Ignore:
Timestamp:
Aug 30, 2007, 2:17:16 PM (15 years ago)
Author:
Argimiro Resende Secchi
Message:

Fixing more wiki notation.

File:
1 edited

Legend:

Unmodified
Added
Removed
  • trunk/eml/costs/column_cost.mso

    r331 r354  
    4141        Brief           = "Model of a distillation column with dynamic condenser and dynamic reboiler.";
    4242        Info            =
    43         "Specify:
    44          * the feed stream of each tray (Inlet);
    45          * the Murphree eficiency for each tray Emv;
    46          * the pump pressure difference;
    47          * the heat supllied in reboiler and condenser;
    48          * the condenser vapor outlet flow (OutletV.F);
    49          * the reboiler liquid outlet flow (OutletL.F);
    50          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    51          * all necessary dimensions and materials for cost evaluation
    52        
    53         Initial Conditions:
    54          * the trays temperature (OutletL.T);
    55          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    56          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    57        
    58          * the condenser temperature (OutletL.T);
    59          * the condenser liquid level (Level);
    60          * (NoComps - 1) OutletL (OR OutletV) compositions;
    61        
    62          * the reboiler temperature (OutletL.T);
    63          * the reboiler liquid level (Level);
    64          * (NoComps - 1) OutletL (OR OutletV) compositions.
    65         ";
     43"== Specify ==
     44* the feed stream of each tray (Inlet);
     45* the Murphree eficiency for each tray Emv;
     46* the pump pressure difference;
     47* the heat supllied in reboiler and condenser;
     48* the condenser vapor outlet flow (OutletV.F);
     49* the reboiler liquid outlet flow (OutletL.F);
     50* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     51* all necessary dimensions and materials for cost evaluation
     52       
     53== Initial Conditions ==
     54* the trays temperature (OutletL.T);
     55* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     56* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     57       
     58* the condenser temperature (OutletL.T);
     59* the condenser liquid level (Level);
     60* (NoComps - 1) OutletL (OR OutletV) compositions;
     61       
     62* the reboiler temperature (OutletL.T);
     63* the reboiler liquid level (Level);
     64* (NoComps - 1) OutletL (OR OutletV) compositions.
     65";
    6666
    6767        PARAMETERS
     
    163163        Brief           = "Model of a distillation column with steady condenser and steady reboiler.";
    164164        Info            =
    165         "Specify:
    166          * the feed stream of each tray (Inlet);
    167          * the Murphree eficiency for each tray Emv;
    168          * the pump head;
    169          * the condenser pressure drop;
    170          * the heat supllied in top and bottom tanks;
    171          * the heat supllied in condenser and reboiler;
    172          * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
    173          * both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    174          * all necessary dimensions and materials for cost evaluation
    175 
    176         Initial Conditions:
    177          * the trays temperature (OutletL.T);
    178          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    179          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    180        
    181          * the top tank temperature (OutletL.T);
    182          * the top tank liquid level (Level);
    183          * (NoComps - 1) OutletL (OR OutletV) compositions;
    184        
    185          * the bottom tank temperature (OutletL.T);
    186          * the bottom tank liquid level (Level);
    187          * (NoComps - 1) OutletL (OR OutletV) compositions.
    188         ";
     165"== Specify ==
     166* the feed stream of each tray (Inlet);
     167* the Murphree eficiency for each tray Emv;
     168* the pump head;
     169* the condenser pressure drop;
     170* the heat supllied in top and bottom tanks;
     171* the heat supllied in condenser and reboiler;
     172* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
     173* both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     174* all necessary dimensions and materials for cost evaluation
     175
     176== Initial Conditions ==
     177* the trays temperature (OutletL.T);
     178* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     179* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     180       
     181* the top tank temperature (OutletL.T);
     182* the top tank liquid level (Level);
     183* (NoComps - 1) OutletL (OR OutletV) compositions;
     184       
     185* the bottom tank temperature (OutletL.T);
     186* the bottom tank liquid level (Level);
     187* (NoComps - 1) OutletL (OR OutletV) compositions.
     188";
    189189
    190190        PARAMETERS
     
    286286        Brief           = "Model of a distillation column with dynamic condenser and steady reboiler.";
    287287        Info            =
    288         "Specify:
    289          * the feed stream of each tray (Inlet);
    290          * the Murphree eficiency for each tray Emv;
    291          * the pump head;
    292          * the condenser vapor outlet flow (OutletV.F);
    293          * the heat supllied in bottom tank;
    294          * the heat supllied in condenser and reboiler;
    295          * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
    296          * all necessary dimensions and materials for cost evaluation
    297 
    298         Initial Conditions:
    299          * the trays temperature (OutletL.T);
    300          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    301          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    302        
    303          * the condenser temperature (OutletL.T);
    304          * the condenser liquid level (Level);
    305          * (NoComps - 1) OutletL (OR OutletV) compositions;
    306        
    307          * the bottom tank temperature (OutletL.T);
    308          * the bottom tank liquid level (Level);
    309          * (NoComps - 1) OutletL (OR OutletV) compositions.
    310         ";
     288"== Specify ==
     289* the feed stream of each tray (Inlet);
     290* the Murphree eficiency for each tray Emv;
     291* the pump head;
     292* the condenser vapor outlet flow (OutletV.F);
     293* the heat supllied in bottom tank;
     294* the heat supllied in condenser and reboiler;
     295* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
     296* all necessary dimensions and materials for cost evaluation
     297
     298== Initial Conditions ==
     299* the trays temperature (OutletL.T);
     300* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     301* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     302       
     303* the condenser temperature (OutletL.T);
     304* the condenser liquid level (Level);
     305* (NoComps - 1) OutletL (OR OutletV) compositions;
     306       
     307* the bottom tank temperature (OutletL.T);
     308* the bottom tank liquid level (Level);
     309* (NoComps - 1) OutletL (OR OutletV) compositions.
     310";
    311311
    312312        PARAMETERS
     
    406406        Brief           = "Model of a distillation column with steady condenser and dynamic reboiler.";
    407407        Info            =
    408         "Specify:
    409          * the feed stream of each tray (Inlet);
    410          * the Murphree eficiency for each tray (Emv);
    411          * the pump pressure difference;
    412          * the heat supllied in reboiler and condenser;
    413          * the heat supllied in the top tank;
    414          * the condenser pressure drop;
    415          * the reboiler liquid outlet flow (OutletL.F);
    416          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    417          * all necessary dimensions and materials for cost evaluation
    418 
    419         Initial Conditions:
    420          * the trays temperature (OutletL.T);
    421          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    422          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    423        
    424          * the top tank temperature (OutletL.T);
    425          * the top tank liquid level (Level);
    426          * (NoComps - 1) OutletL (OR OutletV) compositions;
    427        
    428          * the reboiler temperature (OutletL.T);
    429          * the reboiler liquid level (Level);
    430          * (NoComps - 1) OutletL (OR OutletV) compositions.
    431         ";
     408"== Specify ==
     409* the feed stream of each tray (Inlet);
     410* the Murphree eficiency for each tray (Emv);
     411* the pump pressure difference;
     412* the heat supllied in reboiler and condenser;
     413* the heat supllied in the top tank;
     414* the condenser pressure drop;
     415* the reboiler liquid outlet flow (OutletL.F);
     416* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     417* all necessary dimensions and materials for cost evaluation
     418
     419== Initial Conditions ==
     420* the trays temperature (OutletL.T);
     421* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     422* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     423       
     424* the top tank temperature (OutletL.T);
     425* the top tank liquid level (Level);
     426* (NoComps - 1) OutletL (OR OutletV) compositions;
     427       
     428* the reboiler temperature (OutletL.T);
     429* the reboiler liquid level (Level);
     430* (NoComps - 1) OutletL (OR OutletV) compositions.
     431";
    432432
    433433        PARAMETERS
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