatilization | | | | | | | | | | | | | | | |
Porous Media Transport Properties | | | | | | | | | | | | | | | |
Convection, Diffusion, Adsorption, and Dispersion | | | | | | | | | | | | | | | |
Reactions, extended for Chemical Reaction Engineering | | | | | | | | | | | | | | | |
Automatic Kinetics Generation | | | | | | | | | | | | | | | |
Fick's Law | | | | | | | | | | | | | | | |
Knudsen Diffusion | | | | | | | | | | | | | | | |
Maxwell-Stefan | | | | | | | | | | | | | | | |
Mixture-Averaged | | | | | | | | | | | | | | | |
Hygroscopic Swelling | | | | | | | | | | | | | | | |
Solid Mechanics | | | | | | | | | | | | | | | |