Ignore:
Timestamp:
Aug 30, 2007, 1:12:27 PM (15 years ago)
Author:
Argimiro Resende Secchi
Message:

Fixing some wiki notation.

File:
1 edited

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Unmodified
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  • trunk/eml/stage_separators/reboiler.mso

    r352 r353  
    2525        Icon            = "icon/Reboiler";
    2626        Brief           = "Model of a dynamic reboiler - kettle.";
    27         Info            = "
    28         <h2>Assumptions</h2>
    29         <ul>
    30         <li>perfect mixing of both phases;
    31         <li>thermodynamics equilibrium;
    32         <li>no liquid entrainment in the vapour stream.
    33         </ul>
    34        
    35         <h2>Specify</h2>
    36         <ul>
    37         <li> the inlet stream;
    38         <li> the liquid inlet stream;
    39         <li> the outlet flows: OutletV.F and OutletL.F;
    40         <li> the heat supply.
    41         </ul>
    42        
    43         <h2>Initial Conditions</h2>
    44         <ul>
    45         <li> the reboiler temperature (OutletL.T);
    46         <li> the reboiler liquid level (Level);
    47         <li> (NoComps - 1) OutletL (OR OutletV) compositions.
    48         </ul>
    49         ";     
     27        Info            =
     28"== Assumptions ==
     29
     30* perfect mixing of both phases;
     31* thermodynamics equilibrium;
     32* no liquid entrainment in the vapour stream.
     33       
     34== Specify ==
     35
     36* the inlet stream;
     37* the liquid inlet stream;
     38* the outlet flows: OutletV.F and OutletL.F;
     39* the heat supply.
     40       
     41== Initial Conditions ==
     42
     43* the reboiler temperature (OutletL.T);
     44* the reboiler liquid level (Level);
     45* (NoComps - 1) OutletL (OR OutletV) compositions.
     46";     
    5047       
    5148        PARAMETERS
     
    125122        Brief           = "Model of a  Steady State reboiler with no thermodynamics equilibrium - thermosyphon.";
    126123        Info            =
    127         "Assumptions:
    128          * perfect mixing of both phases;
    129          * no thermodynamics equilibrium;
    130          * no liquid entrainment in the vapour stream.
    131        
    132         Specify:
    133          * the InletL stream;
    134          * the heat supply OR the outlet temperature (OutletV.T);
    135         ";     
     124"== Assumptions ==
     125* perfect mixing of both phases;
     126* no thermodynamics equilibrium;
     127* no liquid entrainment in the vapour stream.
     128       
     129== Specify ==
     130* the InletL stream;
     131* the heat supply OR the outlet temperature (OutletV.T);
     132";     
    136133
    137134        PARAMETERS
     
    176173        Brief           = "Model of a  Steady State reboiler with fake calculation of outlet conditions.";
    177174        Info            =
    178         "Model of a  Steady State reboiler with fake calculation of
    179         vaporisation fraction and output temperature, but with a real
    180         calculation of the output stream enthalpy.
    181         ";
     175"Model of a  Steady State reboiler with fake calculation of
     176vaporisation fraction and output temperature, but with a real
     177calculation of the output stream enthalpy.
     178";
    182179       
    183180        PARAMETERS
     
    222219        Brief           = "Model of a dynamic reboiler with reaction.";
    223220        Info            =
    224         "Assumptions:
    225          * perfect mixing of both phases;
    226          * thermodynamics equilibrium;
    227          * no liquid entrainment in the vapour stream;
    228          * the reaction takes place only in the liquid phase.
    229        
    230         Specify:
    231          * the kinetics variables;
    232          * the inlet stream;
    233          * the liquid inlet stream;
    234          * the outlet flows: OutletV.F and OutletL.F;
    235          * the heat supply.
    236        
    237         Initial Conditions:
    238          * the reboiler temperature (OutletL.T);
    239          * the reboiler liquid level (Level);
    240          * (NoComps - 1) OutletL (OR OutletV) compositions.
    241         ";
     221"== Assumptions ==
     222* perfect mixing of both phases;
     223* thermodynamics equilibrium;
     224* no liquid entrainment in the vapour stream;
     225* the reaction takes place only in the liquid phase.
     226       
     227== Specify ==
     228* the kinetics variables;
     229* the inlet stream;
     230* the liquid inlet stream;
     231* the outlet flows: OutletV.F and OutletL.F;
     232* the heat supply.
     233
     234== Initial Conditions ==
     235* the reboiler temperature (OutletL.T);
     236* the reboiler liquid level (Level);
     237* (NoComps - 1) OutletL (OR OutletV) compositions.
     238";
    242239       
    243240        PARAMETERS
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