Changeset 313 for trunk/sample

Timestamp:

Jul 14, 2007, 1:45:55 PM (16 years ago)

Author:

Argimiro Resende Secchi

Message:

Change name of outlet energy stream to OutletQ.

Location:

trunk/sample

Files:

• controllers/Sample_flash_pid.mso (modified) (1 diff)
• miscellaneous/sample_tanks.mso (modified) (2 diffs)
• optimization/ammonia.mso (modified) (1 diff)
• optimization/ammonia_opt.mso (modified) (1 diff)
• optimization/flash_opt.mso (modified) (2 diffs)
• reactors/sample_batch.mso (modified) (1 diff)
• stage_separators/sample_column.mso (modified) (7 diffs)
• stage_separators/sample_columnReact.mso (modified) (2 diffs)
• stage_separators/sample_condenser.mso (modified) (4 diffs)
• stage_separators/sample_flash.mso (modified) (4 diffs)
• stage_separators/sample_reboiler.mso (modified) (4 diffs)
• stage_separators/sample_tank.mso (modified) (4 diffs)

trunk/sample/controllers/Sample_flash_pid.mso

@@ -86 +86 @@
         CONNECTIONS
         s1.Outlet to fl.Inlet;
-        Q.Outlet to fl.InletQ;
+        Q.OutletQ to fl.InletQ;
         
         SPECIFY
 
-        Q.Outlet.Q = 1026.32 * 'kJ/s';
+        Q.OutletQ.Q = 1026.32 * 'kJ/s';
 
         #Parâmetros do controlador de nível

trunk/sample/miscellaneous/sample_tanks.mso

@@ -40 +40 @@
         INITIAL
         "altura inicial"
-        Tanque.h = 1 * 'm';
+        Tanque.Level = 1 * 'm';
         
         OPTIONS
@@ -70 +70 @@
         INITIAL
         "altura inicial"
-        Tanque1.h = 1 * 'm';
-        Tanque2.h = 2 * 'm';
-        Tanque3.h = 1 * 'm';
+        Tanque1.Level = 1 * 'm';
+        Tanque2.Level = 2 * 'm';
+        Tanque3.Level = 1 * 'm';
         
         OPTIONS

trunk/sample/optimization/ammonia.mso

@@ -147 +147 @@
         C102.Outlet    to   M102.Inlet2;
         
-        Q1.Outlet      to   F101.InletQ;
-        Q2.Outlet      to   F102.InletQ;        
+        Q1.OutletQ      to   F101.InletQ;
+        Q2.OutletQ      to   F102.InletQ;       
         
         SET

trunk/sample/optimization/ammonia_opt.mso

@@ -26 +26 @@
         MINIMIZE
         
-        abs(Q1.Outlet.Q) + abs(Q2.Outlet.Q)
+        abs(Q1.OutletQ.Q) + abs(Q2.OutletQ.Q)
         #loose / 'lbmol/h'
         # C102.Pot/'kW'*180

trunk/sample/optimization/flash_opt.mso

@@ -48 +48 @@
         CONNECTIONS
         s1.Outlet to fl.Inlet;
-        Q.Outlet to fl.InletQ;
+        Q.OutletQ to fl.InletQ;
         
         EQUATIONS
@@ -62 +62 @@
         fl.OutletL.P = 2.5 * 'atm';
 
-        #Q.Outlet.Q = 0 * 'kJ/h';
+        #Q.OutletQ.Q = 0 * 'kJ/h';
         fl.OutletL.T = 315.06 * 'K';
         

trunk/sample/reactors/sample_batch.mso

@@ -29 +29 @@
         DEVICES
         feed as stream;
-        reac as batch_isotermic;
+        reac as batch_isothermic;
         
         CONNECTIONS

trunk/sample/stage_separators/sample_column.mso

@@ -217 +217 @@
         zero to col.trays([1:4]).Inlet;
         zero to col.trays([6:col.NTrays]).Inlet;
-        Qc.Outlet to col.cond.InletQ;
-        Qr.Outlet to col.reb.InletQ;
+        Qc.OutletQ to col.cond.InletQ;
+        Qr.OutletQ to col.reb.InletQ;
         
         SPECIFY
@@ -237 +237 @@
         col.sptop.frac = 0.444445;
         col.cond.OutletV.F = 0 * 'kmol/h';
-        Qr.Outlet.Q = 3.7743e6 * 'kJ/h';
-        Qc.Outlet.Q = -3.71e6 * 'kJ/h';
+        Qr.OutletQ.Q = 3.7743e6 * 'kJ/h';
+        Qc.OutletQ.Q = -3.71e6 * 'kJ/h';
         col.pump1.dP = 16 * 'kPa';
         col.trays.Emv = 1;
@@ -310 +310 @@
         zero to col.trays([1:4]).Inlet;
         zero to col.trays([6:col.NTrays]).Inlet;
-        Qttop.Outlet to col.ttop.InletQ;
-        Qtbottom.Outlet to col.tbottom.InletQ;
-        Qc.Outlet to col.cond.InletQ;
-        Qr.Outlet to col.reb.InletQ;
+        Qttop.OutletQ to col.ttop.InletQ;
+        Qtbottom.OutletQ to col.tbottom.InletQ;
+        Qc.OutletQ to col.cond.InletQ;
+        Qr.OutletQ to col.reb.InletQ;
         
         SPECIFY
@@ -332 +332 @@
         col.spbottom.Outlet1.F = 100 * 'kmol/h';
         
-        Qr.Outlet.Q = 3.7743e6 * 'kJ/h';
-        Qc.Outlet.Q = -3.71e6 * 'kJ/h';
-        Qttop.Outlet.Q = 0 * 'kJ/h';
-        Qtbottom.Outlet.Q = 0 * 'kJ/h';
+        Qr.OutletQ.Q = 3.7743e6 * 'kJ/h';
+        Qc.OutletQ.Q = -3.71e6 * 'kJ/h';
+        Qttop.OutletQ.Q = 0 * 'kJ/h';
+        Qtbottom.OutletQ.Q = 0 * 'kJ/h';
         
         col.pump1.dP = 16 * 'kPa';
@@ -432 +432 @@
         zero to col.trays([1:4]).Inlet;
         zero to col.trays([6:col.NTrays]).Inlet;
-        Qc.Outlet to col.cond.InletQ;
-        Qr.Outlet to col.reb.InletQ;
+        Qc.OutletQ to col.cond.InletQ;
+        Qr.OutletQ to col.reb.InletQ;
 
         EQUATIONS
@@ -452 +452 @@
         TCcond.Ports.input = Tad;
         Tad = (col.cond.OutletL.T-Tmin)/(Tmax-Tmin);
-        Qc.Outlet.Q = Qcmin+(Qcmax-Qcmin)*TCcond.Ports.output;  
+        Qc.OutletQ.Q = Qcmin+(Qcmax-Qcmin)*TCcond.Ports.output; 
 
         "Pressure Controller"
@@ -529 +529 @@
         zero.h = 0 * 'J/mol';
         
-        Qr.Outlet.Q = 3e6 * 'kJ/h';
+        Qr.OutletQ.Q = 3e6 * 'kJ/h';
         col.pump1.dP = 16 * 'kPa';
         col.trays.Emv = 1;

trunk/sample/stage_separators/sample_columnReact.mso

@@ -77 +77 @@
         zero to col.trays([1:4]).Inlet;
         zero to col.trays([6:col.NTrays]).Inlet;
-        Qc.Outlet to col.cond.InletQ;
-        Qr.Outlet to col.reb.InletQ;
+        Qc.OutletQ to col.cond.InletQ;
+        Qr.OutletQ to col.reb.InletQ;
         
         EQUATIONS
@@ -91 +91 @@
  
         if col.reb.startup then
-                Qc.Outlet.Q = 0 * PIDTcond.Ports.output * 'kJ/s';
-                Qr.Outlet.Q = 0 * PIDTreb.Ports.output * 'kJ/s';
+                Qc.OutletQ.Q = 0 * PIDTcond.Ports.output * 'kJ/s';
+                Qr.OutletQ.Q = 0 * PIDTreb.Ports.output * 'kJ/s';
                 
                 PIDTreb.Ports.input = PIDTreb.Ports.setPoint;
         else
-                Qc.Outlet.Q = Qcmin+(Qcmax-Qcmin)*PIDTcond.Ports.output;
-                Qr.Outlet.Q = Qrmin+(Qrmax-Qrmin)*PIDTreb.Ports.output;
+                Qc.OutletQ.Q = Qcmin+(Qcmax-Qcmin)*PIDTcond.Ports.output;
+                Qr.OutletQ.Q = Qrmin+(Qrmax-Qrmin)*PIDTreb.Ports.output;
                 
                 PIDTreb.Ports.input=Treb_ad;

trunk/sample/stage_separators/sample_condenser.mso

@@ -51 +51 @@
         s1.Outlet to c1.InletV;
         c1.OutletL to sp.Inlet;
-        Q.Outlet to c1.InletQ;
+        Q.OutletQ to c1.InletQ;
         
         SPECIFY
@@ -63 +63 @@
         c1.OutletL.F = 153 * 'kmol/h';
 
-        Q.Outlet.Q = -3.71e6 * 'kJ/h';
+        Q.OutletQ.Q = -3.71e6 * 'kJ/h';
 
         SET
@@ -101 +101 @@
         CONNECTIONS
         s1.Outlet to c1.InletV;
-        Q.Outlet to c1.InletQ;
+        Q.OutletQ to c1.InletQ;
         
         SPECIFY
@@ -109 +109 @@
         s1.Outlet.z = [0.664, 0.336];
 
-        Q.Outlet.Q = 3.71e6 * 'kJ/h';
+        Q.OutletQ.Q = 3.71e6 * 'kJ/h';
         c1.DP = 100 * 'kPa';
 

trunk/sample/stage_separators/sample_flash.mso

@@ -49 +49 @@
         CONNECTIONS
         s1.Outlet to fl.Inlet;
-        Q.Outlet to fl.InletQ;
+        Q.OutletQ to fl.InletQ;
         
         EQUATIONS
@@ -62 +62 @@
 
         fl.OutletV.F = 68.5 * 'kmol/h';
-        Q.Outlet.Q = 0 * 'kJ/h';
+        Q.OutletQ.Q = 0 * 'kJ/h';
         
         SET
@@ -111 +111 @@
         CONNECTIONS
         s1.Outlet to fl.Inlet;
-        Q.Outlet to fl.InletQ;
+        Q.OutletQ to fl.InletQ;
         
         SPECIFY
@@ -122 +122 @@
         fl.OutletL.P = 2.5 * 'atm';
 
-        #Q.Outlet = 0 * 'kJ/h';
+        #Q.OutletQ.Q = 0 * 'kJ/h';
         fl.OutletL.T = 315.06 * 'K';
         

trunk/sample/stage_separators/sample_reboiler.mso

@@ -49 +49 @@
         feed to r1.Inlet;
         s1.Outlet to r1.InletL;
-        Q.Outlet to r1.InletQ;
+        Q.OutletQ to r1.InletQ;
         
         SPECIFY
@@ -67 +67 @@
         r1.OutletV.F = 111.6 * 'kmol/h';
 
-        Q.Outlet.Q = 3.7743e6 * 'kJ/h';
+        Q.OutletQ.Q = 3.7743e6 * 'kJ/h';
 
         SET
@@ -106 +106 @@
         CONNECTIONS
         s1.Outlet to r1.InletL;
-        Q.Outlet to r1.InletQ;
+        Q.OutletQ to r1.InletQ;
         
         SPECIFY
@@ -114 +114 @@
         s1.Outlet.z = [0.006061, 0.9939];
         
-#       Q.Outlet.Q = 3.7743e6 * 'kJ/h';
+#       Q.OutletQ.Q = 3.7743e6 * 'kJ/h';
         r1.OutletV.T = 350 * 'K';
 

trunk/sample/stage_separators/sample_tank.mso

@@ -46 +46 @@
         CONNECTIONS
         s.Outlet to t.Inlet;
-        Qtank.Outlet to t.InletQ;
+        Qtank.OutletQ to t.InletQ;
         
         SPECIFY
@@ -55 +55 @@
 #       s.v = 0.698; 
         
-        Qtank.Outlet.Q = 0 * 'J/s';
+        Qtank.OutletQ.Q = 0 * 'J/s';
         t.Outlet.F = 179 * 'kmol/h';
         
@@ -92 +92 @@
         CONNECTIONS
         s.Outlet to t.Inlet;
-        Qtank.Outlet to t.InletQ;
+        Qtank.OutletQ to t.InletQ;
         
         SPECIFY
@@ -101 +101 @@
         #s.v = 0.368;
 
-        Qtank.Outlet.Q = 0 * 'J/s';
+        Qtank.OutletQ.Q = 0 * 'J/s';
         t.Outlet.F = 490 * 'kmol/h';