Computation times#
00:00.000 total execution time for 108 files from all galleries:
Example |
Time |
Mem (MB) |
|---|---|---|
CLib Demo ( |
00:00.000 |
0.0 |
Legacy CLib Demo ( |
00:00.000 |
0.0 |
Class BoundaryValueProblem ( |
00:00.000 |
0.0 |
LiC6 electrode ( |
00:00.000 |
0.0 |
Blasius BVP solver ( |
00:00.000 |
0.0 |
Adiabatic combustor ( |
00:00.000 |
0.0 |
Custom reactor ( |
00:00.000 |
0.0 |
Property calculation demo ( |
00:00.000 |
0.0 |
Benchmark derivative evaluations ( |
00:00.000 |
0.0 |
Example utilities ( |
00:00.000 |
0.0 |
Freely-propagating flame ( |
00:00.000 |
0.0 |
Gas phase transport properties ( |
00:00.000 |
0.0 |
Autoignition in a homogeneous reactor ( |
00:00.000 |
0.0 |
Ignition delay calculation with OpenMP ( |
00:00.000 |
0.0 |
Open Rankine cycle ( |
00:00.000 |
0.0 |
C# Application Example ( |
00:00.000 |
0.0 |
C# SoundSpeed Example ( |
00:00.000 |
0.0 |
CKLIB emulation ( |
00:00.000 |
0.0 |
Fortran 90 demo ( |
00:00.000 |
0.0 |
Fortran 77 wrapper library ( |
00:00.000 |
0.0 |
Fortran 77 demo ( |
00:00.000 |
0.0 |
Isentropic flow ( |
00:00.000 |
0.0 |
Burner-stabilized flat flame ( |
00:00.000 |
0.0 |
Catalytic combustion of a stagnation flow on a platinum surface ( |
00:00.000 |
0.0 |
Simulating growth of a diamond film by CVD ( |
00:00.000 |
0.0 |
Opposed-flow diffusion flame ( |
00:00.000 |
0.0 |
Methane/air chemical equilibrium ( |
00:00.000 |
0.0 |
Freely-propagating flame ( |
00:00.000 |
0.0 |
Constant pressure ignition with user-specified equations ( |
00:00.000 |
0.0 |
Constant volume ignition with user-specified equations ( |
00:00.000 |
0.0 |
Isentropic nozzle flow ( |
00:00.000 |
0.0 |
Lithium-ion battery ( |
00:00.000 |
0.0 |
Continuously stirred tank reactor with periodic behavior ( |
00:00.000 |
0.0 |
Nozzle with compressible flow ( |
00:00.000 |
0.0 |
Prandtl number for an equilibrium H/O gas mixture ( |
00:00.000 |
0.0 |
Prandtl number for an equilibrium H/O gas mixture ( |
00:00.000 |
0.0 |
Rankine cycle ( |
00:00.000 |
0.0 |
Adiabatic, constant pressure reactor ( |
00:00.000 |
0.0 |
Adiabatic, constant volume reactor ( |
00:00.000 |
0.0 |
Zero-dimensional reactor with surface chemistry ( |
00:00.000 |
0.0 |
Blowers-Masel reaction rates ( |
00:00.000 |
0.0 |
Custom reaction rates ( |
00:00.000 |
0.0 |
Growth of diamond film using CVD ( |
00:00.000 |
0.0 |
Extracting a sub-mechanism ( |
00:00.000 |
0.0 |
Interactive Reaction Path Diagrams ( |
00:00.000 |
0.0 |
Jet-stirred reactor temperature and species profiles ( |
00:00.000 |
0.0 |
Lithium Ion Battery Discharge Curve ( |
00:00.000 |
0.0 |
Mechanism reduction ( |
00:00.000 |
0.0 |
Viewing a reaction path diagram ( |
00:00.000 |
0.0 |
Shock-tube species profiles as a function of time ( |
00:00.000 |
0.0 |
Solid oxide fuel cell using elementary kinetics ( |
00:00.000 |
0.0 |
Laminar flame speed calculation ( |
00:00.000 |
0.0 |
Burner-stabilized flame ( |
00:00.000 |
0.0 |
Catalytic combustion of methane on platinum ( |
00:00.000 |
0.0 |
Counterflow diffusion flame ( |
00:00.000 |
0.0 |
Scaling of diffusion flames with pressure and strain rate ( |
00:00.000 |
0.0 |
Diffusion flame unstable branch ( |
00:00.000 |
0.0 |
Diffusion flame extinction strain rate ( |
00:00.000 |
0.0 |
Burner-stabilized flame with imposed temperature profile ( |
00:00.000 |
0.0 |
Saving, loading, and restarting 1D calculations ( |
00:00.000 |
0.0 |
Flame speed as a function of equivalence ratio ( |
00:00.000 |
0.0 |
Flame Speed with Convergence Analysis ( |
00:00.000 |
0.0 |
Laminar flame speed sensitivity analysis ( |
00:00.000 |
0.0 |
Burner-stabilized flame including ionized species ( |
00:00.000 |
0.0 |
Freely-propagating flame with charged species ( |
00:00.000 |
0.0 |
Opposed-flow premixed strained flame ( |
00:00.000 |
0.0 |
Symmetric premixed twin flame ( |
00:00.000 |
0.0 |
Detached flat flame stabilized at a stagnation point ( |
00:00.000 |
0.0 |
One-dimensional packed-bed, catalytic-membrane reactor ( |
00:00.000 |
0.0 |
Plug flow reactor: silicon nitride deposition ( |
00:00.000 |
0.0 |
Combustor residence time ( |
00:00.000 |
0.0 |
Continuously Stirred Tank Reactor ( |
00:00.000 |
0.0 |
Integrating constant pressure ignition using SciPy ( |
00:00.000 |
0.0 |
Using ExtensibleReactor to implement wall inertia ( |
00:00.000 |
0.0 |
Soot precursor formation with time-varying mass flow rate ( |
00:00.000 |
0.0 |
Diesel-type internal combustion engine simulation with gaseous fuel ( |
00:00.000 |
0.0 |
Mixing two streams ( |
00:00.000 |
0.0 |
Nanosecond Pulse Plasma Simulation ( |
00:00.000 |
0.0 |
Ignition delay time using the Redlich-Kwong real gas model ( |
00:00.000 |
0.0 |
Continuously stirred tank reactor with periodic behavior ( |
00:00.000 |
0.0 |
Plug flow reactor modeling approaches ( |
00:00.000 |
0.0 |
Reactors separated by a moving piston ( |
00:00.000 |
0.0 |
Plasma Reactor ( |
00:00.000 |
0.0 |
Reactor cascade model for reactive flows in inert porous media ( |
00:00.000 |
0.0 |
Acceleration of reactor integration using a sparse preconditioned solver ( |
00:00.000 |
0.0 |
Constant-pressure, adiabatic kinetics simulation ( |
00:00.000 |
0.0 |
Reactors with walls and heat transfer ( |
00:00.000 |
0.0 |
Constant-pressure, adiabatic kinetics simulation with sensitivity analysis ( |
00:00.000 |
0.0 |
Plug flow reactor with surface chemistry ( |
00:00.000 |
0.0 |
Plug flow reactor modeled as a chain of well stirred reactors ( |
00:00.000 |
0.0 |
Adiabatic flame temperature including solid carbon formation ( |
00:00.000 |
0.0 |
Surface with coverage-dependent thermo ( |
00:00.000 |
0.0 |
Critical state properties ( |
00:00.000 |
0.0 |
Non-ideal equations of state ( |
00:00.000 |
0.0 |
Equivalence ratio ( |
00:00.000 |
0.0 |
Converging-Diverging Nozzle ( |
00:00.000 |
0.0 |
Isentropic, adiabatic flow (with units) ( |
00:00.000 |
0.0 |
Mixing using Quantity objects ( |
00:00.000 |
0.0 |
EEDF calculation ( |
00:00.000 |
0.0 |
Equilibrium with charged species and multiple condensed phases ( |
00:00.000 |
0.0 |
Rankine cycle ( |
00:00.000 |
0.0 |
Rankine cycle (with units) ( |
00:00.000 |
0.0 |
Sound speeds ( |
00:00.000 |
0.0 |
Sound speeds (with units) ( |
00:00.000 |
0.0 |
Vapor Dome ( |
00:00.000 |
0.0 |
Porous media transport using the dusty gas model ( |
00:00.000 |
0.0 |
High-Pressure transport using two models ( |
00:00.000 |
0.0 |
Parallelizing transport property calculations ( |
00:00.000 |
0.0 |