Changeset 489 for trunk/sample/heat_exchangers

Timestamp:

Mar 31, 2008, 4:53:49 PM (15 years ago)

Author:

gerson bicca

Message:

fixed heater/cooler model

File:

• trunk/sample/heat_exchangers/Sample_Heater.mso (modified) (4 diffs)

trunk/sample/heat_exchangers/Sample_Heater.mso

@@ -30 +30 @@
 DEVICES
 
-        Heater          as heater;
-        streamcold      as simple_source;
-        Heat            as energy_source;
+        Heater                  as heater;
+        IN_1                    as source;
+        IN_2                    as source;
+        IN_3                    as source;
+        Heat                    as energy_source;
+        Sink_Stream     as sink;
         
 CONNECTIONS
 
-        streamcold.Outlet       to Heater.Inlet(1);
+        IN_1.Outlet                     to Heater.Inlet(1);
+        IN_2.Outlet                     to Heater.Inlet(2);
+        IN_3.Outlet                     to Heater.Inlet(3);
         Heat.OutletQ            to Heater.InletQ;
-
+        Heater.Outlet        to Sink_Stream.Inlet;
         
 PARAMETERS
 
         PP                      as Plugin (Type ="PP", LiquidModel = "PR",VapourModel  = "PR",
-                                                        Components      = ["isobutane","benzene"]);
+                                                        Components      = ["nitrogen","methane","ethane","propane","n-hexane","n-octane"]);
         NComp           as Integer;
         
@@ -49 +54 @@
 
         NComp           = PP.NumberOfComponents;
-        Heater.Ninlet           = 1;
+        Heater.Ninlet           = 3;
 
 SPECIFY
 
-        streamcold.Outlet.F             = 10   * 'kmol/h';
-        streamcold.Outlet.P             = 1     * 'atm';
-        streamcold.Outlet.T             = 310   * 'K';
-    streamcold.Outlet.z                 = [0.5,0.5];
+        IN_1.Fw                                 = 10   * 'kg/s';
+        IN_1.Outlet.P           = 5     * 'atm';
+        IN_1.Outlet.T           = (30+273)   * 'K';
+    IN_1.Outlet.z               = [0.007,0.75,0.243,0,0,0];
+        
+        IN_2.Fw                                 = 12   * 'kg/s';
+        IN_2.Outlet.P           = 5     * 'atm';
+        IN_2.Outlet.T           = (33+273)   * 'K';
+    IN_2.Outlet.z               = [0.003,0.66,0.33,0.005,0.001,0.001];
+        
+        IN_3.Fw                                 = 12   * 'kg/s';
+        IN_3.Outlet.P           = 2     * 'atm';
+        IN_3.Outlet.T           = (33+273)   * 'K';
+    IN_3.Outlet.z               = [0,0.7,0.30,0,0,0];
 
-        #Heater.Outlet.T                = 360*'K';
-        Heater.Outlet.P                 = 0.999* 'atm';
-        Heat.OutletQ.Q                  = 51* 'kW';
+        #Heater.Outlet.T                = (66+273)*'K';
+        Heater.Outlet.P                 = 5* 'atm';
+        Heater.Outlet.v                 = 0.8;
+        #Heat.OutletQ.Q                 = 2500* 'kW';
 
 OPTIONS
         Dynamic = false;
+        
 end
 
@@ -70 +87 @@
 DEVICES
 
-        Cooler          as cooler;
-        streamhot       as simple_source;
-        Heat            as energy_source;
+        Cooler                  as cooler;
+        IN_1                    as source;
+        IN_2                    as source;
+        IN_3                    as source;
+        Heat                    as energy_source;
+        Sink_Stream     as sink;
         
 CONNECTIONS
 
-        streamhot.Outlet        to Cooler.Inlet(1);
+        IN_1.Outlet                     to Cooler.Inlet(1);
+        IN_2.Outlet                     to Cooler.Inlet(2);
+        IN_3.Outlet                     to Cooler.Inlet(3);
         Heat.OutletQ            to Cooler.InletQ;
-        
+        Cooler.Outlet        to Sink_Stream.Inlet;
         
 PARAMETERS
 
         PP                      as Plugin (Type ="PP", LiquidModel = "PR",VapourModel  = "PR",
-                                                        Components      = ["isobutane","benzene"]);
+                                                        Components      = ["nitrogen","methane","ethane","propane","n-hexane","n-octane"]);
         NComp           as Integer;
         
@@ -89 +111 @@
 
         NComp           = PP.NumberOfComponents;
-        Cooler.Ninlet           = 1;
+        Cooler.Ninlet           = 3;
 
 SPECIFY
 
-        streamhot.Outlet.F              = 10   * 'kmol/h';
-        streamhot.Outlet.P              = 1     * 'atm';
-        streamhot.Outlet.T              = 310   * 'K';
-    streamhot.Outlet.z                  = [0.5,0.5];
+        IN_1.Fw                                 = 10   * 'kg/s';
+        IN_1.Outlet.P           = 5     * 'atm';
+        IN_1.Outlet.T           = (30+273)   * 'K';
+    IN_1.Outlet.z               = [0.007,0.75,0.243,0,0,0];
+        
+        IN_2.Fw                                 = 12   * 'kg/s';
+        IN_2.Outlet.P           = 5     * 'atm';
+        IN_2.Outlet.T           = (33+273)   * 'K';
+    IN_2.Outlet.z               = [0.003,0.66,0.33,0.005,0.001,0.001];
+        
+        IN_3.Fw                                 = 12   * 'kg/s';
+        IN_3.Outlet.P           = 2     * 'atm';
+        IN_3.Outlet.T           = (33+273)   * 'K';
+    IN_3.Outlet.z               = [0,0.7,0.30,0,0,0];
 
-#       Cooler.Outlet.T                 = 300*'K';
-        Cooler.Outlet.P                 = 0.999* 'atm';
-        Heat.OutletQ.Q                  = 10* 'kW';
+        #Cooler.Outlet.T                = (66+273)*'K';
+        Cooler.Outlet.P                 = 5* 'atm';
+        Cooler.Outlet.v                 = 0.8;
+        #Cooler.OutletQ.Q               = 2500* 'kW';
 
 OPTIONS
         Dynamic = false;
+        
 end
+