Changeset 732 for branches


Ignore:
Timestamp:
Feb 26, 2009, 6:47:01 PM (13 years ago)
Author:
gerson bicca
Message:

costs models are obsoletes

Location:
branches/gui
Files:
4 edited

Legend:

Unmodified
Added
Removed
  • branches/gui/eml/costs/column_cost.mso

    r354 r732  
    1616* Author: Núbia do Carmo Ferreira
    1717* $Id: column.mso 210 2007-03-15 12:52:28Z arge $
    18 *---------------------------------------------------------------------*#
     18*---------------------------------------------------------------------#
    1919
    2020using "stage_separators/column";
    2121
    22 #*----------------------------------------------------------------------
     22
     23
     24
     25                                Needs to be Updated !!!!!!!
     26
     27
     28#----------------------------------------------------------------------
    2329* Model of cost of a distillation column containing:
    2430*       - NTrays like tray;
     
    3339*          0.6m < D < 4.8m
    3440*
    35 *---------------------------------------------------------------------*#
     41*---------------------------------------------------------------------#
    3642
    3743Model Distillation_kettle_cond_cost as Distillation_kettle_cond
     
    156162*       - a pump in reflux stream.
    157163*
    158 * ------------------------------------------------------------------*#
     164* ------------------------------------------------------------------#
    159165Model Distillation_thermosyphon_subcooling_cost as Distillation_thermosyphon_subcooling
    160166        ATTRIBUTES
     
    279285*       - a pump in reflux stream.
    280286*
    281 * ------------------------------------------------------------------*#
     287* ------------------------------------------------------------------#
    282288Model Distillation_thermosyphon_cond_cost as Distillation_thermosyphon_cond
    283289        ATTRIBUTES
     
    399405*       - a pump in reflux stream.
    400406*
    401 * ------------------------------------------------------------------*#
     407* ------------------------------------------------------------------#
    402408Model Distillation_kettle_subcooling_cost as Distillation_kettle_subcooling
    403409        ATTRIBUTES
     
    509515        Ws = dens_mass_material*Di*(Lt + 0.8116*Di)*Tp*Pi;
    510516end
     517
     518*#
  • branches/gui/eml/costs/flash_cost.mso

    r331 r732  
    7474        Ce = Cb*Fm + Ca;
    7575       
    76         switch orientation
     76        switch Orientation
    7777                case "vertical":
    7878               
  • branches/gui/sample/costs/sample_distillation_kettle_cond_cost.mso

    r581 r732  
    2424* Author: Núbia do Carmo Ferreira
    2525* $Id: sample_column.mso 247 2007-04-24 13:44:18Z rafael $
    26 *--------------------------------------------------------------------*#
     26*--------------------------------------------------------------------#
     27
     28
     29
     30Needs to be Updated
     31
    2732
    2833using "costs/column_cost";
     
    142147        #Dynamic = false;       
    143148end
     149*#
  • branches/gui/sample/costs/sample_flash_cost.mso

    r581 r732  
    5151       
    5252        EQUATIONS
    53         fl.OutletL.F = 400*sqrt(fl.Level/'m') * 'kmol/h';
     53        fl.OutletLiquid.F = 400*sqrt(fl.Level/'m') * 'kmol/h';
    5454       
    5555        SPECIFY
     
    5959        s1.Composition = [0.2379,0.3082,0.09958,0.1373,0.08872,0.1283];
    6060
    61         fl.OutletV.F = 68.5 * 'kmol/h';
     61        fl.OutletVapour.F = 68.5 * 'kmol/h';
    6262        Q.OutletQ = 0 * 'kJ/h';
    6363       
    6464        SET
    65         fl.V = 50 * 'm^3';
    66         fl.diameter = 2 * 'm';
    67         fl.orientation = "vertical";
     65        fl.VesselVolume = 50 * 'm^3';
     66        fl.Diameter = 2 * 'm';
     67        fl.Orientation = "vertical";
    6868#       fl.orientation = "horizontal";
    6969       
     
    8383        fl.Cost(6,:) = [1.7,0,0];#For "Stainless steell 304"
    8484
    85         INITIAL
    86         fl.OutletL.T = 338 * 'K';
    87         fl.Level = 0.4 * 'm';
     85        SET
     86       
     87        fl.Levelpercent_Initial =0.4 * 'm';
     88        fl.Temperature_Initial  = 338 * 'K';
     89        fl.Composition_Initial=0.1;
    8890
    89         fl.OutletL.z(1) = 0.1;
    90         fl.OutletL.z(2) = 0.1;
    91         fl.OutletL.z(3) = 0.1;
    92         fl.OutletL.z(4) = 0.1;
    93         fl.OutletL.z(5) = 0.1;
    94        
    95         OPTIONS
     91OPTIONS
    9692        Dynamic = true;
    9793        TimeStep = 0.1;
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