Changeset 88 for mso


Ignore:
Timestamp:
Dec 11, 2006, 11:31:56 AM (16 years ago)
Author:
Paula Bettio Staudt
Message:

Updated sample_column and sample_tank to run with VRTherm DEMO

Location:
mso/sample/stage_separators
Files:
2 edited

Legend:

Unmodified
Added
Removed

  • mso/sample/stage_separators/sample_column.mso

    r86 r88  
    1717*--------------------------------------------------------------------
    1818*
    19 * This sample file needs VRTherm (www.vrtech.com.br) to run.
     19* This sample file needs VRTherm DEMO(www.vrtech.com.br) to run
     20* SectionColumn_Test and needs VRTherm full to run the distillation
     21* column flowsheet.
    2022*
    2123*----------------------------------------------------------------------
    … …  
    3335
    3436        SET
    35         PP.Components = [ "isobutane", "n-pentane"];
     37        PP.Components = [ "isobutane", "benzene"];
    3638        PP.LiquidModel = "PR";
    3739        PP.VapourModel = "PR";
    … …  
    109111
    110112        SET
    111         PP.Components = [ "isobutane", "n-pentane"];
     113        PP.Components = [ "isobutane", "benzene"];
    112114        PP.LiquidModel = "PR";
    113115        PP.VapourModel = "PR";

  • mso/sample/stage_separators/sample_tank.mso

    r86 r88  
    1717*--------------------------------------------------------------------
    1818*
    19 * This sample file needs VRTherm (www.vrtech.com.br) to run.
     19* This sample file needs VRTherm DEMO(www.vrtech.com.br) to run.
    2020*
    2121*----------------------------------------------------------------------
    … …  
    3030        NComp   as Integer;
    3131        SET
    32         PP.Components = ["ethane", "propane", "propylene", "1-butene", "n-hexane"];
     32        PP.Components = ["methane", "isobutane", "benzene"];
    3333        PP.LiquidModel = "PR";
    3434        PP.VapourModel = "PR";
    … …  
    6262        t.Outlet.T = 305 *"K";
    6363        t.Level = 0.5 * "m";
    64         t.Outlet.z([1:4]) = 1.0/NComp;
     64        t.Outlet.z([1:2]) = 1.0/NComp;
    6565       
    6666        OPTIONS
    … …  
    7474        NComp   as Integer;
    7575        SET
    76         PP.Components = ["propane", "propylene", "1-butene","1,3-butadiene", "n-hexane"];
     76        PP.Components = ["methane", "isobutane", "benzene"];
    7777        PP.LiquidModel = "PR";
    7878        PP.VapourModel = "PR";
    … …  
    107107        t.Outlet.T = 280*"K";
    108108        t.Level = 1 * "m";
    109         t.Outlet.z([1:4]) = 1.0/NComp;
     109        t.Outlet.z([1:2]) = 1.0/NComp;
    110110       
    111111        OPTIONS
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