Changeset 916

Timestamp:

Feb 24, 2010, 8:15:15 PM (12 years ago)

Author:

Rafael de Pelegrini Soares

Message:

Fixed ammonia sample

File:

• branches/gui/sample/optimization/ammonia.mso (modified) (3 diffs)

branches/gui/sample/optimization/ammonia.mso

@@ -123 +123 @@
         F101   as flash_steady;
         F102   as flash_steady;
-        S101   as splitter;
+        S101   as splitter2;
         M101   as Mixer;
         M102   as Mixer;
@@ -141 +141 @@
         M102.Outlet    to   R101.Inlet;
         R101.Outlet    to   F101.Inlet;
-        F101.OutletL   to   F102.Inlet;
-        F102.OutletV   to   M101.Inlet2;
-        F101.OutletV   to   S101.Inlet;
+        F101.OutletLiquid   to   F102.Inlet;
+        F102.OutletVapour   to   M101.Inlet2;
+        F101.OutletVapour   to   S101.Inlet;
         S101.Outlet1   to   C102.Inlet;
         C102.Outlet    to   M102.Inlet2;
@@ -165 +165 @@
         R101.X = 0.4; # Convertion of the reactor
         
-        F101.OutletV.P = 199 * 'atm';
-        F101.OutletV.T = (-34 + 273.15) * 'K';
+        F101.OutletVapour.P = 199 * 'atm';
+        F101.OutletVapour.T = (-34 + 273.15) * 'K';
         
-        F102.OutletV.P = 10 * 'atm';
+        F102.OutletVapour.P = 10 * 'atm';
         F102.InletQ = 0 * 'kJ/h';
         
         # We can choose between one of the following specs
-        S101.frac = 0.78; # Recycle fraction
+        S101.FlowRatios(1) = 0.78; # Recycle fraction
         #loose = 1 * 'lbmol/h'; # Ammonia in the purge
         
         EQUATIONS
-        production = purity * F102.OutletL.F;
-        purity = F102.OutletL.z(5);
+        production = purity * F102.OutletLiquid.F;
+        purity = F102.OutletLiquid.z(5);
         loose  = S101.Outlet2.F * S101.Outlet2.z(5);