[Doc] Fix spelling errors

doc/sphinx/cti/input-files.rst

@@ -681,10 +681,10 @@ in the report for Chemkin referenced above. These errors include:
     | 1                | An integer with value 0, 1, or 2 indicating          |
     |                  | monatomic, linear, or non-linear molecular geometry. |
     +------------------+------------------------------------------------------+
-    | 2                | The Lennerd-Jones potential well depth               |
+    | 2                | The Lennard-Jones potential well depth               |
     |                  | :math:`\varepsilon/k_B` in Kelvin                    |
     +------------------+------------------------------------------------------+
-    | 3                | The Lennerd-Jones collision diameter :math:`\sigma`  |
+    | 3                | The Lennard-Jones collision diameter :math:`\sigma`  |
     |                  | in Angstrom                                          |
     +------------------+------------------------------------------------------+
     | 4                | The dipole moment :math:`\mu` in Debye               |

include/cantera/equil/vcs_VolPhase.h

@@ -34,7 +34,7 @@ class ThermoPhase;
 #define VCS_EOS_STOICH_SUB 5
 #define VCS_EOS_IDEAL_SOLN 22
 #define VCS_EOS_DEBEYE_HUCKEL 23
-#define VCS_EOS_REDLICK_KWONG 24
+#define VCS_EOS_REDLICH_KWONG 24
 #define VCS_EOS_REGULAR_SOLN 25
 #define VCS_EOS_UNK_CANTERA -1
 

include/cantera/equil/vcs_solve.h

@@ -912,7 +912,7 @@ public:
 
     //! Redimensionalize the problem data
     /*!
-     * Reddimensionalize the free energies using the multiplier R * T
+     * Redimensionalize the free energies using the multiplier R * T
      *
      * Essentially the internal data can either be in dimensional form or in
      * nondimensional form. This routine switches the data from nondimensional
@@ -1069,7 +1069,7 @@ public:
 private:
     //! Zero out the concentration of a species.
     /*!
-     * Make sure to conserveelements and keep track of the total moles in all
+     * Make sure to conserve elements and keep track of the total moles in all
      * phases.
      * - w[]
      * - m_tPhaseMoles_old[]
@@ -1429,7 +1429,7 @@ public:
      *
      * m_stoichCoeffRxnMatrix(j,irxn) : j refers to the component number, and
      *     irxn refers to the irxn_th non-component species. The stoichiometric
-     *     coefficients multilplied by the Formula coefficients of the component
+     *     coefficients multiplied by the Formula coefficients of the component
      *     species add up to the negative value of the number of elements in the
      *     species kspec.
      *
@@ -1469,7 +1469,7 @@ public:
     vector_fp m_feSpecies_old;
 
     //! Dimensionless new free energy for all the species in the mechanism
-    //! at the new tentatite T, P, and mole numbers.
+    //! at the new tentative T, P, and mole numbers.
     /*!
      *   The first NC entries are for components. The following
      *   NR entries are for the current non-component species in the mechanism.
@@ -1746,7 +1746,7 @@ public:
      */
     char m_unitsState;
 
-    //! Multiplier for the mole numbers within the nondimensionless formulation
+    //! Multiplier for the mole numbers within the nondimensional formulation
     /*!
      * All numbers within the main routine are on an absolute basis. This
      * presents some problems wrt very large and very small mole numbers. We get
@@ -1787,7 +1787,7 @@ public:
     //! Molar-based Activity Coefficients for Species based on old mole numbers
     /*!
      * These activity coefficients are based on the m_molNumSpecies_old
-     * values Molar based activity coeffients. Length = number of species
+     * values Molar based activity coefficients. Length = number of species
      */
     vector_fp m_actCoeffSpecies_old;
 
@@ -1814,7 +1814,7 @@ public:
 
     std::vector<std::vector<size_t> > phasePopProblemLists_;
 
-    //! Vector of pointers to thermostructures which identify the model
+    //! Vector of pointers to thermo structures which identify the model
     //! and parameters for evaluating the thermodynamic functions for that
     //! particular species.
     /*!
@@ -1847,10 +1847,10 @@ public:
 
     //! Debug printing lvl
     /*!
-     *  Levels correspond to the following guidlines
+     *  Levels correspond to the following guidelines
      *     * 0  No printing at all
      *     * 1  Serious warnings or fatal errors get one line
-     *     * 2  one line per eacdh successful vcs package call
+     *     * 2  one line per each successful vcs package call
      *     * 3  one line per every successful solve_TP calculation
      *     * 4  one line for every successful operation -> solve_TP gets a summary report
      *     * 5  each iteration in solve_TP gets a report with one line per species

include/cantera/numerics/IDA_Solver.h

@@ -77,7 +77,7 @@ public:
      */
     virtual void setMaxNumSteps(int n);
 
-    //! Sset the initial step size
+    //! Set the initial step size
     /*!
      * @param h0  initial step size value
      */

include/cantera/numerics/RootFind.h

@@ -96,7 +96,7 @@ namespace Cantera
  * ResidEval * ec;
  * // Instantiate the root finder with the residual to be solved, ec.
  * RootFind rf(&ec);
- * // Set the relative and absolute tolerancess for f and x.
+ * // Set the relative and absolute tolerances for f and x.
  * rf.setTol(1.0E-5, 1.0E-10, 1.0E-5, 1.0E-11);
  * // Give a hint about the function's dependence on x. This is needed, for example, if the function has
  * // flat regions.

include/cantera/thermo/IdealSolidSolnPhase.h

@@ -438,7 +438,7 @@ public:
      * returns an array of partial molar volumes of the species
      * in the solution. Units: m^3 kmol-1.
      *
-     * For this solution, thepartial molar volumes are equal to the
+     * For this solution, the partial molar volumes are equal to the
      * constant species molar volumes.
      *
      * @param vbar  Output vector of partial molar volumes. Length: m_kk.

include/cantera/thermo/LatticeSolidPhase.h

@@ -381,7 +381,7 @@ public:
      * returns an array of partial molar volumes of the species in the solution.
      * Units: m^3 kmol-1.
      *
-     * For this solution, thepartial molar volumes are equal to the constant
+     * For this solution, the partial molar volumes are equal to the constant
      * species molar volumes.
      *
      * @param vbar  Output vector of partial molar volumes. Length: m_kk.

include/cantera/thermo/MixedSolventElectrolyte.h

@@ -16,7 +16,7 @@
 namespace Cantera
 {
 //! MixedSolventElectrolyte is a derived class of GibbsExcessVPSSTP that employs
-//! the DH and local Marguless approximations for the excess Gibbs free energy
+//! the DH and local Margules approximations for the excess Gibbs free energy
 /*!
  * MixedSolventElectrolyte derives from class GibbsExcessVPSSTP which is derived
  * from VPStandardStateTP.

include/cantera/thermo/WaterPropsIAPWS.h

@@ -23,7 +23,7 @@ namespace Cantera
  * location of where we are in (T,rho) space.
  *
  * WATER_UNSTABLELIQUID indicates that we are in the unstable region, inside the
- * spinodal curve where dpdrho < 0.0 amonst other properties. The difference
+ * spinodal curve where dpdrho < 0.0 amongst other properties. The difference
  * between WATER_UNSTABLELIQUID and WATER_UNSTABLEGAS is that
  *     for WATER_UNSTABLELIQUID  d2pdrho2 > 0   and dpdrho < 0.0
  *     for WATER_UNSTABLEGAS     d2pdrho2 < 0   and dpdrho < 0.0
@@ -38,7 +38,7 @@ namespace Cantera
 
 //! Class for calculating the equation of state of water.
 /*!
- * The reference is W. Wagner, A. Prub, "The IAPWS Formulation 1995 for the
+ * The reference is W. Wagner, A. Pruss, "The IAPWS Formulation 1995 for the
  * Thermodynamic Properties of Ordinary Water Substance for General and
  * Scientific Use," J. Phys. Chem. Ref. Dat, 31, 387, 2002.
  *

include/cantera/thermo/WaterPropsIAPWSphi.h

@@ -21,7 +21,7 @@ namespace Cantera
 
 //! Low level class for the real description of water.
 /*!
- * The reference is W. Wagner, A. Prub, "The IAPWS Formulation 1995 for the
+ * The reference is W. Wagner, A. Pruss, "The IAPWS Formulation 1995 for the
  * Thermodynamic Properties of Ordinary Water Substance for General and
  * Scientific Use," J. Phys. Chem. Ref. Dat, 31, 387, 2002.
  *
@@ -35,7 +35,7 @@ public:
 
     //! Calculate the Phi function, which is the base function
     /*!
-     * The phi function is basically the helmholtz free energy Eqn. (6.4) All
+     * The phi function is basically the Helmholtz free energy Eqn. (6.4) All
      * internal polynomials are recalculated.
      *
      * @param tau     Dimensionless temperature = T_c/T

include/cantera/thermo/WaterSSTP.h

@@ -23,7 +23,7 @@ class WaterProps;
 //! Class for single-component water. This is designed to cover just the liquid
 //! part of water.
 /*!
- * The reference is W. Wagner, A. Prub, "The IAPWS Formulation 1995 for the
+ * The reference is W. Wagner, A. Pruss, "The IAPWS Formulation 1995 for the
  * Thermodynamic Properties of Ordinary Water Substance for General and
  * Scientific Use," J. Phys. Chem. Ref. Dat, 31, 387, 2002.
  *
@@ -172,9 +172,9 @@ public:
     //@}
     //! @name Thermodynamic Values for the Species Reference State
     /*!
-     *  All functions in this group need to be overrided, because the m_spthermo
+     *  All functions in this group need to be overridden, because the
-     *  MultiSpeciesThermo function is not adequate for the real equation of
+     *  m_spthermo MultiSpeciesThermo function is not adequate for the real
-     *  state.
+     *  equation of state.
      */
     //@{
 

include/cantera/thermo/electrolytes.h

@@ -31,7 +31,7 @@ const int cEST_strongAcidAssociated = 3; // Species which always breaks
 // in the speciation vector.
 const int cEST_polarNeutral = 4; // Polar neutral species
 const int cEST_nonpolarNeutral = 5; // Nonpolar neutral species. These
-// usually have activity coefficnt
+// usually have activity coefficient
 // corrections applied to them to
 // account for salting-out effects
 

include/cantera/transport/LiquidTransportParams.h

@@ -31,18 +31,18 @@ public:
     //! Object that specifies the viscosity interaction for the mixture
     LiquidTranInteraction* viscosity;
 
-    //! Object that specifes the ionic Conductivity of the mixture
+    //! Object that specifies the ionic Conductivity of the mixture
     LiquidTranInteraction* ionConductivity;
 
     //! Vector of pointer to the LiquidTranInteraction object which handles the
     //! calculation of the mobility ratios for the phase
     /*!
      * The mobility ratio is defined via the following quantity where i and j
-     * are species indecises.
+     * are species indices.
      *
      *   mobRat(i,j) = mu_i / mu_j
      *
-     * It is returned in fortran-ordering format. ie. it is returned as
+     * It is returned in fortran-ordering format. i.e. it is returned as
      * mobRat[k], where
      *
      *        k = j * nsp + i

include/cantera/transport/TransportBase.h

@@ -276,7 +276,7 @@ public:
      *
      *         mobRat(i,j) = mu_i / mu_j
      *
-     * It is returned in fortran-ordering format. ie. it is returned as
+     * It is returned in fortran-ordering format. i.e. it is returned as
      * mobRat[k], where
      *
      *        k = j * nsp + i

src/equil/vcs_VolPhase.cpp

@@ -839,7 +839,7 @@ std::string string16_EOSType(int EOSType)
     case VCS_EOS_DEBEYE_HUCKEL:
         sprintf(st,"Debeye Huckel   ");
         break;
-    case VCS_EOS_REDLICK_KWONG:
+    case VCS_EOS_REDLICH_KWONG:
         sprintf(st,"Redlick_Kwong   ");
         break;
     case VCS_EOS_REGULAR_SOLN:
@@ -1142,8 +1142,8 @@ std::string vcs_VolPhase::eos_name() const
         return "Ideal Soln";
     case VCS_EOS_DEBEYE_HUCKEL:
         return "Debeye Huckel";
-    case VCS_EOS_REDLICK_KWONG:
+    case VCS_EOS_REDLICH_KWONG:
-        return "Redlick_Kwong";
+        return "Redlich_Kwong";
     case VCS_EOS_REGULAR_SOLN:
         return "Regular Soln";
     default:

src/equil/vcs_rxnadj.cpp

@@ -323,8 +323,8 @@ int VCS_SOLVE::vcs_rxn_adj_cg()
         if (m_molNumSpecies_old[kspec] == 0.0 && (!m_SSPhase[kspec])) {
             // MULTISPECIES PHASE WITH total moles equal to zero
             //
-            // HKM -> the statment below presupposes units in m_deltaGRxn_new[].
+            // HKM -> the statement below presupposes units in m_deltaGRxn_new[].
-            // It probably should be replaced with something more relativistic
+            // It probably should be replaced with something more relative
             if (m_deltaGRxn_new[irxn] < -1.0e-4) {
                 sprintf(ANOTE, "MultSpec: come alive DG = %11.3E", m_deltaGRxn_new[irxn]);
                 m_deltaMolNumSpecies[kspec] = 1.0e-10;

src/kinetics/GasKinetics.cpp

@@ -287,7 +287,7 @@ void GasKinetics::addFalloffReaction(FalloffReaction& r)
         if (k != npos) {
             efficiencies[k] = eff.second;
         } else if (!m_skipUndeclaredThirdBodies) {
-            throw CanteraError("GasKinetics::addTFalloffReaction", "Found "
+            throw CanteraError("GasKinetics::addFalloffReaction", "Found "
                 "third-body efficiency for undefined species '" + eff.first +
                 "' while adding reaction '" + r.equation() + "'");
         }

src/kinetics/solveSP.cpp

@@ -124,7 +124,7 @@ int solveSP::solveSurfProb(int ifunc, doublereal time_scale, doublereal TKelvin,
     int label_d = -1; // Species IDs for damping control
     int label_t_old=-1;
     doublereal label_factor = 1.0;
-    int iter=0; // iteration number on numlinear solver
+    int iter=0; // iteration number on nonlinear solver
     int iter_max=1000; // maximum number of nonlinear iterations
     doublereal deltaT = 1.0E-10; // Delta time step
     doublereal damp=1.0;

src/zeroD/IdealGasConstPressureReactor.cpp

@@ -100,7 +100,7 @@ void IdealGasConstPressureReactor::evalEqs(doublereal time, doublereal* y,
     mcpdTdt -= m_Q;
 
     for (size_t n = 0; n < m_nsp; n++) {
-        // heat release from gas phase and surface reations
+        // heat release from gas phase and surface reactions
         mcpdTdt -= m_wdot[n] * m_hk[n] * m_vol;
         mcpdTdt -= m_sdot[n] * m_hk[n];
         // production in gas phase and from surfaces

src/zeroD/IdealGasReactor.cpp

@@ -102,7 +102,7 @@ void IdealGasReactor::evalEqs(doublereal time, doublereal* y,
     mcvdTdt += - m_pressure * m_vdot - m_Q;
 
     for (size_t n = 0; n < m_nsp; n++) {
-        // heat release from gas phase and surface reations
+        // heat release from gas phase and surface reactions
         mcvdTdt -= m_wdot[n] * m_uk[n] * m_vol;
         mcvdTdt -= m_sdot[n] * m_uk[n];
         // production in gas phase and from surfaces
@@ -128,7 +128,7 @@ void IdealGasReactor::evalEqs(doublereal time, doublereal* y,
             // flow of species into system and dilution by other species
             dYdt[n] += (mdot_spec - mdot_in * Y[n]) / m_mass;
 
-            // In combintion with h_in*mdot_in, flow work plus thermal
+            // In combination with h_in*mdot_in, flow work plus thermal
             // energy carried with the species
             mcvdTdt -= m_uk[n] / mw[n] * mdot_spec;
         }

src/zeroD/Reactor.cpp

@@ -210,7 +210,7 @@ void Reactor::evalEqs(doublereal time, doublereal* y,
     applySensitivity(params);
     evalWalls(time);
     double mdot_surf = evalSurfaces(time, ydot + m_nsp + 3);
-    dmdt += mdot_surf; // mass added to gas phase from surface reations
+    dmdt += mdot_surf; // mass added to gas phase from surface reactions
 
     // volume equation
     ydot[1] = m_vdot;