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[Doc] Correct title of "Chemically Reacting Flow"

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This commit is contained in:
Ray Speth 2015-01-15 21:15:12 +00:00
parent ad1cd8c7bb
commit 217a001a08
3 changed files with 7 additions and 6 deletions
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5
include/cantera/transport/MixTransport.h
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@ -17,8 +17,9 @@ namespace Cantera
{
//! Class MixTransport implements mixture-averaged transport properties for ideal gas mixtures.
/*!
* The model is based on that described by Kee, Coltrin, and Glarborg,
* "Theoretical and Practical Aspects of Chemically Reacting Flow Modeling."
* The model is based on that described in: R. J. Kee, M. J. Coltrin, and P.
* Glarborg, "Chemically Reacting Flow: Theory & Practice", John Wiley & Sons,
* 2003.
*
* The viscosity is computed using the Wilke mixture rule (kg /m /s)
*

6
include/cantera/transport/MultiTransport.h
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@ -17,9 +17,9 @@ namespace Cantera
//! Class MultiTransport implements multicomponent transport properties for
//! ideal gas mixtures.
/*!
* The implementation generally follows the procedure outlined in Kee,
* Coltrin, and Glarborg, "Theoretical and Practical Aspects of Chemically
* Reacting Flow Modeling," Wiley Interscience.
* The implementation generally follows the procedure outlined in: R. J. Kee, M.
* J. Coltrin, and P. Glarborg, "Chemically Reacting Flow: Theory & Practice",
* John Wiley & Sons, 2003.
*
* @ingroup tranprops
*/

2
samples/matlab/tut6.m
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@ -19,7 +19,7 @@
% Currently, two models are implemented. Both are based on kinetic
% theory expressions, and follow the approach described in Dixon-Lewis
% (1968) and Kee, Coltrin, and Glarborg (2002). The first is a full
% (1968) and Kee, Coltrin, and Glarborg (2003). The first is a full
% multicomponent formulation, and the second is a simplification that
% uses expressions derived for mixtures with a small number of species
% (1 to 3), using approximate mixture rules to average over