Ignore:
Timestamp:
Nov 7, 2006, 2:11:10 PM (16 years ago)
Author:
gerson bicca
Message:

updated heat exchanger model

File:
1 edited

Legend:

Unmodified
Added
Removed
  • mso/sample/heat_exchangers/sampleNTU.mso

    r26 r45  
    66PARAMETERS
    77
    8 PP               as CalcObject (Brief="Physical Properties",File="vrpp");
    9 HE           as CalcObject (Brief="Heat Exchangers Calculations",File="Heatex");
     8PP        as CalcObject (Brief="Physical Properties",File="vrpp");
    109NComp as Integer;
    1110       
     11
     12       
     13DEVICES
     14exchanger       as HeatExchanger_NTU;
     15streamhot       as streamTP;
     16streamcold  as streamTP;
     17
    1218SET
    1319
     
    1622PP.Components   = ["water","n-butane", "benzene", "n-octane" ];
    1723NComp                                           = PP.NumberOfComponents;
    18 HE.FlowDirection    = "Cocurrent";
    19        
    20 DEVICES
    21 exchanger       as HeatExchanger_NTU;
    22 streamhot       as streamTP;
    23 streamcold  as streamTP;
    24        
     24exchanger.HE.FlowDirection    = "Cocurrent";
     25
    2526CONNECTIONS
    2627
    2728streamhot               to exchanger.Inlet.Hot;
    28 streamcold      to exchanger.Inlet.Cold;
     29streamcold              to exchanger.Inlet.Cold;
    2930       
    3031SPECIFY
     
    4142streamcold.T            = 300 * "K";   
    4243streamcold.z            = [0,0.5, 0.1, 0.4];
    43 exchanger.Outlet.Cold.T = 350*"K";
     44exchanger.Outlet.Cold.T = 340*"K";
    4445       
    4546OPTIONS
    46  mode                     = "steady";
     47 mode   = "steady";
    4748 end
Note: See TracChangeset for help on using the changeset viewer.