diff --git a/Cantera/src/thermo/PhaseCombo_Interaction.h b/Cantera/src/thermo/PhaseCombo_Interaction.h index a14049990..8e42709f5 100644 --- a/Cantera/src/thermo/PhaseCombo_Interaction.h +++ b/Cantera/src/thermo/PhaseCombo_Interaction.h @@ -527,58 +527,12 @@ namespace Cantera { * @{ */ - //! This method returns an array of generalized concentrations - /*! - * \f$ C^a_k\f$ are defined such that \f$ a_k = C^a_k / - * C^0_k, \f$ where \f$ C^0_k \f$ is a standard concentration - * defined below and \f$ a_k \f$ are activities used in the - * thermodynamic functions. These activity (or generalized) - * concentrations are used - * by kinetics manager classes to compute the forward and - * reverse rates of elementary reactions. Note that they may - * or may not have units of concentration --- they might be - * partial pressures, mole fractions, or surface coverages, - * for example. - * - * @param c Output array of generalized concentrations. The - * units depend upon the implementation of the - * reaction rate expressions within the phase. - */ - virtual void getActivityConcentrations(doublereal* c) const; - - - /** - * The standard concentration \f$ C^0_k \f$ used to normalize - * the generalized concentration. In many cases, this quantity - * will be the same for all species in a phase - for example, - * for an ideal gas \f$ C^0_k = P/\hat R T \f$. For this - * reason, this method returns a single value, instead of an - * array. However, for phases in which the standard - * concentration is species-specific (e.g. surface species of - * different sizes), this method may be called with an - * optional parameter indicating the species. - * - * @param k species index. Defaults to zero. - */ - virtual doublereal standardConcentration(int k=0) const; - - /** - * Returns the natural logarithm of the standard - * concentration of the kth species - * - * @param k species index - */ - virtual doublereal logStandardConc(int k=0) const; - //! Get the array of non-dimensional molar-based activity coefficients at //! the current solution temperature, pressure, and solution concentration. /*! * @param ac Output vector of activity coefficients. Length: m_kk. */ virtual void getActivityCoefficients(doublereal* ac) const; - - - //@} /// @name Partial Molar Properties of the Solution