MolalityVPSSTP.h

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/**
 *  @file MolalityVPSSTP.h
 *   Header for intermediate ThermoPhase object for phases which
 *   employ molality based activity coefficient formulations
 *  (see \ref thermoprops
 * and class \link Cantera::MolalityVPSSTP MolalityVPSSTP\endlink).
 *
 * Header file for a derived class of ThermoPhase that handles
 * variable pressure standard state methods for calculating
 * thermodynamic properties that are further based upon activities
 * based on the molality scale.  These include most of the methods for
 * calculating liquid electrolyte thermodynamics.
 */
 
// This file is part of Cantera. See License.txt in the top-level directory or
// at https://cantera.org/license.txt for license and copyright information.
 
#ifndef CT_MOLALITYVPSSTP_H
#define CT_MOLALITYVPSSTP_H
 
#include "VPStandardStateTP.h"
 
namespace Cantera
{
 
/*!
 * MolalityVPSSTP is a derived class of ThermoPhase that handles variable
 * pressure standard state methods for calculating thermodynamic properties that
 * are further based on molality-scaled activities. This category incorporates
 * most of the methods for calculating liquid electrolyte thermodynamics that
 * have been developed since the 1970's.
 *
 * This class adds additional functions onto the ThermoPhase interface that
 * handle molality based standard states. The ThermoPhase class includes a
 * member function, ThermoPhase::activityConvention() that indicates which
 * convention the activities are based on. The default is to assume activities
 * are based on the molar convention. However, classes which derive from the
 * MolalityVPSSTP class return `cAC_CONVENTION_MOLALITY` from this member
 * function.
 *
 * The molality of a solute, \f$ m_i \f$, is defined as
 *
 * \f[
 *     m_i = \frac{n_i}{\tilde{M}_o n_o}
 * \f]
 * where
 * \f[
 *     \tilde{M}_o = \frac{M_o}{1000}
 * \f]
 *
 * where \f$ M_o \f$ is the molecular weight of the solvent. The molality has
 * units of gmol/kg. For the solute, the molality may be considered
 * as the amount of gmol's of solute per kg of solvent, a natural experimental
 * quantity.
 *
 * The formulas for calculating mole fractions if given the molalities of the
 * solutes is stated below. First calculate \f$ L^{sum} \f$, an intermediate
 * quantity.
 *
 * \f[
 *     L^{sum} = \frac{1}{\tilde{M}_o X_o} = \frac{1}{\tilde{M}_o} + \sum_{i\ne o} m_i
 * \f]
 * Then,
 * \f[
 *     X_o =   \frac{1}{\tilde{M}_o L^{sum}}
 * \f]
 * \f[
 *     X_i =   \frac{m_i}{L^{sum}}
 * \f]
 * where \f$ X_o \f$ is the mole fraction of solvent, and \f$ X_o \f$ is the
 * mole fraction of solute *i*. Thus, the molality scale and the mole fraction
 * scale offer a one-to-one mapping between each other, except in the limit of a
 * zero solvent mole fraction.
 *
 * The standard states for thermodynamic objects that derive from MolalityVPSSTP
 * are on the unit molality basis. Chemical potentials of the solutes, \f$ \mu_k
 * \f$, and the solvent, \f$ \mu_o \f$, which are based on the molality form,
 * have the following general format:
 *
 * \f[
 *    \mu_k = \mu^{\triangle}_k(T,P) + R T ln(\gamma_k^{\triangle} \frac{m_k}{m^\triangle})
 * \f]
 * \f[
 *    \mu_o = \mu^o_o(T,P) + RT ln(a_o)
 * \f]
 *
 * where \f$ \gamma_k^{\triangle} \f$ is the molality based activity coefficient
 * for species \f$k\f$.
 *
 * The chemical potential of the solvent is thus expressed in a different format
 * than the chemical potential of the solutes. Additionally, the activity of the
 * solvent, \f$ a_o \f$, is further reexpressed in terms of an osmotic
 * coefficient, \f$ \phi \f$.
 * \f[
 *     \phi = \frac{- ln(a_o)}{\tilde{M}_o \sum_{i \ne o} m_i}
 * \f]
 *
 * MolalityVPSSTP::osmoticCoefficient() returns the value of \f$ \phi \f$. Note
 * there are a few of definitions of the osmotic coefficient floating around. We
 * use the one defined in (Activity Coefficients in Electrolyte Solutions, K. S.
 * Pitzer CRC Press, Boca Raton, 1991, p. 85, Eqn. 28). This definition is most
 * clearly related to theoretical calculation.
 *
 * The molar-based activity coefficients \f$ \gamma_k \f$ may be calculated from
 * the molality-based activity coefficients, \f$ \gamma_k^\triangle \f$ by the
 * following formula.
 * \f[
 *     \gamma_k = \frac{\gamma_k^\triangle}{X_o}
 * \f]
 * For purposes of establishing a convention, the molar activity coefficient of
 * the solvent is set equal to the molality-based activity coefficient of the
 * solvent:
 * \f[
 *     \gamma_o = \gamma_o^\triangle
 * \f]
 *
 * The molality-based and molarity-based standard states may be related to one
 * another by the following formula.
 *
 * \f[
 *   \mu_k^\triangle(T,P) = \mu_k^o(T,P) + R T \ln(\tilde{M}_o m^\triangle)
 * \f]
 *
 * An important convention is followed in all routines that derive from
 * MolalityVPSSTP. Standard state thermodynamic functions and reference state
 * thermodynamic functions return the molality-based quantities. Also all
 * functions which return activities return the molality-based activities. The
 * reason for this convention has been discussed in supporting memos. However,
 * it's important because the term in the equation above is non-trivial. For
 * example it's equal to 2.38 kcal/gmol for water at 298 K.
 *
 * In order to prevent a singularity, this class includes the concept of a
 * minimum value for the solvent mole fraction. All calculations involving the
 * formulation of activity coefficients and other non-ideal solution behavior
 * adhere to this concept of a minimal value for the solvent mole fraction. This
 * makes sense because these solution behavior were all designed and measured
 * far away from the zero solvent singularity condition and are not applicable
 * in that limit.
 *
 * This objects add a layer that supports molality. It inherits from
 * VPStandardStateTP.
 *
 * All objects that derive from this are assumed to have molality based standard
 * states.
 *
 * Molality based activity coefficients are scaled according to the current pH
 * scale. See the Eq3/6 manual for details.
 *
 * Activity coefficients for species k may be altered between scales s1 to s2
 * using the following formula
 *
 * \f[
 *     ln(\gamma_k^{s2}) = ln(\gamma_k^{s1})
 *        + \frac{z_k}{z_j} \left(  ln(\gamma_j^{s2}) - ln(\gamma_j^{s1}) \right)
 * \f]
 *
 * where j is any one species. For the NBS scale, j is equal to the Cl- species
 * and
 *
 * \f[
 *     ln(\gamma_{Cl-}^{s2}) = \frac{-A_{\phi} \sqrt{I}}{1.0 + 1.5 \sqrt{I}}
 * \f]
 *
 * The Pitzer scale doesn't actually change anything. The pitzer scale is
 * defined as the raw unscaled activity coefficients produced by the underlying
 * objects.
 *
 * ### SetState Strategy
 *
 * The MolalityVPSSTP object does not have a setState strategy concerning the
 * molalities. It does not keep track of whether the molalities have changed.
 * It's strictly an interfacial layer that writes the current mole fractions to
 * the State object. When molalities are needed it recalculates the molalities
 * from the State object's mole fraction vector.
 *
 * @todo Make two solvent minimum fractions. One would be for calculation of the
 *       non-ideal factors. The other one would be for purposes of stoichiometry
 *       evaluation. the stoichiometry evaluation one would be a 1E-13 limit.
 *       Anything less would create problems with roundoff error.
 */
class MolalityVPSSTP : public VPStandardStateTP
{
public:
    /// Default Constructor
    /*!
     * This doesn't do much more than initialize constants with default values
     * for water at 25C. Water molecular weight comes from the default
     * elements.xml file. It actually differs slightly from the IAPWS95 value of
     * 18.015268. However, density conservation and therefore element
     * conservation is the more important principle to follow.
     */
    MolalityVPSSTP();
 
    //! @name  Utilities
    //! @{
 
    //! String indicating the mechanical phase of the matter in this Phase.
    /*!
     * All derived phases from `MolalityVPSSTP` always represent liquids.
     */
    virtual std::string phaseOfMatter() const {
        return "liquid";
    }
 
    //! Set the pH scale, which determines the scale for single-ion activity
    //! coefficients.
    /*!
     * Single ion activity coefficients are not unique in terms of the
     * representing actual measurable quantities.
     *
     * @param pHscaleType  Integer representing the pHscale
     */
    void setpHScale(const int pHscaleType);
 
    //! Reports the pH scale, which determines the scale for single-ion activity
    //! coefficients.
    /*!
     * Single ion activity coefficients are not unique in terms of the
     * representing actual measurable quantities.
     *
     * @returns the pHscale type
     */
    int pHScale() const;
 
    //! @}
    //! @name Utilities for Solvent ID and Molality
    //! @{
 
    /**
     * Sets the minimum mole fraction in the molality formulation. Note the
     * molality formulation is singular in the limit that the solvent mole
     * fraction goes to zero. Numerically, how this limit is treated and
     * resolved is an ongoing issue within Cantera. The minimum mole fraction
     * must be in the range 0 to 0.9.
     *
     * @param xmolSolventMIN  Input double containing the minimum mole fraction
     */
    void setMoleFSolventMin(doublereal xmolSolventMIN);
 
    //! Returns the minimum mole fraction in the molality formulation.
    doublereal moleFSolventMin() const;
 
    //! Calculates the molality of all species and stores the result internally.
    /*!
     * We calculate the vector of molalities of the species in the phase and
     * store the result internally:
     * \f[
     *     m_i = \frac{X_i}{1000 * M_o * X_{o,p}}
     * \f]
     * where
     *    - \f$ M_o \f$ is the molecular weight of the solvent
     *    - \f$ X_o \f$ is the mole fraction of the solvent
     *    - \f$ X_i \f$ is the mole fraction of the solute.
     *    - \f$ X_{o,p} = \max (X_{o}^{min}, X_o) \f$
     *    - \f$ X_{o}^{min} \f$ = minimum mole fraction of solvent allowed
     *              in the denominator.
     */
    void calcMolalities() const;
 
    //! This function will return the molalities of the species.
    /*!
     * We calculate the vector of molalities of the species in the phase
     * \f[
     *     m_i = \frac{X_i}{1000 * M_o * X_{o,p}}
     * \f]
     * where
     *    - \f$ M_o \f$ is the molecular weight of the solvent
     *    - \f$ X_o \f$ is the mole fraction of the solvent
     *    - \f$ X_i \f$ is the mole fraction of the solute.
     *    - \f$ X_{o,p} = \max (X_{o}^{min}, X_o) \f$
     *    - \f$ X_{o}^{min} \f$ = minimum mole fraction of solvent allowed
     *              in the denominator.
     *
     * @param molal       Output vector of molalities. Length: m_kk.
     */
    void getMolalities(doublereal* const molal) const;
 
    //! Set the molalities of the solutes in a phase
    /*!
     * Note, the entry for the solvent is not used. We are supplied with the
     * molalities of all of the solute species. We then calculate the mole
     * fractions of all species and update the ThermoPhase object.
     * \f[
     *     m_i = \frac{X_i}{M_o/1000 * X_{o,p}}
     * \f]
     * where
     *    -  \f$M_o\f$ is the molecular weight of the solvent
     *    -  \f$X_o\f$ is the mole fraction of the solvent
     *    -  \f$X_i\f$ is the mole fraction of the solute.
     *    -  \f$X_{o,p} = \max(X_o^{min}, X_o)\f$
     *    -  \f$X_o^{min}\f$ = minimum mole fraction of solvent allowed
     *                     in the denominator.
     *
     * The formulas for calculating mole fractions are
     * \f[
     *     L^{sum} = \frac{1}{\tilde{M}_o X_o} = \frac{1}{\tilde{M}_o} + \sum_{i\ne o} m_i
     * \f]
     * Then,
     * \f[
     *     X_o =   \frac{1}{\tilde{M}_o L^{sum}}
     * \f]
     * \f[
     *     X_i =   \frac{m_i}{L^{sum}}
     * \f]
     * It is currently an error if the solvent mole fraction is attempted to be
     * set to a value lower than \f$ X_o^{min} \f$.
     *
     * @param molal   Input vector of molalities. Length: m_kk.
     */
    void setMolalities(const doublereal* const molal);
 
    //! Set the molalities of a phase
    /*!
     * Set the molalities of the solutes in a phase. Note, the entry for the
     * solvent is not used.
     *
     * @param xMap  Composition Map containing the molalities.
     */
    void setMolalitiesByName(const compositionMap& xMap);
 
    //! Set the molalities of a phase
    /*!
     * Set the molalities of the solutes in a phase. Note, the entry for the
     * solvent is not used.
     *
     * @param name  String containing the information for a composition map.
     */
    void setMolalitiesByName(const std::string& name);
 
    /**
     * @}
     * @name Activities, Standard States, and Activity Concentrations
     *
     * The activity \f$a_k\f$ of a species in solution is related to the
     * chemical potential by \f[ \mu_k = \mu_k^0(T) + \hat R T \log a_k. \f] The
     * quantity \f$\mu_k^0(T,P)\f$ is the chemical potential at unit activity,
     * which depends only on temperature and pressure.
     * @{
     */
 
    /**
     *  We set the convention to molality here.
     */
    int activityConvention() const;
 
    virtual void getActivityConcentrations(doublereal* c) const;
    virtual doublereal standardConcentration(size_t k=0) const;
 
    //! Get the array of non-dimensional activities (molality based for this
    //! class and classes that derive from it) at the current solution
    //! temperature, pressure, and solution concentration.
    /*!
     * All standard state properties for molality-based phases are evaluated
     * consistent with the molality scale. Therefore, this function must return
     * molality-based activities.
     *
     * \f[
     *     a_i^\triangle = \gamma_k^{\triangle} \frac{m_k}{m^\triangle}
     * \f]
     *
     * This function must be implemented in derived classes.
     *
     * @param ac     Output vector of molality-based activities. Length: m_kk.
     */
    virtual void getActivities(doublereal* ac) const;
 
    //! Get the array of non-dimensional activity coefficients at
    //! the current solution temperature, pressure, and solution concentration.
    /*!
     * These are mole-fraction based activity coefficients. In this
     * object, their calculation is based on translating the values
     * of the molality-based activity coefficients.
     *  See Denbigh p. 278 for a thorough discussion.
     *
     * The molar-based activity coefficients \f$ \gamma_k \f$ may be calculated
     * from the molality-based activity coefficients, \f$ \gamma_k^\triangle \f$
     * by the following formula.
     * \f[
     *     \gamma_k = \frac{\gamma_k^\triangle}{X_o}
     * \f]
     *
     * For purposes of establishing a convention, the molar activity coefficient of the
     * solvent is set equal to the molality-based activity coefficient of the
     * solvent:
     *
     * \f[
     *     \gamma_o = \gamma_o^\triangle
     * \f]
     *
     * Derived classes don't need to overload this function. This function is
     * handled at this level.
     *
     * @param ac  Output vector containing the mole-fraction based activity
     *            coefficients. length: m_kk.
     */
    virtual void getActivityCoefficients(doublereal* ac) const;
 
    //! Get the array of non-dimensional molality based activity coefficients at
    //! the current solution temperature, pressure, and solution concentration.
    /*!
     * See Denbigh p. 278 for a thorough discussion. This class must be
     * overridden in classes which derive from MolalityVPSSTP. This function
     * takes over from the molar-based activity coefficient calculation,
     * getActivityCoefficients(), in derived classes.
     *
     * These molality based activity coefficients are scaled according to the
     * current pH scale. See the Eq3/6 manual for details.
     *
     * Activity coefficients for species k may be altered between scales s1 to
     * s2 using the following formula
     *
     * \f[
     *     ln(\gamma_k^{s2}) = ln(\gamma_k^{s1})
     *        + \frac{z_k}{z_j} \left(  ln(\gamma_j^{s2}) - ln(\gamma_j^{s1}) \right)
     * \f]
     *
     * where j is any one species. For the NBS scale, j is equal to the Cl-
     * species and
     *
     * \f[
     *     ln(\gamma_{Cl-}^{s2}) = \frac{-A_{\phi} \sqrt{I}}{1.0 + 1.5 \sqrt{I}}
     * \f]
     *
     * @param acMolality Output vector containing the molality based activity
     *                   coefficients. length: m_kk.
     */
    virtual void getMolalityActivityCoefficients(doublereal* acMolality) const;
 
    //! Calculate the osmotic coefficient
    /*!
     * \f[
     *     \phi = \frac{- ln(a_o)}{\tilde{M}_o \sum_{i \ne o} m_i}
     * \f]
     *
     * Note there are a few of definitions of the osmotic coefficient floating
     * around. We use the one defined in (Activity Coefficients in Electrolyte
     * Solutions, K. S. Pitzer CRC Press, Boca Raton, 1991, p. 85, Eqn. 28).
     * This definition is most clearly related to theoretical calculation.
     *
     *  units = dimensionless
     */
    virtual double osmoticCoefficient() const;
 
    //@}
 
    //! Set equation of state parameter values from XML entries.
    /*!
     * This method is called by function importPhase() when processing a phase
     * definition in an input file. It should be overloaded in subclasses to set
     * any parameters that are specific to that particular phase model.
     *
     * The MolalityVPSSTP object defines a new method for setting the
     * concentrations of a phase. The new method is defined by a block called
     * "soluteMolalities". If this block is found, the concentrations within
     * that phase are set to the "name":"molalities pairs found within that XML
     * block. The solvent concentration is then set to everything else.
     *
     * The function first calls the overloaded function,
     * VPStandardStateTP::setStateFromXML(), to pick up the parent class
     * behavior.
     *
     * usage: Overloaded functions should call this function before carrying out
     *        their own behavior.
     *
     * @param state An XML_Node object corresponding to the "state" entry for
     *              this phase in the input file.
     *
     * @deprecated The XML input format is deprecated and will be removed in
     *     Cantera 3.0.
     */
    virtual void setStateFromXML(const XML_Node& state);
 
    //@}
    //! @name Initialization
    /// The following methods are used in the process of constructing the phase
    /// and setting its parameters from a specification in an input file. They
    /// are not normally used in application programs. To see how they are used,
    /// see importPhase().
    //@{
 
    virtual bool addSpecies(shared_ptr<Species> spec);
    virtual void initThermo();
 
    //@}
 
    //! Set the temperature (K), pressure (Pa), and molalities
    //!(gmol kg-1) of the solutes
    /*!
     * @param t           Temperature (K)
     * @param p           Pressure (Pa)
     * @param molalities  Input vector of molalities of the solutes.
     *                    Length: m_kk.
     */
    void setState_TPM(doublereal t, doublereal p,
                      const doublereal* const molalities);
 
    //! Set the temperature (K), pressure (Pa), and molalities.
    /*!
     * @param t           Temperature (K)
     * @param p           Pressure (Pa)
     * @param m           compositionMap containing the molalities
     */
    void setState_TPM(doublereal t, doublereal p, const compositionMap& m);
 
    //! Set the temperature (K), pressure (Pa), and molalities.
    /*!
     * @param t           Temperature (K)
     * @param p           Pressure (Pa)
     * @param m           String which gets translated into a composition
     *                    map for the molalities of the solutes.
     */
    void setState_TPM(doublereal t, doublereal p, const std::string& m);
 
    //! @copydoc ThermoPhase::setState
    /*!
     * Additionally uses the keys `molalities` or `M` to set the molalities.
     */
    virtual void setState(const AnyMap& state);
 
    virtual void getdlnActCoeffdlnN(const size_t ld, doublereal* const dlnActCoeffdlnN) {
        getdlnActCoeffdlnN_numderiv(ld, dlnActCoeffdlnN);
    }
 
    virtual std::string report(bool show_thermo=true,
                               doublereal threshold=1e-14) const;
 
protected:
    virtual void getCsvReportData(std::vector<std::string>& names,
                                  std::vector<vector_fp>& data) const;
 
    //! Get the array of unscaled non-dimensional molality based activity
    //! coefficients at the current solution temperature, pressure, and solution
    //! concentration.
    /*!
     * See Denbigh p. 278 for a thorough discussion. This class must be
     * overridden in classes which derive from MolalityVPSSTP. This function
     * takes over from the molar-based activity coefficient calculation,
     * getActivityCoefficients(), in derived classes.
     *
     * @param acMolality Output vector containing the molality based activity
     *                   coefficients. length: m_kk.
     */
    virtual void getUnscaledMolalityActivityCoefficients(doublereal* acMolality) const;
 
    //! Apply the current phScale to a set of activity Coefficients or
    //! activities
    /*!
     * See the Eq3/6 Manual for a thorough discussion.
     *
     * @param acMolality input/Output vector containing the molality based
     *                   activity coefficients. length: m_kk.
     */
    virtual void applyphScale(doublereal* acMolality) const;
 
private:
    //! Returns the index of the Cl- species.
    /*!
     * The Cl- species is special in the sense that its single ion molality-
     * based activity coefficient is used in the specification of the pH scale
     * for single ions. Therefore, we need to know what species index is Cl-. If
     * the species isn't in the species list then this routine returns -1, and
     * we can't use the NBS pH scale.
     *
     * Right now we use a restrictive interpretation. The species must be named
     * "Cl-". It must consist of exactly one Cl and one E atom.
     */
    virtual size_t findCLMIndex() const;
 
protected:
    //! Scaling to be used for output of single-ion species activity
    //! coefficients.
    /*!
     * Index of the species to be used in the single-ion scaling law. This is
     * the identity of the Cl- species for the PHSCALE_NBS scaling. Either
     * PHSCALE_PITZER or PHSCALE_NBS
     */
    int m_pHScalingType;
 
    //! Index of the phScale species
    /*!
     * Index of the species to be used in the single-ion scaling law. This is
     * the identity of the Cl- species for the PHSCALE_NBS scaling
     */
    size_t m_indexCLM;
 
    //! Molecular weight of the Solvent
    doublereal m_weightSolvent;
 
    /*!
     * In any molality implementation, it makes sense to have a minimum solvent
     * mole fraction requirement, since the implementation becomes singular in
     * the xmolSolvent=0 limit. The default is to set it to 0.01. We then modify
     * the molality definition to ensure that molal_solvent = 0 when
     * xmol_solvent = 0.
     */
    doublereal m_xmolSolventMIN;
 
    //! This is the multiplication factor that goes inside log expressions
    //! involving the molalities of species. It's equal to Wt_0 / 1000, where
    //! Wt_0 = weight of solvent (kg/kmol)
    doublereal m_Mnaught;
 
    //! Current value of the molalities of the species in the phase. Note this
    //! vector is a mutable quantity. units are (kg/kmol)
    mutable vector_fp m_molalities;
};
 
 
//! Scale to be used for the output of single-ion activity coefficients is that
//! used by Pitzer.
/*!
 * This is the internal scale used within the code. One property is that the
 * activity coefficients for the cation and anion of a single salt will be
 * equal. This scale is the one presumed by the formulation of the single-ion
 * activity coefficients described in this report.
 *
 * Activity coefficients for species k may be altered between scales s1 to s2
 * using the following formula
 *
 * \f[
 *     ln(\gamma_k^{s2}) = ln(\gamma_k^{s1})
 *        + \frac{z_k}{z_j} \left(  ln(\gamma_j^{s2}) - ln(\gamma_j^{s1}) \right)
 * \f]
 *
 * where j is any one species.
 */
const int PHSCALE_PITZER = 0;
 
//! Scale to be used for evaluation of single-ion activity coefficients is that
//! used by the NBS standard for evaluation of the pH variable.
/*!
 * This is not the internal scale used within the code.
 *
 * Activity coefficients for species k may be altered between scales s1 to s2
 * using the following formula
 *
 * \f[
 *     ln(\gamma_k^{s2}) = ln(\gamma_k^{s1})
 *        + \frac{z_k}{z_j} \left(  ln(\gamma_j^{s2}) - ln(\gamma_j^{s1}) \right)
 * \f]
 *
 * where j is any one species. For the NBS scale, j is equal to the Cl- species
 * and
 *
 * \f[
 *     ln(\gamma_{Cl-}^{s2}) = \frac{-A_{\phi} \sqrt{I}}{1.0 + 1.5 \sqrt{I}}
 * \f]
 *
 * This is the NBS pH scale, which is used in all conventional pH measurements.
 * and is based on the Bates-Guggenheim equations.
 */
const int PHSCALE_NBS = 1;
 
}
 
#endif