*** empty log message ***

Cantera/matlab/cantera/@Solution/set.m

@@ -40,6 +40,8 @@ hval = -999;
 uval = -999;
 sval = -999;
 vval = -999;
+qval = -999;
+
 np = 0;
 nt = 0;
 nv = 0;
@@ -48,6 +50,7 @@ ny = 0;
 ns = 0;
 nh = 0;
 nu = 0;
+nq = 0;
 
 while length(property_argin) >= 2,
   prop = property_argin{1};
@@ -105,6 +108,9 @@ while length(property_argin) >= 2,
    case 'S'
     sval = val; 
     ns = ns + 1;       
+   case 'Sat'
+    qval = val;
+    nq = nq + 1;
    otherwise
     error(['unknown property ' char(prop)])
   end
@@ -114,7 +120,7 @@ if nx + ny > 1
   error('composition specified multiple times');
 end
 
-ntot = nt + np + nv + ns + nh + nu;
+ntot = nt + np + nv + ns + nh + nu + nq;
 
 if ntot == 1
   %
@@ -138,7 +144,13 @@ elseif ntot == 2
     if nv == 1
       setDensity(a,1.0/vval);   % temperature held fixed
     elseif np == 1
-      setPressure(a, pval);     % temperature held fixed    
+      setPressure(a, pval);     % temperature held fixed 
+    elseif nq == 1
+      if qval == 'Liquid'
+	setState_satLiquid(a);
+      elseif qval == 'Vapor'
+	setState_satVapor(a);
+      end
     else
       error('unimplemented property pair');  
     end

Cantera/matlab/cantera/@ThermoPhase/critDensity.m

@@ -0,0 +1,4 @@
+function v = critDensity(a)
+% CRITDENSITY - Critical density [kg/m3].
+%
+  v = thermo_get(a.tp_id,21);

Cantera/matlab/cantera/@ThermoPhase/critPressure.m

@@ -0,0 +1,4 @@
+function v = critPressure(a)
+% CRITPRESSURE - Critical pressure [Pa].
+%
+  v = thermo_get(a.tp_id,20);

Cantera/matlab/cantera/@ThermoPhase/critTemperature.m

@@ -0,0 +1,4 @@
+function v = critTemperature(a)
+% CRITTEMPERATURE - Critical temperature [K].
+%
+  v = thermo_get(a.tp_id,19);

Cantera/matlab/cantera/@ThermoPhase/minTemp.m

@@ -1,12 +1,6 @@
-function v = minTemp(p)
+function v = critTemperature(a)
-% MINTEMP - Minimum temperature.
+% CRITTEMPERATURE - Critical temperature [K].
-% 
-%   The parameterizations used to represent the temperature-dependent
-%   species thermodynamic properties are generally only valid in some
-%   finite temperature range, which may be different for each species
-%   in the phase. This method returns the lowest temperature at which
-%   the parameterizations are valid for all species in the phase.
 %
-%   See also: maxTemp
+%    The critical temperature is the temperature at the critical point
 %
-  v = thermo_get(p.tp_id,16);
+  v = thermo_get(p.tp_id,19);

Cantera/matlab/cantera/@ThermoPhase/satPressure.m

@@ -0,0 +1,3 @@
+function v = satPressure(a, T)
+% SATPRESSURE - Saturation pressure for temperature T.
+  v = thermo_get(a.tp_id,24,T);

Cantera/matlab/cantera/@ThermoPhase/satTemperature.m

@@ -0,0 +1,3 @@
+function v = satTemperature(a, p)
+% SATTEMPERATURE - Saturation temperature for pressure p.
+  v = thermo_get(a.tp_id,23,p);

Cantera/matlab/cantera/@ThermoPhase/setState_satLiquid.m

@@ -0,0 +1,5 @@
+function a = setState_satLiquid(a)
+% SETSTATE_SATLIQUID    Set the fluid to the saturated liquid state
+% at the current temperature. 
+%  
+thermo_set(a.tp_id,2,0);

Cantera/matlab/cantera/@ThermoPhase/setState_satVapor.m

@@ -0,0 +1,5 @@
+function a = setState_satVapor(a)
+% SETSTATE_SATVAPOR    Set the fluid to the saturated vapor state at the
+% current temperature. 
+%  
+thermo_set(a.tp_id,3,0);

Cantera/matlab/cantera/@ThermoPhase/vaporFraction.m

@@ -0,0 +1,5 @@
+function v = vaporFraction(a)
+% VAPORFRACTION - Vapor fraction.
+%   If object 'a' represents a liquid/vapor mixture, this method
+%   returns the vapor fraction. 
+  v = thermo_get(a.tp_id,22);

Cantera/matlab/cantera/@Transport/Transport.m

@@ -15,7 +15,7 @@ if nargin == 4
       node = child(xml_phase,'transport');
       tr.model = attrib(node,'model');
     catch
-      tr.model = '';
+      tr.model = 'None';
     end
   else
     tr.model = model;

Cantera/matlab/cantera/Hydrogen.m

@@ -0,0 +1,11 @@
+function n = Hydrogen()
+% HYDROGEN - Return an object representing hydrogen.
+%
+%   The object returned by this method implements an accurate equation of
+%   state for hydrogen that can be used in the liquid, vapor, saturated
+%   liquid/vapor, and supercritical regions of the phase diagram.  The
+%   equation of state is taken from W. C. Reynolds, "Thermodynamic
+%   Properties in SI."
+%
+n = importPhase('purefluids.cti','hydrogen');
+

Cantera/matlab/cantera/Methane.m

@@ -0,0 +1,11 @@
+function n = Methane()
+% METHANE - Return an object representing methane.
+%
+%   The object returned by this method implements an accurate equation of
+%   state for methane that can be used in the liquid, vapor, saturated
+%   liquid/vapor, and supercritical regions of the phase diagram.  The
+%   equation of state is taken from W. C. Reynolds, "Thermodynamic
+%   Properties in SI."
+%
+n = importPhase('purefluids.cti','methane');
+

Cantera/matlab/cantera/Nitrogen.m

@@ -0,0 +1,11 @@
+function n = Nitrogen()
+% NITROGEN - Return an object representing nitrogen.
+%
+%   The object returned by this method implements an accurate equation of
+%   state for nitrogen that can be used in the liquid, vapor, saturated
+%   liquid/vapor, and supercritical regions of the phase diagram.  The
+%   equation of state is taken from W. C. Reynolds, "Thermodynamic
+%   Properties in SI."
+%
+n = importPhase('purefluids.cti','nitrogen');
+

Cantera/matlab/cantera/Oxygen.m

@@ -0,0 +1,11 @@
+function n = Oxygen()
+% OXYGEN - Return an object representing oxygen.
+%
+%   The object returned by this method implements an accurate equation of
+%   state for oxygen that can be used in the liquid, vapor, saturated
+%   liquid/vapor, and supercritical regions of the phase diagram.  The
+%   equation of state is taken from W. C. Reynolds, "Thermodynamic
+%   Properties in SI."
+%
+n = importPhase('purefluids.cti','oxygen');
+

Cantera/matlab/cantera/Water.m

@@ -0,0 +1,11 @@
+function w = Water()
+% WATER - Return an object representing water.
+%
+%   The object returned by this method implements an accurate equation of
+%   state for water that can be used in the liquid, vapor, saturated
+%   liquid/vapor, and supercritical regions of the phase diagram.  The
+%   equation of state is taken from W. C. Reynolds, "Thermodynamic
+%   Properties in SI."
+%
+w = importPhase('purefluids.cti','water');
+

Cantera/matlab/cantera/examples/rankine.m

@@ -0,0 +1,42 @@
+%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% 
+%
+%  An ideal Rankine cycle.
+%
+%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
+
+
+% create an object representing water
+w = Water;
+
+% start with saturated liquid water at 300 K
+set(w,'T',300.0,'Sat','Liquid');
+h1 = enthalpy_mass(w);
+s1 = entropy_mass(w);
+p1 = pressure(w);
+
+% pump it isentropically to 10 MPa
+set(w,'S',s1,'P',1.0e7);
+h2 = enthalpy_mass(w);
+p2 = pressure(w);
+
+pump_work = h2 - h1;
+
+
+% heat to 1500 K at constant pressure
+set(w,'T',1500.0,'P',p2);
+h3 = enthalpy_mass(w);
+s3 = entropy_mass(w);
+
+heat_added = h3 - h2;
+
+
+% expand isentropically to the initial pressure
+set(w,'S',s3,'P',p1);
+h4 = enthalpy_mass(w);
+x4 = vaporFraction(w);
+
+work_output = h3 - h4;
+
+% compute the efficiency
+efficiency = (work_output - pump_work)/heat_added
+

Cantera/matlab/cantera/private/thermomethods.cpp

@@ -27,7 +27,11 @@ static void thermoset( int nlhs, mxArray *plhs[],
         case 10:
             ierr = delThermo(th); break;
         case 1:
-            ierr = th_setPressure(th,*ptr); break; 
+            ierr = th_setPressure(th,*ptr); break;
+        case 2:
+            ierr = th_setState_satLiquid(th); break;
+        case 3:
+            ierr = th_setState_satVapor(th); break;
         default:
             mexErrMsgTxt("unknown attribute.");
         }
@@ -69,7 +73,7 @@ static void thermoset( int nlhs, mxArray *plhs[],
 static void thermoget( int nlhs, mxArray *plhs[],
         int nrhs, const mxArray *prhs[] )
     {
-        double vv;
+        double vv, psat, tsat;
         int n = getInt(prhs[1]);
         int job = getInt(prhs[2]);
 
@@ -123,11 +127,11 @@ static void thermoget( int nlhs, mxArray *plhs[],
             case 22:
                 vv = th_vaporFraction(n); break;
             case 23:
-                double p = getDouble(prhs[3]); 
+                psat = getDouble(prhs[3]); 
-                vv = th_satTemperature(n, p); break;
+                vv = th_satTemperature(n, psat); break;
             case 24:
-                double t = getDouble(prhs[3]);
+                tsat = getDouble(prhs[3]);
-                vv = th_satPressure(n, t); break;
+                vv = th_satPressure(n, tsat); break;
 #endif
             default:
                 ok = false;

Cantera/matlab/setup_winmatlab.py

@@ -1,7 +1,7 @@
 
 import sys
 
-bindir = '/home/goodwin/ct153d/bin'
+bindir = '/home/goodwin/ctt/bin'
 libdir = '/home/goodwin/dv/sf/cantera/build/lib/i686-pc-linux-gnu'
 incdir = '/home/goodwin/dv/sf/cantera/build/include'
 dflibdir = ''