Changeset 325 for trunk/eml/heat_exchangers/DoublePipe.mso

Timestamp:

Jul 28, 2007, 9:41:04 PM (16 years ago)

Author:

Argimiro Resende Secchi

Message:

Set icons positions for most devices.

File:

• trunk/eml/heat_exchangers/DoublePipe.mso (modified) (2 diffs)

trunk/eml/heat_exchangers/DoublePipe.mso

@@ -29 +29 @@
 PARAMETERS
 
-outer PP                        as Plugin               (Brief="External Physical Properties", Type="PP");
-outer NComp             as Integer      (Brief="Number of Components");
+outer PP            as Plugin           (Brief="External Physical Properties", Type="PP");
+outer NComp     as Integer      (Brief="Number of Components");
         
         M(NComp)        as molweight    (Brief="Component Mol Weight");
         
-        HotSide                                 as Switcher     (Brief="Flag for Fluid Alocation ",Valid=["outer","inner"],Default="outer");
+        HotSide                         as Switcher     (Brief="Flag for Fluid Alocation ",Valid=["outer","inner"],Default="outer");
         innerFlowRegime         as Switcher     (Brief="Inner Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar");
         outerFlowRegime         as Switcher     (Brief="Outer Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar");
@@ -40 +40 @@
         InnerLaminarCorrelation         as Switcher             (Brief="Heat Transfer Correlation in Laminar Flow for the Inner Side",Valid=["Hausen","Schlunder"],Default="Hausen");
         InnerTransitionCorrelation  as Switcher         (Brief="Heat Transfer Correlation in Transition Flow for the Inner Side",Valid=["Gnielinski","ESDU"],Default="Gnielinski");
-        InnerTurbulentCorrelation  as Switcher                  (Brief="Heat Transfer Correlation in Turbulent Flow for the Inner Side",Valid=["Petukhov","SiederTate"],Default="Petukhov");
+        InnerTurbulentCorrelation   as Switcher         (Brief="Heat Transfer Correlation in Turbulent Flow for the Inner Side",Valid=["Petukhov","SiederTate"],Default="Petukhov");
 
         OuterLaminarCorrelation         as Switcher             (Brief="Heat Transfer Correlation in Laminar Flow for the Outer Side",Valid=["Hausen","Schlunder"],Default="Hausen");
         OuterTransitionCorrelation  as Switcher         (Brief="Heat Transfer Correlation in Transition Flow for the OuterSide",Valid=["Gnielinski","ESDU"],Default="Gnielinski");
-        OuterTurbulentCorrelation  as Switcher          (Brief="Heat Transfer Correlation in Turbulent Flow for the Outer Side",Valid=["Petukhov","SiederTate"],Default="Petukhov");
-
-        Pi                      as constant             (Brief="Pi Number",Default=3.14159265);
-        DoInner  as length                      (Brief="Outside Diameter of Inner Pipe",Lower=1e-6);
+        OuterTurbulentCorrelation   as Switcher         (Brief="Heat Transfer Correlation in Turbulent Flow for the Outer Side",Valid=["Petukhov","SiederTate"],Default="Petukhov");
+
+        Pi              as constant             (Brief="Pi Number",Default=3.14159265);
+        DoInner as length                       (Brief="Outside Diameter of Inner Pipe",Lower=1e-6);
         DiInner as length                       (Brief="Inside Diameter of Inner Pipe",Lower=1e-10);
         DiOuter as length                       (Brief="Inside Diameter of Outer pipe",Lower=1e-10);
-        Lpipe           as length                       (Brief="Effective Tube Length",Lower=0.1);
-        Kwall           as conductivity         (Brief="Tube Wall Material Thermal Conductivity",Default=1.0);
-        Rfi                     as positive                     (Brief="Inside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0);
+        Lpipe   as length                       (Brief="Effective Tube Length",Lower=0.1);
+        Kwall   as conductivity         (Brief="Tube Wall Material Thermal Conductivity",Default=1.0);
+        Rfi             as positive                     (Brief="Inside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0);
         Rfo             as positive                     (Brief="Outside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0);
 
 VARIABLES
 
-in      InletInner              as stream                       (Brief="Inlet Inner Stream");   
-in      InletOuter              as stream                       (Brief="Inlet Outer Stream");
-out     OutletInner             as streamPH             (Brief="Outlet Inner Stream");
-out     OutletOuter     as streamPH             (Brief="Outlet Outer Stream");
-
-        Details                 as Details_Main                 (Brief="Some Details in the Heat Exchanger");
-        Inner                   as Main_DoublePipe              (Brief="Inner Side of the Heat Exchanger");
-        Outer                   as Main_DoublePipe              (Brief="Outer Side of the Heat Exchanger");
+in  InletInner          as stream               (Brief="Inlet Inner Stream", PosX=0, PosY=0.5225);      
+in  InletOuter          as stream               (Brief="Inlet Outer Stream", PosX=0.2805, PosY=0);
+out OutletInner         as streamPH     (Brief="Outlet Inner Stream", PosX=1, PosY=0.5225);
+out OutletOuter         as streamPH     (Brief="Outlet Outer Stream", PosX=0.7264, PosY=1);
+
+        Details         as Details_Main         (Brief="Some Details in the Heat Exchanger");
+        Inner                   as Main_DoublePipe      (Brief="Inner Side of the Heat Exchanger");
+        Outer                   as Main_DoublePipe      (Brief="Outer Side of the Heat Exchanger");
 
 SET