Changeset 135 for branches/newlanguage/sample

Timestamp:

Jan 25, 2007, 6:00:26 PM (17 years ago)

Author:

gerson bicca

Message:

updated models and samples for the new language

Location:

branches/newlanguage/sample/heat_exchangers

Files:

• Eshell_Detailed_LMTD.mso (modified) (1 diff)
• Mheatex_sample2.mso (modified) (7 diffs)

branches/newlanguage/sample/heat_exchangers/Eshell_Detailed_LMTD.mso

@@ -56 +56 @@
 
 #   LMTD Correction Factor
-        exchanger.HE.LMTDcorrection     = "Fakeri";
-#       exchanger.HE.LMTDcorrection     = "Bowmann";
+        exchanger.HE.LMTDcorrection     = "Bowmann";
 
 #   Heat Transfer Correlation

branches/newlanguage/sample/heat_exchangers/Mheatex_sample2.mso

@@ -1 @@
-using "Mheatex";
+
+using "heat_exchangers/Mheatex";
 
 FlowSheet MHeater
-        
+
+PARAMETERS
+
+        PP                      as Plugin       (File="vrpp");
+        NComp           as Integer      (Brief="Number Components");
+
 DEVICES
 
@@ -9 +15 @@
         streamhot1              as source;
         streamhot2              as source;
-        streamcold2             as source;
+        streamcold2     as source;
         
 CONNECTIONS
-
         streamcold1.Outlet      to Mheater.Inlet.Cold(1);
         streamhot1.Outlet       to Mheater.Inlet.Hot(1);
@@ -18 +23 @@
         streamcold2.Outlet      to Mheater.Inlet.Cold(2);
         
-PARAMETERS
-
-        PP                      as Plugin       (File="vrpp");
-        NComp           as Integer              (Brief="Number Components");
-        Ncold           as Integer              (Brief="Number of Inlet Cold Streams");
-        Nhot            as Integer              (Brief="Number of Inlet Hot Streams");
-        
 SET
 
-        PP.LiquidModel  = "PR";
+        PP.LiquidModel          = "PR";
         PP.VapourModel  = "PR";
         PP.Components   = ["water","methanol","benzene", "toluene"];
-        NComp                   = PP.NumberOfComponents;
-        Mheater.Nhot            = 2;
-    Mheater.Ncold               = 2;
+        NComp                           = PP.NumberOfComponents;
+        Mheater.Nhot      = 2;
+    Mheater.Ncold     = 2;
         
 SPECIFY
@@ -41 +39 @@
         streamcold1.Outlet.P            = 1     * "atm";
         streamcold1.Outlet.T            = 278   * "K";
-        streamcold1.Outlet.v            = 0;
-   streamcold1.Outlet.z                 = [1,0,0,0];
+    streamcold1.Outlet.z                = [1,0,0,0];
         
         streamcold2.Outlet.F            = 50   * "kmol/h";
         streamcold2.Outlet.P            = 1     * "atm";
         streamcold2.Outlet.T            = 298   * "K";
-        streamcold2.Outlet.v            = 0;
     streamcold2.Outlet.z                = [1,0,0,0];
 
@@ -56 +52 @@
         streamhot1.Outlet.P             = 1     * "atm";
         streamhot1.Outlet.T             = 330   * "K";
-        streamhot1.Outlet.v             = 0;
     streamhot1.Outlet.z                 = [0,1,0,0];
         
@@ -62 +57 @@
         streamhot2.Outlet.P             = 1     * "atm";
         streamhot2.Outlet.T             = 340   * "K";
-        streamhot2.Outlet.v             = 0;
     streamhot2.Outlet.z                 = [0,0,0.75,0.25];
         
@@ -77 +71 @@
         Mheater.Outlet.Hot(1).P         = 1 * "atm";
         Mheater.Outlet.Hot(2).P         = 1 * "atm";
-        Mheater.Outlet.Cold(1).P        = 1 * "atm";
-        Mheater.Outlet.Cold(2).P        = 1 * "atm";
+        Mheater.Outlet.Cold(1).P   = 1 * "atm";
+        Mheater.Outlet.Cold(2).P   = 1 * "atm";
         
 OPTIONS