Fipy and Cantera - Revision history

Admin: /* Diffusion */

2017-04-17T07:40:50Z

Diffusion

2017-04-17T07:40:26Z

Cantera Evaluation of Properties

2014-01-13T18:24:30Z

Fipy-Only Pieces

← Older revision		Revision as of 18:24, 13 January 2014
Line 241:		Line 241:

	A simple transient problem with Fipy:		A simple transient problem with Fipy:
	* [[Fipy/~~Simple_Transient_Problem~~]]		* [[Fipy/Simple Transient Problem]]
			* [[Fipy/Multiple Variable Transient Problem]]

	=0D Reaction Equation=		=0D Reaction Equation=

2014-01-13T18:08:29Z

Diffusion

← Older revision		Revision as of 18:08, 13 January 2014
Line 181:		Line 181:

	Note that if we use multicomponent diffusion coefficients, we have to specify that when we create the gas:		Note that if we use multicomponent diffusion coefficients, we have to specify that when we create the gas:

			'''Wrong:'''

	<source lang="python">		<source lang="python">
Line 212:		Line 214:
	(Did you forget to specify a transport model?)		(Did you forget to specify a transport model?)

			</source>

			'''Correct:'''

			<source lang="python">
	In [6]: g = GRI30('Multi')		In [6]: g = GRI30('Multi')

2014-01-13T18:06:12Z

Cantera Evaluation of Properties

2014-01-13T17:55:21Z

Cantera Evaluation of Properties

← Older revision		Revision as of 17:55, 13 January 2014
Line 1:		Line 1:
	=Cantera Evaluation of Properties=		=Cantera Evaluation of Properties=

	Some notes, from an algorithmic perspective, on hooking up Cantera with a finite-volume solver for computing solutions:		Some notes, from an algorithmic perspective, on hooking up Cantera with a finite-volume solver for computing solutions.

	~~[[Fipy and Cantera/Algorithm Notes]]~~

	=Fipy-Only Pieces=		=Fipy-Only Pieces=

2014-01-13T17:52:51Z

0D Reaction Equation

← Older revision		Revision as of 17:52, 13 January 2014
Line 27:		Line 27:

	[[Fipy and Cantera/Batch Reactor]]		[[Fipy and Cantera/Batch Reactor]]

			=1D Convection-Reaction Equation=

			Using Fipy+Cantera to solve the one-dimensional convection reaction equation:

			[[Fipy and Cantera/1D Convection Reaction]]

			==1D Convection-Reaction Model: Axial Profile==

			Once you can solve the one-dimensional convection reaction equation, you can reproduce an axial profile model for a PFR.

			[[Fipy and Cantera/PFR Axial Profile Model]]

	=1D Diffusion Equation=		=1D Diffusion Equation=

2014-01-13T17:50:06Z

← Older revision		Revision as of 17:50, 13 January 2014
Line 5:		Line 5:
	[[Fipy and Cantera/Algorithm Notes]]		[[Fipy and Cantera/Algorithm Notes]]

	=~~0D Reaction~~=		=Fipy-Only Pieces=

	A Fipy script that will solve ~~an ODE of the form~~:		A simple transient problem with Fipy:
			* [[Fipy/Simple_Transient_Problem]]

			=0D Reaction Equation=

			A Fipy script that will solve a very simple 0D reaction equation:

	<math>		<math>
Line 13:		Line 18:
	</math>		</math>

	~~where the~~ reaction source terms ~~are~~ computed by Cantera.		with reaction source terms computed by Cantera.

			[[Fipy and Cantera/0D Reaction]]

			==0D Reaction Model: Batch Reactor==

	~~A simple transient problem with Fipy:~~		Filpy script that solves the 0D reaction equation, as well as other governing equations, for a 0D batch reactor model.
	* [[Fipy/Simple_Transient_Problem]]

	~~Turning the simple transient problem into a reactor model with Fipy and Cantera:~~		[[Fipy and Cantera/Batch Reactor]]
	* [[Fipy and Cantera/~~0D Reaction~~]]

	=1D Diffusion=		=1D Diffusion Equation=

	A 1D diffusion problem solved by Fipy, with diffusion coefficients computed by Cantera. Illustrates how to solve a variable-diffusivity problem and sweep over the solution.		A 1D diffusion problem solved by Fipy, with diffusion coefficients computed by Cantera. Illustrates how to solve a variable-diffusivity problem and sweep over the solution.

	[[Fipy and Cantera/1D Diffusion]]		[[Fipy and Cantera/1D Diffusion]]

			==1D Diffusion Model: Boundary Value Problem==

			[[Fipy and Cantera/PFR Boundary Value Problem]]

2014-01-13T17:42:51Z

0D Reaction

← Older revision		Revision as of 17:42, 13 January 2014
Line 15:		Line 15:
	where the reaction source terms are computed by Cantera.		where the reaction source terms are computed by Cantera.

	[[Fipy and Cantera/0D Reaction]]		A simple transient problem with Fipy:
			* [[Fipy/Simple_Transient_Problem]]

			Turning the simple transient problem into a reactor model with Fipy and Cantera:
			* [[Fipy and Cantera/0D Reaction]]

	=1D Diffusion=		=1D Diffusion=

2013-12-20T22:39:56Z

← Older revision		Revision as of 22:39, 20 December 2013
Line 1:		Line 1:
			=Cantera Evaluation of Properties=

			Some notes, from an algorithmic perspective, on hooking up Cantera with a finite-volume solver for computing solutions:

			[[Fipy and Cantera/Algorithm Notes]]

	=0D Reaction=		=0D Reaction=