Fix spelling errors

include/cantera/numerics/NonlinearSolver.h

@@ -10,7 +10,7 @@
  *  $Revision$
  */
 /*
- * Copywrite 2004 Sandia Corporation. Under the terms of Contract
+ * Copyright 2004 Sandia Corporation. Under the terms of Contract
  * DE-AC04-94AL85000 with Sandia Corporation, the U.S. Government
  * retains certain rights in this software.
  * See file License.txt for licensing information.
@@ -199,7 +199,7 @@ public:
      *  @param typeCalc     Type of the calculation
      *  @param y_curr       Current value of the solution vector
      *  @param ydot_curr    Current value of the time derivative of the solution vector
-     *  @param evalType     Base evalulation type. Defaults to Base_ResidEval
+     *  @param evalType     Base evaluation type. Defaults to Base_ResidEval
      *
      * @return Returns a flag to indicate that operation is successful.
      *            1  Means a successful operation.
@@ -1095,7 +1095,7 @@ private:
     //! absolute tolerance in the unscaled solution unknowns
     doublereal userResidRtol_;
 
-    //! Check the residual tolerances explictly against user input
+    //! Check the residual tolerances explicitly against user input
     /*!
      *   0 Don't calculate residual weights from residual tolerance inputs
      *   1 Calculate residual weights from residual tolerance inputs only

include/cantera/thermo/PureFluidPhase.h

@@ -438,7 +438,7 @@ public:
      */
     virtual doublereal satTemperature(doublereal p) const;
 
-    //! Return the saturation pressure given the temperatur
+    //! Return the saturation pressure given the temperature
     /*!
      * @param t Temperature (Kelvin)
      */

interfaces/cython/cantera/examples/dusty_gas.py

@@ -1,7 +1,7 @@
 """
 Dusty Gas transport model.
 
-The Dusty Gas model is a mulicomponent transport model for gas transport
+The Dusty Gas model is a multicomponent transport model for gas transport
 through the pores of a stationary porous medium. This example shows how to
 create a transport manager that implements the Dusty Gas model and use it to
 compute the multicomponent diffusion coefficients.

interfaces/cython/cantera/examples/surface_chemistry/sofc.py

@@ -11,7 +11,7 @@ not need to be separately specified), as well as polarization curves.
 NOTE: The parameters here, and in the input file sofc.cti, are not to be
 relied upon for a real SOFC simulation! They are meant to illustrate only how
 to do such a calculation in Cantera. While some of the parameters may be close
-to real values, others are simply set arbitratily to give reasonable-looking
+to real values, others are simply set arbitrarily to give reasonable-looking
 results.
 
 It is recommended that you read input file sofc.cti before reading or running

interfaces/python/ctml_writer.py

@@ -1416,7 +1416,7 @@ class pdep_arrhenius(reaction):
     :param equation:
         A string specifying the chemical equation.
     :param args:
-        Each additiona argument is a sequence of four elements specifying the
+        Each additional argument is a sequence of four elements specifying the
         pressure and the Arrhenius parameters at that pressure.
     """
     def __init__(self, equation='', *args, **kwargs):

samples/python/fuel_cells/sofc.py

@@ -13,7 +13,7 @@
 # to be relied upon for a real SOFC simulation! They are meant to
 # illustrate only how to do such a calculation in Cantera. While some
 # of the parameters may be close to real values, others are simply set
-# arbitratily to give reasonable-looking results.
+# arbitrarily to give reasonable-looking results.
 
 # It is recommended that you read input file sofc.cti before reading
 # or running this script!

samples/python/transport/dustygas.py

@@ -1,7 +1,7 @@
 """
  Dusty Gas transport model.
 
- The Dusty Gas model is a mulicomponent transport model for gas
+ The Dusty Gas model is a multicomponent transport model for gas
  transport through the pores of a stationary porous medium. This
  example shows how to create a transport manager that implements the
  Dusty Gas model and use it to compute the multicomponent diffusion

src/oneD/Sim1D.cpp

@@ -28,7 +28,7 @@ Sim1D::Sim1D() :
 Sim1D::Sim1D(vector<Domain1D*>& domains) :
     OneDim(domains)
 {
-    // resize the internal solution vector and the wprk array, and perform
+    // resize the internal solution vector and the work array, and perform
     // domain-specific initialization of the solution vector.
 
     m_x.resize(size(), 0.0);

src/thermo/StatMech.cpp

@@ -502,18 +502,18 @@ int StatMech::buildmap()
     name_map["e"]->nvib=0;
 
     for (ii=0; ii < SS.size(); ii++) {
-        // check nvib was initalized for all species
+        // check nvib was initialized for all species
         if (name_map[SS[ii]]->nvib == -1) {
             std::cout << name_map[SS[ii]]->nvib << std::endl;
             throw CanteraError("Error in StatMech.cpp",
                                "nvib not initialized!. \n\n");
 
         } else {
-            // check that theta is initalized
+            // check that theta is initialized
             for (int i=0; i<name_map[SS[ii]]->nvib; i++) {
                 if (name_map[SS[ii]]->theta[i] <= 0.0) {
                     throw CanteraError("Error in StatMech.cpp",
-                                       "theta not initalized!. \n\n");
+                                       "theta not initialized!. \n\n");
                 }
             }