Changeset 421 for trunk/eml/reactors/tank_basic.mso

Timestamp:

Nov 29, 2007, 10:05:51 AM (16 years ago)

Author:

Rodolfo Rodrigues

Message:

Added symbols

File:

• trunk/eml/reactors/tank_basic.mso (modified) (11 diffs)

trunk/eml/reactors/tank_basic.mso

@@ -17 +17 @@
 *----------------------------------------------------------------------
 *
+*   Description:
+*       Generic model for a dynamic tank.
 *
+*   Assumptions:
+*               * single- and two-phases involved
+*       * dynamic
 *
 *----------------------------------------------------------------------
@@ -28 +33 @@
 
 Model tank_basic
+        ATTRIBUTES
+        Brief   = "Basic model for a dynamic tank";
+        
         PARAMETERS
-outer PP                as Plugin (Brief="External physical properties", Type="PP");
-outer   NComp   as Integer (Brief="Number of components", Default=1);
+outer PP        as Plugin       (Brief="External physical properties", Type="PP");
+outer NComp as Integer  (Brief="Number of components", Default=1);
         
         VARIABLES
-in      Inlet   as stream;              # Inlet stream
-out     Outletm as stream;              # Intermediary outlet stream
+in      Inlet   as stream       (Brief="Inlet stream", PosX=0, PosY=0, Symbol="_{in}");
+out     Outletm as stream       (Brief="Intermediary outlet stream", Symbol="_{outm}");
 
         M(NComp)as mol          (Brief="Component molar holdup");
         Mt              as mol          (Brief="Total component molar holdup");
-        V               as volume       (Brief="Volume of reactional mixture");
+        Vr              as volume       (Brief="Volume of reactional mixture");
         E               as energy       (Brief="Internal energy");
         Q               as heat_rate(Brief="Reactor duty", Default=0);
@@ -53 +61 @@
         
         "Mole fraction normalisation"
-        sum(Outletm.z) = 1.0;
+        sum(Outletm.z) = 1;
         
         "Energy balance"
@@ -59 +67 @@
         
         "Geometry"
-        V = Across*Level;
-end
-
-
-#*---------------------------------------------------------------------
-*       only liquid phase
-*--------------------------------------------------------------------*#
-
-Model tank_liq as tank_basic
-        EQUATIONS
-        "Vapourisation fraction"
-        Outletm.v = 0.0;
-
-        "Liquid Enthalpy"
-        Outletm.h = PP.LiquidEnthalpy(Outletm.T,Outletm.P,Outletm.z);
-        
-        "Volume constraint"
-        V = Mt*PP.LiquidVolume(Outletm.T,Outletm.P,Outletm.z);
-        
-        "Total internal energy"
-        E = Mt*Outletm.h - Outletm.P*V;
+        Vr = Across*Level;
 end
 
@@ -86 +74 @@
 *       only vapour phase
 *--------------------------------------------------------------------*#
-
 Model tank_vap as tank_basic
+        ATTRIBUTES
+        Brief   = "Model of a generic vapour-phase tank";
+        
         EQUATIONS
         "Vapourisation fraction"
-        Outletm.v = 1.0;
+        Outletm.v = 1;
 
         "Vapour Enthalpy"
@@ -96 +86 @@
 
         "Volume constraint"
-        V = Mt*PP.VapourVolume(Outletm.T,Outletm.P,Outletm.z);
+        Vr = Mt*PP.VapourVolume(Outletm.T,Outletm.P,Outletm.z);
 
         "Total internal energy"
@@ -104 +94 @@
 
 #*---------------------------------------------------------------------
+*       only liquid phase
+*--------------------------------------------------------------------*#
+Model tank_liq as tank_basic
+        ATTRIBUTES
+        Brief   = "Model of a generic liquid-phase tank";
+        
+        EQUATIONS
+        "Vapourisation fraction"
+        Outletm.v = 0;
+
+        "Liquid Enthalpy"
+        Outletm.h = PP.LiquidEnthalpy(Outletm.T,Outletm.P,Outletm.z);
+        
+        "Volume constraint"
+        Vr = Mt*PP.LiquidVolume(Outletm.T,Outletm.P,Outletm.z);
+        
+        "Total internal energy"
+        E = Mt*Outletm.h - Outletm.P*Vr;
+end
+
+
+#*---------------------------------------------------------------------
 *       liquid and vapour phases
 *--------------------------------------------------------------------*#
-
 Model tank_liqvap
+        ATTRIBUTES
+        Brief   = "Model of a generic two-phase tank";
+        
         PARAMETERS
 outer PP                as Plugin(Brief="External physical properties", Type="PP");
@@ -113 +127 @@
 
         VARIABLES
-in      Inlet    as stream;                     # Inlet stream
-out     OutletmL as liquid_stream;      # Intermediary liquid outlet stream
-out     OutletV  as vapour_stream;      # Outlet vapour stream
+in      Inlet    as stream                      (Brief="Inlet stream", PosX=0, PosY=0, Symbol="_{in}");
+out     OutletmL as liquid_stream       (Brief="Intermediary liquid outlet stream", Symbol="_{outmL}");
+out     OutletV  as vapour_stream       (Brief="Outlet vapour stream", Symbol="_{outV}");
 
         M(NComp)as mol                  (Brief="Component molar holdup");
         ML              as mol                  (Brief="Molar liquid holdup");
         MV              as mol                  (Brief="Molar vapour holdup");
-        V               as volume               (Brief="Volume of reactional mixture");
+        Vr              as volume               (Brief="Volume of reactional mixture");
         E               as energy               (Brief="Internal energy");
         Q               as heat_rate    (Brief="Reactor duty", Default=0);
@@ -137 +151 @@
         
         "Mole fraction normalisation"
-        sum(OutletmL.z) = 1.0;
+        sum(OutletmL.z) = 1;
         
         "Mole fraction normalisation"
@@ -144 +158 @@
         
         "Vapourisation fraction"
-        OutletV.v = 1.0;
+        OutletV.v = 1;
         
         "Vapourisation fraction"
-        OutletmL.v = 0.0;
+        OutletmL.v = 0;
         
         
@@ -157 +171 @@
         
         "Geometry constraint"
-        V = ML*vL + MV*PP.VapourVolume(OutletV.T,OutletV.P,OutletV.z);
+        Vr = ML*vL + MV*PP.VapourVolume(OutletV.T,OutletV.P,OutletV.z);