Changeset 739 for branches/gui/eml/mixers_splitters/splitter.mso

Timestamp:

Feb 27, 2009, 7:18:32 PM (13 years ago)

Author:

gerson bicca

Message:

updates (changes in icons/models/samples)

File:

• branches/gui/eml/mixers_splitters/splitter.mso (modified) (3 diffs)

branches/gui/eml/mixers_splitters/splitter.mso

@@ -23 +23 @@
 Model splitter_n
         ATTRIBUTES
-        Pallete         = true;
+        Pallete         = false;
         Icon            = "icon/splitter_n"; 
-        Brief           = "Model of a splitter";
+        Brief           = "Model of a splitter (NOT Handled by the GUI)";
         Info            =
 "== Assumptions ==
@@ -75 +75 @@
 end
 
-
-Model splitter
+Model splitter2
         ATTRIBUTES
         Pallete         = true;
@@ -83 +82 @@
         Info            =
 "== Assumptions ==
-* thermodynamics equilibrium
-* adiabatic
+*Thermodynamics equilibrium
+*Adiabatic
                         
 == Specify ==
-* the inlet stream
-* (Noutlet - 1) fraction of split of the outlet streams:
-
-        frac(i) = (Mole Flow of the outlet stream i / 
+* The inlet stream
+* One FlowRatios of split of the outlet streams:
+
+        FlowRatios(i) = (Mole Flow of the outlet stream i / 
                                 Mole Flow of the inlet stream)
-                                where i = 1, 2,...,Noutlet
+                                where i = 1, 2
 ";
 
-        VARIABLES
+VARIABLES
 in  Inlet   as stream (Brief = "Inlet stream", PosX=0, PosY=0.5069, Symbol="_{in}");
 out Outlet1 as stream (Brief = "Outlet stream 1", PosX=1, PosY=0.3027, Symbol="_{out1}");
 out Outlet2 as stream (Brief = "Outlet stream 2", PosX=1, PosY=0.7141, Symbol="_{out2}");
-        frac as fraction (Brief = "Fraction to Outlet 1", Symbol="\phi");
-
-        EQUATIONS
-        "Flow"
-        Outlet1.F = Inlet.F * frac;
+        FlowRatios(2)   as fraction     (Brief = "Distribution of Outlets", Default=0.33, Symbol="\phi");
+
+EQUATIONS
+
+"Normalize Flow Ratios" 
+        sum(FlowRatios) = 1;
+        
+"Flow"
+        Outlet1.F = Inlet.F * FlowRatios(1);
         Outlet1.F + Outlet2.F = Inlet.F;
-        "Composition"
+
+"Composition"
         Outlet1.z = Inlet.z;
         Outlet2.z = Inlet.z;
-        "Pressure"
+
+"Pressure"
         Outlet1.P = Inlet.P;
         Outlet2.P = Inlet.P;
-        "Enthalpy"
+
+"Enthalpy"
         Outlet1.h = Inlet.h;
         Outlet2.h = Inlet.h;
-        "Temperature"
+
+"Temperature"
         Outlet1.T = Inlet.T;
         Outlet2.T = Inlet.T;
-        "Vapourisation Fraction"
+
+"Vapourisation Fraction"
         Outlet1.v = Inlet.v;
         Outlet2.v = Inlet.v;
+
 end
+
+Model splitter3
+        ATTRIBUTES
+        Pallete         = true;
+        Icon            = "icon/splitter"; 
+        Brief           = "Model of a splitter with 3 outlet streams";
+        Info            =
+"== Assumptions ==
+* Thermodynamics equilibrium
+* Adiabatic
+                        
+== Specify ==
+*The inlet stream
+*Two FlowRatios of split of the outlet streams:
+
+        FlowRatios(i) = (Mole Flow of the outlet stream i / 
+                                Mole Flow of the inlet stream)
+                                where i = 1, 2, 3
+";
+        
+VARIABLES
+
+in      Inlet                           as stream       (Brief = "Inlet stream", PosX=0, PosY=0.5001, Symbol="_{in}");
+out  Outlet1    as stream       (Brief = "Outlet stream 1", PosX=1, PosY=0.25, Symbol="_{Out1}");
+out  Outlet2    as stream       (Brief = "Outlet stream 2", PosX=1, PosY=0.5059, Symbol="_{Out2}");
+out  Outlet3    as stream       (Brief = "Outlet stream 3", PosX=1, PosY=0.75, Symbol="_{Out3}");
+
+        FlowRatios(3)   as fraction     (Brief = "Distribution of Outlets", Default=0.33, Symbol="\phi");
+
+EQUATIONS
+        
+"Normalize Flow Ratios" 
+        sum(FlowRatios) = 1;
+        
+"Outlet1 Flow"
+        Outlet1.F = Inlet.F*FlowRatios(1);
+        
+"Outlet2 Flow"
+        Outlet2.F = Inlet.F*FlowRatios(2);
+        
+"Outlet3 Flow"
+        Outlet3.F = Inlet.F*FlowRatios(3);
+        
+"Outlet1 Composition"
+        Outlet1.z = Inlet.z;
+
+"Outlet2 Composition"
+        Outlet2.z = Inlet.z;
+
+"Outlet3 Composition"
+        Outlet3.z = Inlet.z;
+
+"Outlet1 Pressure"
+        Outlet1.P = Inlet.P;
+
+"Outlet2 Pressure"
+        Outlet2.P = Inlet.P;
+
+"Outlet3 Pressure"
+        Outlet3.P = Inlet.P;
+
+"Outlet1 Enthalpy"
+        Outlet1.h = Inlet.h;
+
+"Outlet2 Enthalpy"
+        Outlet2.h = Inlet.h;
+
+"Outlet3 Enthalpy"
+        Outlet3.h = Inlet.h;
+        
+"Outlet1 Temperature"   
+        Outlet1.T = Inlet.T;
+
+"Outlet2 Temperature"   
+        Outlet2.T = Inlet.T;
+
+"Outlet3 Temperature"   
+        Outlet3.T = Inlet.T;
+
+"Outlet1 Vapourisation Fraction"
+        Outlet1.v = Inlet.v;
+
+"Outlet2 Vapourisation Fraction"
+        Outlet2.v = Inlet.v;
+        
+"Outlet3 Vapourisation Fraction"
+        Outlet3.v = Inlet.v;
+
+end