[Matlab] Fix various typos

interfaces/matlab_experimental/Base/Interface.m

@@ -6,7 +6,7 @@
     % See `ideal-surface <https://cantera.org/documentation/docs-2.6/sphinx/html/yaml/phases.html#sec-yaml-ideal-surface>`__
     % and `Declaring adjacent phases <https://cantera.org/tutorials/yaml/phases.html#declaring-adjacent-phases>`__.
     %
-    % :param varagin:
+    % :param varargin:
     %     Variable number of inputs consisting of the following:
     %       - src: YAML file containing the interface or edge phase.
     %       - id: Name of the interface or edge phase in the YAML file.
@@ -91,7 +91,7 @@ function delete(s)
 
         function d = get.siteDensity(s)
             surfID = s.tpID;
-            d = calllibt(ct, 'surf_siteDensity', surfID);
+            d = ctFunc('surf_siteDensity', surfID);
         end
 
         function c = get.concentrations(s)

interfaces/matlab_experimental/Base/Kinetics.m

@@ -11,7 +11,7 @@
     % reaction rates of progress, species production rates, and other
     % quantities pertaining to a reaction mechanism.
     %
-    % :param varagin:
+    % :param varargin:
     %     Variable number of inputs consisting of the following:
     %       - ph:
     %           An instance of class :mat:class:`ThermoPhase` representing the
@@ -235,7 +235,7 @@ function delete(kin)
             %    coefficients should be retrieved. Optional argument; if
             %    specified, ``rxns`` must be specified as well.
             % :param rxns:
-            %    Reaction indicies for which reactant stoichiometric
+            %    Reaction indices for which reactant stoichiometric
             %    coefficients should be retrieved. Optional argument; if
             %    specified, ``species`` must be specified as well.
             % :return:
@@ -246,7 +246,7 @@ function delete(kin)
             %    matrix will contain only entries for the specified species
             %    and reactions. For example, ``stoich_p(a, 3, [1, 3, 5,
             %    7])`` returns a sparse matrix containing only the
-            %    coefficients for specis 3 in reactions 1, 3, 5, and 7.
+            %    coefficients for species 3 in reactions 1, 3, 5, and 7.
 
             nsp = kin.nTotalSpecies;
             nr = kin.nReactions;
@@ -288,7 +288,7 @@ function delete(kin)
             %    coefficients should be retrieved. Optional argument; if
             %    specified, ``rxns`` must be specified as well.
             % :param rxns:
-            %    Reaction indicies for which product stoichiometric
+            %    Reaction indices for which product stoichiometric
             %    coefficients should be retrieved. Optional argument; if
             %    specified, ``species`` must be specified as well.
             % :return:
@@ -335,7 +335,7 @@ function delete(kin)
             %    should be retrieved. Optional argument; if specified,
             %    "rxns" must be specified as well.
             % :param rxns:
-            %    Reaction indicies for which net stoichiometric
+            %    Reaction indices for which net stoichiometric
             %    coefficients should be retrieved. Optional argument; if
             %    specified, "species" must be specified as well.
             % :return:
@@ -534,7 +534,7 @@ function delete(kin)
         end
 
         function advanceCoverages(kin, dt)
-            % Advance the surface coveages forward in time. ::
+            % Advance the surface coverages forward in time. ::
             %
             %     >> kin.advanceCoverages(dt)
             %

interfaces/matlab_experimental/Base/Mixture.m

@@ -105,7 +105,7 @@
         % :param m:
         %     Instance of class :mat:class:`Mixture`.
         % :param name:
-        %     Name of the speces whose index is desired.
+        %     Name of the species whose index is desired.
         % :return:
         %     Index of species with name ``name``.
         %

interfaces/matlab_experimental/Base/ThermoPhase.m

@@ -667,11 +667,6 @@ function display(tp)
                 m = element;
             end
 
-            % if k < 0 | m < 0
-            %     n = -1;
-            %     return
-            % end
-
             n = ctFunc('thermo_nAtoms', tp.tpID, k - 1, m - 1);
 
         end
@@ -1341,7 +1336,7 @@ function display(tp)
             elseif isa(yy, 'char')
                 ctFunc('thermo_setMassFractionsByName', tp.tpID, yy);
             else
-                error('Invalud input.')
+                error('Invalid input.')
             end
 
         end

interfaces/matlab_experimental/OneDim/Domain1D.m

@@ -121,7 +121,7 @@ function delete(d)
         function b = bounds(d, component)
             % Get the (lower, upper) bounds for a solution component. ::
             %
-            %     >> b = d.bounds(componoent)
+            %     >> b = d.bounds(component)
             %
             % :param component:
             %    String name of the component for which the bounds are returned.

interfaces/matlab_experimental/OneDim/Sim1D.m

@@ -121,7 +121,7 @@ function save(s, fname, id, desc)
             % :param component:
             %    String component for which the solution is desired. If omitted,
             %    solution for all of the components will be returned in
-            %    an :math:`nPoints \times nComponnts` array.
+            %    an :math:`nPoints \times nComponents` array.
             % :return:
             %    Either an :math:`nPoints \times 1` vector, or
             %    :math:`nPoints \times nComponents` array.
@@ -163,7 +163,7 @@ function solve(s, loglevel, refineGrid)
             %    Instance of class :mat:class:`Sim1D`.
             % :param loglevel:
             %    Integer flag controlling the amount of diagnostic output.
-            %    Zero supresses all output, and 5 produces very verbose output.
+            %    Zero suppresses all output, and 5 produces very verbose output.
             % :param refineGrid:
             %    Integer, 1 to allow grid refinement, 0 to disallow.
 
@@ -483,7 +483,7 @@ function setValue(s, n, comp, localPoints, v)
             % This sets component 5 at the leftmost point (local point 1)
             % in domain 3 to the value 5.6. Note that the local index
             % always begins at 1 at the left of each domain, independent of
-            % the global index of the point, wchih depends on the location
+            % the global index of the point, which depends on the location
             % of this domain in the class :mat:class:`Sim1D` object.
             %
             % :param s:

interfaces/matlab_experimental/OneDim/Surface.m

@@ -1,4 +1,4 @@
-classdef Surface < Bondary1D
+classdef Surface < Boundary1D
     % Create a surface domain. ::
     %
     %     >> m = Surface(phase, id)

interfaces/matlab_experimental/Reactor/FlowDevice.m

@@ -24,7 +24,7 @@
     properties (SetAccess = immutable)
 
         type % Type of flow device.
-        id % ID of Flowdevice object.
+        id % ID of FlowDevice object.
 
     end
 
@@ -110,13 +110,13 @@ function install(f, upstream, downstream)
 
         end
 
-        %% Flowdevice Get Methods
+        %% FlowDevice Get Methods
 
         function mdot = get.massFlowRate(f)
             mdot = ctFunc('flowdev_massFlowRate2', f.id);
         end
 
-        %% Flowdevice Set Methods
+        %% FlowDevice Set Methods
 
         function set.massFlowRate(f, mdot)
 

interfaces/matlab_experimental/Reactor/Reactor.m

@@ -48,7 +48,7 @@
         %
         % If the chemistry is disabled, then the reactor composition is
         % constant. The parameter should be the string "on" to enable
-        % the species equaionts, or "off" to disable it.
+        % the species equations, or "off" to disable it.
         %
         % By default, :mat:class:`Reactor` objects are created with the species
         % equations enabled if there are reactions present in the
@@ -92,9 +92,9 @@
             %     >> r = Reactor(content, typ)
             %
             % A :mat:class:`Reactor` object simulates a perfectly-stirred reactor.
-            % It has a time-dependent tstate, and may be coupled to other
+            % It has a time-dependent state, and may be coupled to other
             % reactors through flow lines or through walls that may expand
-            % or contract and/orconduct heat.
+            % or contract and/or conduct heat.
             %
             % :param contents:
             %    Instance of :mat:class:`Solution` representing the contents of

interfaces/matlab_experimental/Reactor/ReactorNet.m

@@ -39,9 +39,9 @@
         % The integrator chooses a step size based on the desired error
         % tolerance and the rate at which the solution is changing.
         % In some cases, the solution changes very slowly at first,
-        % then very rapidly (ifnition problems). In such cases, the
+        % then very rapidly (ignition problems). In such cases, the
         % integrator may choose a timestep that is too large, which
-        % leads to numerical problems later. Use thismethod to set an
+        % leads to numerical problems later. Use this method to set an
         % upper bound on the timestep.
         maxTimeStep
 
@@ -124,7 +124,7 @@ function advance(r, tout)
             % In some cases, the solution changes very slowly at first,
             % then very rapidly (ignition problems). In such cases, the
             % integrator may choose a timestep that is too large, which
-            % leads to numerical problems later. Use thismethod to set an
+            % leads to numerical problems later. Use this method to set an
             % upper bound on the timestep.
             %
             % :param maxstep:

interfaces/matlab_experimental/Reactor/ReactorSurface.m

@@ -5,7 +5,7 @@
     %
     % A surface on which heterogeneous reactions take place. The
     % mechanism object (typically an instance of :mat:class:`Interface`)
-    % mustb be constructed so that it is properly linked to the
+    % must be constructed so that it is properly linked to the
     % object representing the fluid in the reactor. The surface
     % temperature on each side is taken to be equal to the
     % temperature of the reactor.

interfaces/matlab_experimental/Reactor/Valve.m

@@ -18,8 +18,7 @@
     % does not model real valve characteristics - in particular, it
     % does not model choked flow. The mass flow rate is always assumed
     % to be linearly proportional to the pressure difference, no matter how
-    % large the pressure difference. THIS MAY CHANGE IN A F`UTURE
-    % RELEASE.
+    % large the pressure difference. THIS MAY CHANGE IN A FUTURE RELEASE.
     %
     % see also: :mat:class:`FlowDevice`, :mat:class:`MassFlowController`
     %

interfaces/matlab_experimental/Utility/ctUnload.m

@@ -1,5 +1,5 @@
 function ctUnload()
-    % Unload the Cantear C Library from the Memory
+    % Unload the Cantera C Library from the Memory
 
     if libisloaded(ctLib)
         ctCleanUp;

samples/matlab_experimental/catcomb.m

@@ -7,7 +7,7 @@
 % chemistry is included too, and has some effect very near the
 % surface.
 %
-% The catalytic combustion mechanism is from Deutschman et al., 26th
+% The catalytic combustion mechanism is from Deutschmann et al., 26th
 % Symp. (Intl.) on Combustion,1996 pp. 1747-1754
 %
 % Keywords: combustion, catalysis, 1D flow, surface chemistry

samples/matlab_experimental/ignite.m

@@ -42,7 +42,7 @@
     % boundary conditions - the rate of change of volume, the heat
     % flux, and the area.
 
-    % Rate of change of volume. Any arbirtrary function may be implemented.
+    % Rate of change of volume. Any arbitrary function may be implemented.
     % Input arguments:
     %   t      time
     %   vol    volume

samples/matlab_experimental/reactor1.m

@@ -1,5 +1,5 @@
 function reactor1(g)
-    %% REACTOR1 Zero-dimensional kinetics: adiabatc, constant pressure.
+    %% REACTOR1 Zero-dimensional kinetics: adiabatic, constant pressure.
     %
     % This example illustrates how to use class 'Reactor' for zero-dimensional
     % kinetics simulations. Here the parameters are set so that the reactor is

samples/matlab_experimental/surf_reactor.m

@@ -21,7 +21,7 @@
 gas.TPX = {t, OneAtm, 'CH4:0.01, O2:0.21, N2:0.78'};
 
 % The surface reaction mechanism describes catalytic combustion of
-% methane on platinum, and is from Deutschman et al., 26th
+% methane on platinum, and is from Deutschmann et al., 26th
 % Symp. (Intl.) on Combustion,1996, pp. 1747-1754
 surf = Interface('ptcombust.yaml', 'Pt_surf', gas);
 surf.TP = {t, surf.P};