Changeset 353 for trunk/eml


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

Fixing some wiki notation.

Location:
trunk/eml
Files:
11 edited

Legend:

Unmodified
Added
Removed

  • trunk/eml/pressure_changers/compressor.mso

    r351 r353  
    2626        Brief           = "Model of a centrifugal compressor.";
    2727        Info            =
    28         "Assumptions:
    29          * Steady State;
    30          * Only Vapor;
    31          * Adiabatic.
     28"== Assumptions ==
     29* Steady State;
     30* Only Vapor;
     31* Adiabatic.
    3232       
    33         Specify:
    34          * the inlet stream;
    35          * the outlet pressure (Outlet.P);
    36          * the Isentropic efficiency (Effs).
    37         ";
     33== Specify ==
     34* the inlet stream;
     35* the outlet pressure (Outlet.P);
     36* the Isentropic efficiency (Effs).
     37";
    3838       
    3939        PARAMETERS

  • trunk/eml/pressure_changers/pump.mso

    r351 r353  
    2626        Brief           = "Model of a centrifugal pump.";
    2727        Info            =
    28         "Assumptions:
    29          * Steady State;
    30          * Only Liquid;
    31          * Adiabatic;
    32          * Isentropic.
     28"== Assumptions ==
     29* Steady State;
     30* Only Liquid;
     31* Adiabatic;
     32* Isentropic.
    3333       
    34         Specify:
    35          * the inlet stream;
    36          * the Pressure Increase Pdiff.
    37         ";
     34== Specify ==
     35* the inlet stream;
     36* the Pressure Increase Pdiff.
     37";
    3838       
    3939        PARAMETERS

  • trunk/eml/pressure_changers/turbine.mso

    r351 r353  
    2626        Brief           = "Model of a Hidraulic Turbine.";
    2727        Info            =
    28         "Assumptions:
    29          * Steady State;
    30          * Only Liquid;
    31          * Adiabatic;
    32          * Isentropic.
     28"== Assumptions ==
     29* Steady State;
     30* Only Liquid;
     31* Adiabatic;
     32* Isentropic.
    3333       
    34         Specify:
    35          * the inlet stream;
    36          * the Pressure Increase (Pdiff) OR the outlet pressure (Outlet.P);
    37          * the Turbine efficiency (Eff);
    38          * the Brake efficiency (Meff);
    39          * the Volumetric expansivity (Beta).
    40         ";
     34== Specify ==
     35* the inlet stream;
     36* the Pressure Increase (Pdiff) OR the outlet pressure (Outlet.P);
     37* the Turbine efficiency (Eff);
     38* the Brake efficiency (Meff);
     39* the Volumetric expansivity (Beta).
     40";
    4141       
    4242        PARAMETERS

  • trunk/eml/pressure_changers/valve.mso

    r351 r353  
    2727        Brief           = "Model of a valve.";
    2828        Info            =
    29         "Model of valves:
    30          * Linear;
    31          * Parabolic;
    32          * Equal;
    33          * Quick;
    34          * Hyperbolic.
     29"== Model of valves ==
     30* Linear;
     31* Parabolic;
     32* Equal;
     33* Quick;
     34* Hyperbolic.
    3535       
    36         Assumptions:
    37          * Steady State;
    38          * Liquid;
    39          * Isentalpic.
     36== Assumptions ==
     37* Steady State;
     38* Liquid;
     39* Isentalpic.
    4040       
    41         Specify:
    42          * the valve type;
    43          * the inlet stream;
    44          * the Volumetric Flow (Qv);
    45          * the Valve Coefficient (cv);
    46          * the opening (x).
    47         ";
     41== Specify ==
     42* the valve type;
     43* the inlet stream;
     44* the Volumetric Flow (Qv);
     45* the Valve Coefficient (cv);
     46* the opening (x).
     47";
    4848               
    4949        PARAMETERS
    … …  
    142142        Brief           = "Model of a very simple valve - used in distillation column models.";
    143143        Info            =
    144         "Assumptions:
    145          * no flashing liquid in the valve;
    146          * the flow in the valve is adiabatic;
    147          * dynamics in the valve are neglected;
    148          * linear flow type.
     144"== Assumptions ==
     145* no flashing liquid in the valve;
     146* the flow in the valve is adiabatic;
     147* dynamics in the valve are neglected;
     148* linear flow type.
    149149       
    150         Specify:
    151          * the inlet stream
    152          * the plug position (x) OR outlet temperature (Outlet.T) OR outlet pressure (Outlet.P)
     150== Specify ==
     151* the inlet stream
     152* the plug position (x) OR outlet temperature (Outlet.T) OR outlet pressure (Outlet.P)
    153153       
    154154        OR             
    155155       
    156          * the inlet stream excluding its flow (Inlet.F)
    157          * the outlet pressure (Outlet.P) OR outlet flow (Outlet.F)
    158          * the plug position (x)
    159         ";
     156* the inlet stream excluding its flow (Inlet.F)
     157* the outlet pressure (Outlet.P) OR outlet flow (Outlet.F)
     158* the plug position (x)
     159";
    160160
    161161        PARAMETERS

  • trunk/eml/stage_separators/batch_dist.mso

    r352 r353  
    2525        Brief           = "Model of a Batch Differential Distillation.";
    2626        Info            =
    27         "Assumptions:
    28          * perfect mixing of both phases;
    29          * thermodynamics equilibrium;
    30          * no liquid entrainment in the vapour stream.
     27"== Assumptions ==
     28* perfect mixing of both phases;
     29* thermodynamics equilibrium;
     30* no liquid entrainment in the vapour stream.
    3131       
    32         Specify:
    33          * the inlet stream;
    34          * the liquid inlet stream;
    35          * the molar flow of the vapour outlet stream.
     32== Specify ==
     33* the inlet stream;
     34* the liquid inlet stream;
     35* the molar flow of the vapour outlet stream.
    3636       
    37         Initial Conditions:
    38          * the distillator temperature (T);
    39          * the distillator liquid level (Level);
    40          * (NoComps - 1) compositions in the distillator or in the OutletV.
    41         ";
     37== Initial Conditions ==
     38* the distillator temperature (T);
     39* the distillator liquid level (Level);
     40* (NoComps - 1) compositions in the distillator or in the OutletV.
     41";
    4242
    4343        PARAMETERS

  • trunk/eml/stage_separators/column.mso

    r300 r353  
    5050        Brief           = "Model of a column section.";
    5151        Info            =
    52         "Model of a column section containing:
    53          * NTrays trays.
    54        
    55         Specify:
    56          * the feed stream of each tray (Inlet);
    57          * the Murphree eficiency for each tray Emv;
    58          * the InletL stream of the top tray;
    59          * the InletV stream of the bottom tray.
    60        
    61         Initial Conditions:
    62          * the trays temperature (OutletL.T);
    63          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    64          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray.
    65         ";
     52"== Model of a column section containing ==
     53* NTrays trays.
     54       
     55== Specify ==
     56* the feed stream of each tray (Inlet);
     57* the Murphree eficiency for each tray Emv;
     58* the InletL stream of the top tray;
     59* the InletV stream of the bottom tray.
     60       
     61== Initial Conditions ==
     62* the trays temperature (OutletL.T);
     63* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     64* (NoComps - 1) OutletL (OR OutletV) compositions for each tray.
     65";
    6666       
    6767        PARAMETERS
    … …  
    110110        Brief           = "Model of a distillation column with dynamic condenser and dynamic reboiler.";
    111111        Info            =
    112         "Specify:
    113          * the feed stream of each tray (Inlet);
    114          * the Murphree eficiency for each tray Emv;
    115          * the pump pressure difference;
    116          * the heat supllied in reboiler and condenser;
    117          * the condenser vapor outlet flow (OutletV.F);
    118          * the reboiler liquid outlet flow (OutletL.F);
    119          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    120        
    121         Initial Conditions:
    122          * the trays temperature (OutletL.T);
    123          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    124          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    125        
    126          * the condenser temperature (OutletL.T);
    127          * the condenser liquid level (Level);
    128          * (NoComps - 1) OutletL (OR OutletV) compositions;
    129        
    130          * the reboiler temperature (OutletL.T);
    131          * the reboiler liquid level (Level);
    132          * (NoComps - 1) OutletL (OR OutletV) compositions.
    133         ";
     112"== Specify ==
     113* the feed stream of each tray (Inlet);
     114* the Murphree eficiency for each tray Emv;
     115* the pump pressure difference;
     116* the heat supllied in reboiler and condenser;
     117* the condenser vapor outlet flow (OutletV.F);
     118* the reboiler liquid outlet flow (OutletL.F);
     119* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     120       
     121== Initial Conditions ==
     122* the trays temperature (OutletL.T);
     123* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     124* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     125       
     126* the condenser temperature (OutletL.T);
     127* the condenser liquid level (Level);
     128* (NoComps - 1) OutletL (OR OutletV) compositions;
     129       
     130* the reboiler temperature (OutletL.T);
     131* the reboiler liquid level (Level);
     132* (NoComps - 1) OutletL (OR OutletV) compositions.
     133";
    134134       
    135135        PARAMETERS
    … …  
    209209        Brief           = "Model of a distillation column with steady condenser and steady reboiler.";
    210210        Info            =
    211         "Specify:
    212          * the feed stream of each tray (Inlet);
    213          * the Murphree eficiency for each tray Emv;
    214          * the pump head;
    215          * the condenser pressure drop;
    216          * the heat supllied in top and bottom tanks;
    217          * the heat supllied in condenser and reboiler;
    218          * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
    219          * both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    220        
    221         Initial Conditions:
    222          * the trays temperature (OutletL.T);
    223          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    224          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    225        
    226          * the top tank temperature (OutletL.T);
    227          * the top tank liquid level (Level);
    228          * (NoComps - 1) OutletL (OR OutletV) compositions;
    229        
    230          * the bottom tank temperature (OutletL.T);
    231          * the bottom tank liquid level (Level);
    232          * (NoComps - 1) OutletL (OR OutletV) compositions.
    233         ";
     211"== Specify ==
     212* the feed stream of each tray (Inlet);
     213* the Murphree eficiency for each tray Emv;
     214* the pump head;
     215* the condenser pressure drop;
     216* the heat supllied in top and bottom tanks;
     217* the heat supllied in condenser and reboiler;
     218* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
     219* both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     220       
     221== Initial Conditions ==
     222* the trays temperature (OutletL.T);
     223* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     224* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     225       
     226* the top tank temperature (OutletL.T);
     227* the top tank liquid level (Level);
     228* (NoComps - 1) OutletL (OR OutletV) compositions;
     229       
     230* the bottom tank temperature (OutletL.T);
     231* the bottom tank liquid level (Level);
     232* (NoComps - 1) OutletL (OR OutletV) compositions.
     233";
    234234       
    235235        PARAMETERS
    … …  
    314314        Brief           = "Model of a distillation column with dynamic condenser and steady reboiler.";
    315315        Info            =
    316         "Specify:
    317          * the feed stream of each tray (Inlet);
    318          * the Murphree eficiency for each tray Emv;
    319          * the pump head;
    320          * the condenser vapor outlet flow (OutletV.F);
    321          * the heat supllied in bottom tank;
    322          * the heat supllied in condenser and reboiler;
    323          * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
    324        
    325         Initial Conditions:
    326          * the trays temperature (OutletL.T);
    327          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    328          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    329        
    330          * the condenser temperature (OutletL.T);
    331          * the condenser liquid level (Level);
    332          * (NoComps - 1) OutletL (OR OutletV) compositions;
    333        
    334          * the bottom tank temperature (OutletL.T);
    335          * the bottom tank liquid level (Level);
    336          * (NoComps - 1) OutletL (OR OutletV) compositions.
    337         ";
     316"== Specify ==
     317* the feed stream of each tray (Inlet);
     318* the Murphree eficiency for each tray Emv;
     319* the pump head;
     320* the condenser vapor outlet flow (OutletV.F);
     321* the heat supllied in bottom tank;
     322* the heat supllied in condenser and reboiler;
     323* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
     324       
     325== Initial Conditions ==
     326* the trays temperature (OutletL.T);
     327* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     328* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     329       
     330* the condenser temperature (OutletL.T);
     331* the condenser liquid level (Level);
     332* (NoComps - 1) OutletL (OR OutletV) compositions;
     333       
     334* the bottom tank temperature (OutletL.T);
     335* the bottom tank liquid level (Level);
     336* (NoComps - 1) OutletL (OR OutletV) compositions.
     337";
    338338
    339339        PARAMETERS
    … …  
    414414        Brief           = "Model of a distillation column with steady condenser and dynamic reboiler.";
    415415        Info            =
    416         "Specify:
    417          * the feed stream of each tray (Inlet);
    418          * the Murphree eficiency for each tray (Emv);
    419          * the pump pressure difference;
    420          * the heat supllied in reboiler and condenser;
    421          * the heat supllied in the top tank;
    422          * the condenser pressure drop;
    423          * the reboiler liquid outlet flow (OutletL.F);
    424          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    425        
    426         Initial Conditions:
    427          * the trays temperature (OutletL.T);
    428          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    429          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    430        
    431          * the top tank temperature (OutletL.T);
    432          * the top tank liquid level (Level);
    433          * (NoComps - 1) OutletL (OR OutletV) compositions;
    434        
    435          * the reboiler temperature (OutletL.T);
    436          * the reboiler liquid level (Level);
    437          * (NoComps - 1) OutletL (OR OutletV) compositions.
    438         ";
     416"== Specify ==
     417* the feed stream of each tray (Inlet);
     418* the Murphree eficiency for each tray (Emv);
     419* the pump pressure difference;
     420* the heat supllied in reboiler and condenser;
     421* the heat supllied in the top tank;
     422* the condenser pressure drop;
     423* the reboiler liquid outlet flow (OutletL.F);
     424* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     425       
     426== Initial Conditions ==
     427* the trays temperature (OutletL.T);
     428* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     429* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     430       
     431* the top tank temperature (OutletL.T);
     432* the top tank liquid level (Level);
     433* (NoComps - 1) OutletL (OR OutletV) compositions;
     434       
     435* the reboiler temperature (OutletL.T);
     436* the reboiler liquid level (Level);
     437* (NoComps - 1) OutletL (OR OutletV) compositions.
     438";
    439439       
    440440        PARAMETERS
    … …  
    510510        Brief           = "Model of a rectifier column with dynamic condenser.";
    511511        Info            =
    512         "Specify:
    513          * the feed stream of each tray (Inlet);
    514          * the Murphree eficiency for each tray Emv;
    515          * the InletV stream of the bottom tray;
    516          * the pump pressure difference;
    517          * the heat supllied in the condenser;
    518          * the condenser vapor outlet flow (OutletV.F);
    519          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    520        
    521         Initial Conditions:
    522          * the trays temperature (OutletL.T);
    523          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    524          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    525        
    526          * the condenser temperature (OutletL.T);
    527          * the condenser liquid level (Level);
    528          * (NoComps - 1) OutletL (OR OutletV) compositions;
    529         ";
     512"== Specify ==
     513* the feed stream of each tray (Inlet);
     514* the Murphree eficiency for each tray Emv;
     515* the InletV stream of the bottom tray;
     516* the pump pressure difference;
     517* the heat supllied in the condenser;
     518* the condenser vapor outlet flow (OutletV.F);
     519* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     520       
     521== Initial Conditions ==
     522* the trays temperature (OutletL.T);
     523* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     524* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     525       
     526* the condenser temperature (OutletL.T);
     527* the condenser liquid level (Level);
     528* (NoComps - 1) OutletL (OR OutletV) compositions;
     529";
    530530
    531531        PARAMETERS
    … …  
    590590        Brief           = "Model of a rectifier column with steady condenser.";
    591591        Info            =
    592         "Specify:
    593          * the feed stream of each tray (Inlet);
    594          * the Murphree eficiency for each tray Emv;
    595          * the InletV stream of the bottom tray;
    596          * the pump head;
    597          * the condenser pressure drop;
    598          * the heat supllied in  the top tank;
    599          * the heat supllied in condenser;
    600          * both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    601        
    602         Initial Conditions:
    603          * the trays temperature (OutletL.T);
    604          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    605          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    606        
    607          * the top tank temperature (OutletL.T);
    608          * the top tank liquid level (Level);
    609          * (NoComps - 1) OutletL (OR OutletV) compositions;
    610         ";
     592"== Specify ==
     593* the feed stream of each tray (Inlet);
     594* the Murphree eficiency for each tray Emv;
     595* the InletV stream of the bottom tray;
     596* the pump head;
     597* the condenser pressure drop;
     598* the heat supllied in  the top tank;
     599* the heat supllied in condenser;
     600* both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     601       
     602== Initial Conditions ==
     603* the trays temperature (OutletL.T);
     604* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     605* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     606       
     607* the top tank temperature (OutletL.T);
     608* the top tank liquid level (Level);
     609* (NoComps - 1) OutletL (OR OutletV) compositions;
     610";
    611611       
    612612        PARAMETERS
    … …  
    670670        Brief           = "Model of a refluxed stripping column with dynamic condenser.";
    671671        Info            =
    672         "Specify:
    673          * the feed stream of each tray (Inlet);
    674          * the Murphree eficiency for each tray Emv;
    675          * the InletV stream of the bottom tray;
    676          * the pump pressure difference;
    677          * the heat supllied in the condenser;
    678          * the condenser vapor outlet flow (OutletV.F);
    679          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    680        
    681         Initial Conditions:
    682          * the trays temperature (OutletL.T);
    683          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    684          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    685        
    686          * the condenser temperature (OutletL.T);
    687          * the condenser liquid level (Level);
    688          * (NoComps - 1) OutletL (OR OutletV) compositions;
    689         ";
     672"== Specify ==
     673* the feed stream of each tray (Inlet);
     674* the Murphree eficiency for each tray Emv;
     675* the InletV stream of the bottom tray;
     676* the pump pressure difference;
     677* the heat supllied in the condenser;
     678* the condenser vapor outlet flow (OutletV.F);
     679* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     680       
     681== Initial Conditions ==
     682* the trays temperature (OutletL.T);
     683* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     684* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     685       
     686* the condenser temperature (OutletL.T);
     687* the condenser liquid level (Level);
     688* (NoComps - 1) OutletL (OR OutletV) compositions;
     689";
    690690       
    691691        PARAMETERS
    … …  
    750750        Brief           = "Model of a refluxed stripping column with steady condenser.";
    751751        Info            =
    752         "Specify:
    753          * the feed stream of each tray (Inlet);
    754          * the Murphree eficiency for each tray Emv;
    755          * the InletV stream of the bottom tray;
    756          * the pump head;
    757          * the condenser pressure drop;
    758          * the heat supllied in  the top tank;
    759          * the heat supllied in condenser;
    760          * both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    761        
    762         Initial Conditions:
    763          * the trays temperature (OutletL.T);
    764          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    765          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    766        
    767          * the top tank temperature (OutletL.T);
    768          * the top tank liquid level (Level);
    769          * (NoComps - 1) OutletL (OR OutletV) compositions;
    770         ";
     752"== Specify ==
     753* the feed stream of each tray (Inlet);
     754* the Murphree eficiency for each tray Emv;
     755* the InletV stream of the bottom tray;
     756* the pump head;
     757* the condenser pressure drop;
     758* the heat supllied in  the top tank;
     759* the heat supllied in condenser;
     760* both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     761       
     762== Initial Conditions ==
     763* the trays temperature (OutletL.T);
     764* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     765* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     766       
     767* the top tank temperature (OutletL.T);
     768* the top tank liquid level (Level);
     769* (NoComps - 1) OutletL (OR OutletV) compositions;
     770";
    771771       
    772772        PARAMETERS
    … …  
    830830        Brief           = "Model of a refluxed absorption column with dynamic condenser.";
    831831        Info            =
    832         "Specify:
    833          * the feed stream of each tray (Inlet);
    834          * the Murphree eficiency for each tray Emv;
    835          * the InletV stream of the bottom tray;
    836          * the pump pressure difference;
    837          * the heat supllied in the condenser;
    838          * the condenser vapor outlet flow (OutletV.F);
    839          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    840        
    841         Initial Conditions:
    842          * the trays temperature (OutletL.T);
    843          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    844          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    845        
    846          * the condenser temperature (OutletL.T);
    847          * the condenser liquid level (Level);
    848          * (NoComps - 1) OutletL (OR OutletV) compositions;
    849         ";
     832"== Specify ==
     833* the feed stream of each tray (Inlet);
     834* the Murphree eficiency for each tray Emv;
     835* the InletV stream of the bottom tray;
     836* the pump pressure difference;
     837* the heat supllied in the condenser;
     838* the condenser vapor outlet flow (OutletV.F);
     839* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     840       
     841== Initial Conditions ==
     842* the trays temperature (OutletL.T);
     843* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     844* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     845       
     846* the condenser temperature (OutletL.T);
     847* the condenser liquid level (Level);
     848* (NoComps - 1) OutletL (OR OutletV) compositions;
     849";
    850850       
    851851        PARAMETERS
    … …  
    911911        Brief           = "Model of a refluxed absorption column with steady condenser.";
    912912        Info            =
    913         "Specify:
    914          * the feed stream of each tray (Inlet);
    915          * the Murphree eficiency for each tray Emv;
    916          * the InletV stream of the bottom tray;
    917          * the pump head;
    918          * the condenser pressure drop;
    919          * the heat supllied in  the top tank;
    920          * the heat supllied in condenser;
    921          * both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    922        
    923         Initial Conditions:
    924          * the trays temperature (OutletL.T);
    925          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    926          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    927        
    928          * the top tank temperature (OutletL.T);
    929          * the top tank liquid level (Level);
    930          * (NoComps - 1) OutletL (OR OutletV) compositions;
    931         ";
     913"== Specify ==
     914* the feed stream of each tray (Inlet);
     915* the Murphree eficiency for each tray Emv;
     916* the InletV stream of the bottom tray;
     917* the pump head;
     918* the condenser pressure drop;
     919* the heat supllied in  the top tank;
     920* the heat supllied in condenser;
     921* both  top splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     922       
     923== Initial Conditions ==
     924* the trays temperature (OutletL.T);
     925* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     926* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     927       
     928* the top tank temperature (OutletL.T);
     929* the top tank liquid level (Level);
     930* (NoComps - 1) OutletL (OR OutletV) compositions;
     931";
    932932       
    933933        PARAMETERS
    … …  
    991991        Brief           = "Model of a reboiled stripping column with dynamic reboiler.";
    992992        Info            =
    993         "Specify:
    994          * the feed stream of each tray (Inlet);
    995          * the Murphree eficiency for each tray Emv;
    996          * the InletL stream of the top tray;
    997          * the heat supllied in the reboiler;
    998          * the reboiler liquid outlet flow (OutletL.F);
    999        
    1000         Initial Conditions:
    1001          * the trays temperature (OutletL.T);
    1002          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    1003          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    1004        
    1005          * the reboiler temperature (OutletL.T);
    1006          * the reboiler liquid level (Level);
    1007          * (NoComps - 1) OutletL (OR OutletV) compositions.
    1008         ";
     993"== Specify ==
     994* the feed stream of each tray (Inlet);
     995* the Murphree eficiency for each tray Emv;
     996* the InletL stream of the top tray;
     997* the heat supllied in the reboiler;
     998* the reboiler liquid outlet flow (OutletL.F);
     999       
     1000== Initial Conditions ==
     1001* the trays temperature (OutletL.T);
     1002* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     1003* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     1004       
     1005* the reboiler temperature (OutletL.T);
     1006* the reboiler liquid level (Level);
     1007* (NoComps - 1) OutletL (OR OutletV) compositions.
     1008";
    10091009
    10101010        PARAMETERS
    … …  
    10691069        Brief           = "Model of a reboiled stripping column with steady reboiler.";
    10701070        Info            =
    1071         "Specify:
    1072          * the feed stream of each tray (Inlet);
    1073          * the Murphree eficiency for each tray (Emv);
    1074          * the InletL stream of the top tray;
    1075          * the heat supllied in bottom tank;
    1076          * the heat supllied in the reboiler;
    1077          * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
    1078        
    1079         Initial Conditions:
    1080          * the trays temperature (OutletL.T);
    1081          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    1082          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    1083 
    1084          * the bottom tank temperature (OutletL.T);
    1085          * the bottom tank liquid level (Level);
    1086          * (NoComps - 1) OutletL (OR OutletV) compositions.
    1087         ";
     1071"== Specify ==
     1072* the feed stream of each tray (Inlet);
     1073* the Murphree eficiency for each tray (Emv);
     1074* the InletL stream of the top tray;
     1075* the heat supllied in bottom tank;
     1076* the heat supllied in the reboiler;
     1077* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
     1078       
     1079== Initial Conditions ==
     1080* the trays temperature (OutletL.T);
     1081* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     1082* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     1083
     1084* the bottom tank temperature (OutletL.T);
     1085* the bottom tank liquid level (Level);
     1086* (NoComps - 1) OutletL (OR OutletV) compositions.
     1087";
    10881088       
    10891089        PARAMETERS
    … …  
    11501150        Brief           = "Model of a reboiled absorption column with dynamic reboiler.";
    11511151        Info            =
    1152         "Specify:
    1153          * the feed stream of each tray (Inlet);
    1154          * the Murphree eficiency for each tray Emv;
    1155          * the InletL stream of the top tray;
    1156          * the heat supllied in the reboiler;
    1157          * the reboiler liquid outlet flow (OutletL.F);
    1158        
    1159         Initial Conditions:
    1160          * the trays temperature (OutletL.T);
    1161          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    1162          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    1163        
    1164          * the reboiler temperature (OutletL.T);
    1165          * the reboiler liquid level (Level);
    1166          * (NoComps - 1) OutletL (OR OutletV) compositions.
    1167         ";
     1152"== Specify ==
     1153* the feed stream of each tray (Inlet);
     1154* the Murphree eficiency for each tray Emv;
     1155* the InletL stream of the top tray;
     1156* the heat supllied in the reboiler;
     1157* the reboiler liquid outlet flow (OutletL.F);
     1158       
     1159== Initial Conditions ==
     1160* the trays temperature (OutletL.T);
     1161* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     1162* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     1163       
     1164* the reboiler temperature (OutletL.T);
     1165* the reboiler liquid level (Level);
     1166* (NoComps - 1) OutletL (OR OutletV) compositions.
     1167";
    11681168       
    11691169        PARAMETERS
    … …  
    12281228        Brief           = "Model of a reboiled absorption column with steady reboiler.";
    12291229        Info            =
    1230         "Specify:
    1231          * the feed stream of each tray (Inlet);
    1232          * the Murphree eficiency for each tray (Emv);
    1233          * the InletL stream of the top tray;
    1234          * the heat supllied in bottom tank;
    1235          * the heat supllied in the reboiler;
    1236          * the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
    1237        
    1238         Initial Conditions:
    1239          * the trays temperature (OutletL.T);
    1240          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    1241          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    1242 
    1243          * the bottom tank temperature (OutletL.T);
    1244          * the bottom tank liquid level (Level);
    1245          * (NoComps - 1) OutletL (OR OutletV) compositions.
    1246         ";
     1230"== Specify ==
     1231* the feed stream of each tray (Inlet);
     1232* the Murphree eficiency for each tray (Emv);
     1233* the InletL stream of the top tray;
     1234* the heat supllied in bottom tank;
     1235* the heat supllied in the reboiler;
     1236* the Outlet1 flow in the bottom splitter (spbottom.Outlet1.F) that corresponds to the bottom product;
     1237       
     1238== Initial Conditions ==
     1239* the trays temperature (OutletL.T);
     1240* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     1241* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     1242
     1243* the bottom tank temperature (OutletL.T);
     1244* the bottom tank liquid level (Level);
     1245* (NoComps - 1) OutletL (OR OutletV) compositions.
     1246";
    12471247       
    12481248        PARAMETERS
    … …  
    13051305        Brief           = "Model of a reactive distillation column with dynamic condenser and reboiler.";
    13061306        Info            =
    1307         "Specify:
    1308          * the reaction related variables for each tray, condenser and reboiler;
    1309          * the feed stream of each tray (Inlet);
    1310          * the Murphree eficiency for each tray Emv;
    1311          * the pump pressure difference;
    1312          * the heat supllied in reboiler and condenser;
    1313          * the condenser vapor outlet flow (OutletV.F);
    1314          * the reboiler liquid outlet flow (OutletL.F);
    1315          * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
    1316        
    1317         Initial Conditions:
    1318          * the trays temperature (OutletL.T);
    1319          * the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
    1320          * (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
    1321        
    1322          * the condenser temperature (OutletL.T);
    1323          * the condenser liquid level (Level);
    1324          * (NoComps - 1) OutletL (OR OutletV) compositions;
    1325        
    1326          * the reboiler temperature (OutletL.T);
    1327          * the reboiler liquid level (Level);
    1328          * (NoComps - 1) OutletL (OR OutletV) compositions.
    1329         ";
     1307"== Specify ==
     1308* the reaction related variables for each tray, condenser and reboiler;
     1309* the feed stream of each tray (Inlet);
     1310* the Murphree eficiency for each tray Emv;
     1311* the pump pressure difference;
     1312* the heat supllied in reboiler and condenser;
     1313* the condenser vapor outlet flow (OutletV.F);
     1314* the reboiler liquid outlet flow (OutletL.F);
     1315* both splitter outlet flows OR one of the splitter outlet flows and the splitter frac.
     1316       
     1317== Initial Conditions ==
     1318* the trays temperature (OutletL.T);
     1319* the trays liquid level (Level) OR the trays liquid flow (OutletL.F);
     1320* (NoComps - 1) OutletL (OR OutletV) compositions for each tray;
     1321       
     1322* the condenser temperature (OutletL.T);
     1323* the condenser liquid level (Level);
     1324* (NoComps - 1) OutletL (OR OutletV) compositions;
     1325       
     1326* the reboiler temperature (OutletL.T);
     1327* the reboiler liquid level (Level);
     1328* (NoComps - 1) OutletL (OR OutletV) compositions.
     1329";
    13301330       
    13311331        PARAMETERS

  • trunk/eml/stage_separators/condenser.mso

    r352 r353  
    2626        Brief           = "Model of a dynamic condenser.";
    2727        Info            =
    28         "Assumptions:
    29          * perfect mixing of both phases;
    30          * thermodynamics equilibrium.
    31        
    32         Specify:
    33          * the inlet stream;
    34          * the outlet flows: OutletV.F and OutletL.F;
    35          * the heat supply.
    36        
    37         Initial Conditions:
    38          * the condenser temperature (OutletL.T);
    39          * the condenser liquid level (Level);
    40          * (NoComps - 1) OutletL (OR OutletV) compositions.
    41         ";     
     28"== Assumptions ==
     29* perfect mixing of both phases;
     30* thermodynamics equilibrium.
     31       
     32== Specify ==
     33* the inlet stream;
     34* the outlet flows: OutletV.F and OutletL.F;
     35* the heat supply.
     36       
     37== Initial Conditions ==
     38* the condenser temperature (OutletL.T);
     39* the condenser liquid level (Level);
     40* (NoComps - 1) OutletL (OR OutletV) compositions.
     41";     
    4242       
    4343        PARAMETERS
    … …  
    112112        Brief           = "Model of a  Steady State condenser with no thermodynamics equilibrium.";
    113113        Info            =
    114         "Assumptions:
    115          * perfect mixing of both phases;
    116          * no thermodynamics equilibrium.
    117        
    118         Specify:
    119          * the inlet stream;
    120          * the pressure drop in the condenser;
    121          * the heat supply.
    122         ";
     114"== Assumptions ==
     115* perfect mixing of both phases;
     116* no thermodynamics equilibrium.
     117       
     118== Specify ==
     119* the inlet stream;
     120* the pressure drop in the condenser;
     121* the heat supply.
     122";
    123123       
    124124        PARAMETERS
    … …  
    153153        Brief           = "Model of a Condenser with reaction in liquid phase.";
    154154        Info            =
    155         "Assumptions:
    156          * perfect mixing of both phases;
    157          * thermodynamics equilibrium;
    158          * the reaction only takes place in liquid phase.
    159        
    160         Specify:
    161          * the reaction related variables;
    162          * the inlet stream;
    163          * the outlet flows: OutletV.F and OutletL.F;
    164          * the heat supply.
    165        
    166         Initial Conditions:
    167          * the condenser temperature (OutletL.T);
    168          * the condenser liquid level (Level);
    169          * (NoComps - 1) OutletL (OR OutletV) compositions.
    170         ";
     155"== Assumptions ==
     156* perfect mixing of both phases;
     157* thermodynamics equilibrium;
     158* the reaction only takes place in liquid phase.
     159       
     160== Specify ==
     161* the reaction related variables;
     162* the inlet stream;
     163* the outlet flows: OutletV.F and OutletL.F;
     164* the heat supply.
     165
     166== Initial Conditions ==
     167* the condenser temperature (OutletL.T);
     168* the condenser liquid level (Level);
     169* (NoComps - 1) OutletL (OR OutletV) compositions.
     170";
    171171       
    172172        PARAMETERS

  • trunk/eml/stage_separators/flash.mso

    r352 r353  
    2525        Brief           = "Model of a dynamic flash.";
    2626        Info            =
    27         "Assumptions:
    28          * both phases are perfectly mixed.
    29        
    30         Specify:
    31          * the feed stream;
    32          * the outlet flows: OutletV.F and OutletL.F.
    33 
    34         Initial Conditions:
    35          * the flash initial temperature (OutletL.T);
    36          * the flash initial level (Level);
    37          * (NoComps - 1) OutletL (OR OutletV) compositions.
    38         ";
     27"== Assumptions ==
     28* both phases are perfectly mixed.
     29       
     30== Specify ==
     31* the feed stream;
     32* the outlet flows: OutletV.F and OutletL.F.
     33
     34== Initial Conditions ==
     35* the flash initial temperature (OutletL.T);
     36* the flash initial level (Level);
     37* (NoComps - 1) OutletL (OR OutletV) compositions.
     38";
    3939       
    4040        PARAMETERS
    … …  
    133133        Brief           = "Model of a Steady State flash.";
    134134        Info            =
    135         "Assumptions:
    136          * both phases are perfectly mixed.
    137        
    138         Specify:
    139          * the feed stream;
    140          * the outlet pressure (OutletV.P);
    141          * the outlet temperature OR the heat supplied.
    142         ";
     135"== Assumptions ==
     136* both phases are perfectly mixed.
     137       
     138== Specify ==
     139* the feed stream;
     140* the outlet pressure (OutletV.P);
     141* the outlet temperature OR the heat supplied.
     142";
    143143       
    144144        PARAMETERS
    … …  
    180180        Icon            = "icon/Flash";
    181181        Brief           = "Model of a static PH flash.";
    182         Info            = "
    183         This model is for using the flashPH
    184         routine available on VRTherm.
    185 
    186         Assumptions:
    187          * perfect mixing of both phases;
    188 
    189         Specify:
    190          * the feed stream;
    191          * the heat duty;
    192          * the outlet pressure.
    193         ";     
     182        Info            =
     183"This model is for using the flashPH routine available on VRTherm.
     184
     185== Assumptions ==
     186* perfect mixing of both phases;
     187
     188== Specify ==
     189* the feed stream;
     190* the heat duty;
     191* the outlet pressure.
     192";     
    194193
    195194        PARAMETERS
    … …  
    234233        Icon            = "icon/Flash";
    235234        Brief           = "Another model of a static PH flash.";
    236         Info            = "
    237         This model shows how to model a pressure enthalpy flash
    238         directly with the EMSO modeling language.
    239 
    240         This model is for demonstration purposes only, the flashPH
    241         routine available on VRTherm is much more robust.
    242 
    243         Assumptions:
    244          * perfect mixing of both phases;
    245 
    246         Specify:
    247          * the feed stream;
    248          * the heat duty;
    249          * the outlet pressure.
    250         ";     
     235        Info            =
     236"This model shows how to model a pressure enthalpy flash
     237directly with the EMSO modeling language.
     238
     239This model is for demonstration purposes only, the flashPH
     240routine available on VRTherm is much more robust.
     241
     242== Assumptions ==
     243* perfect mixing of both phases;
     244
     245== Specify ==
     246* the feed stream;
     247* the heat duty;
     248* the outlet pressure.
     249";     
    251250       
    252251        PARAMETERS

  • 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

  • trunk/eml/stage_separators/tank.mso

    r352 r353  
    4242        Brief           = "Model of a cylindrical tank.";
    4343        Info            =
    44         "Specify:
    45          * the Inlet stream;
    46          * the outlet flow;
    47          * the tank Q.
    48 
    49         Initial Conditions:
    50          * the tank initial temperature (OutletL.T);
    51          * the tank initial level (Level);
    52          * (NoComps - 1) OutletL (OR OutletV) compositions.
    53         ";
     44"== Specify ==
     45* the Inlet stream;
     46* the outlet flow;
     47* the tank Q.
     48
     49== Initial Conditions ==
     50* the tank initial temperature (OutletL.T);
     51* the tank initial level (Level);
     52* (NoComps - 1) OutletL (OR OutletV) compositions.
     53";
    5454
    5555        PARAMETERS
    … …  
    101101        Brief           = "Model of a tank with a lain cylinder geometry.";
    102102        Info            =
    103         "Specify:
    104          * the Inlet stream;
    105          * the outlet flow;
    106          * the tank Q.
    107 
    108         Initial Conditions:
    109          * the tank initial temperature (OutletL.T);
    110          * the tank initial level (Level);
    111          * (NoComps - 1) OutletL (OR OutletV) compositions.
    112         ";
     103"== Specify ==
     104* the Inlet stream;
     105* the outlet flow;
     106* the tank Q.
     107
     108== Initial Conditions ==
     109* the tank initial temperature (OutletL.T);
     110* the tank initial level (Level);
     111* (NoComps - 1) OutletL (OR OutletV) compositions.
     112";
    113113       
    114114        PARAMETERS
    … …  
    161161        Brief           = "Model of a simplified tank.";
    162162        Info            =
    163         "Specify:
    164          * the Inlet flow rate;
    165 
    166         Initial Conditions:
    167          * the tank initial level (Level);
    168         ";
     163"== Specify ==
     164* the Inlet flow rate;
     165
     166== Initial Conditions ==
     167* the tank initial level (Level);
     168";
    169169
    170170        PARAMETERS
    … …  
    191191        Brief           = "Model of a tank with feed stream.";
    192192        Info            =
    193         "Specify:
    194          * the Inlet stream;
    195          * the Feed stream;
    196          * the outlet flow;
    197          * the tank Q.
    198 
    199         Initial Conditions:
    200          * the tank initial temperature (OutletL.T);
    201          * the tank initial level (Level);
    202          * (NoComps - 1) OutletL (OR OutletV) compositions.
    203         ";
     193"== Specify ==
     194* the Inlet stream;
     195* the Feed stream;
     196* the outlet flow;
     197* the tank Q.
     198
     199== Initial Conditions ==
     200* the tank initial temperature (OutletL.T);
     201* the tank initial level (Level);
     202* (NoComps - 1) OutletL (OR OutletV) compositions.
     203";
    204204
    205205        PARAMETERS

  • trunk/eml/stage_separators/tray.mso

    r351 r353  
    2626        Brief           = "Basic equations of a tray column model.";
    2727        Info            =
    28         "This model contains only the main equations of a column tray equilibrium model without
    29         the hidraulic equations.
    30        
    31         Assumptions
    32          * both phases (liquid and vapour) exists all the time;
    33          * thermodymanic equilibrium with Murphree plate efficiency;
    34          * no entrainment of liquid or vapour phase;
    35          * no weeping;
    36          * the dymanics in the downcomer are neglected.
    37         ";
     28"This model contains only the main equations of a column tray equilibrium model without
     29the hidraulic equations.
     30       
     31== Assumptions ==
     32* both phases (liquid and vapour) exists all the time;
     33* thermodymanic equilibrium with Murphree plate efficiency;
     34* no entrainment of liquid or vapour phase;
     35* no weeping;
     36* the dymanics in the downcomer are neglected.
     37";
    3838       
    3939        PARAMETERS
    … …  
    111111        Brief           = "Complete model of a column tray.";
    112112        Info            =
    113         "Specify:
    114          * the Feed stream
    115          * the Liquid inlet stream
    116          * the Vapour inlet stream
    117          * the Vapour outlet flow (OutletV.F)
    118        
    119         Initial:
    120          * the plate temperature (OutletL.T)
    121          * the liquid height (Level) OR the liquid flow OutletL.F
    122          * (NoComps - 1) OutletL compositions
    123         ";     
     113"== Specify ==
     114* the Feed stream
     115* the Liquid inlet stream
     116* the Vapour inlet stream
     117* the Vapour outlet flow (OutletV.F)
     118       
     119== Initial ==
     120* the plate temperature (OutletL.T)
     121* the liquid height (Level) OR the liquid flow OutletL.F
     122* (NoComps - 1) OutletL compositions
     123";     
    124124
    125125        PARAMETERS
    … …  
    160160        Brief           = "Model of a tray with reaction.";
    161161        Info            =
    162         "Assumptions
    163          * both phases (liquid and vapour) exists all the time;
    164          * thermodymanic equilibrium with Murphree plate efficiency;
    165          * no entrainment of liquid or vapour phase;
    166          * no weeping;
    167          * the dymanics in the downcomer are neglected.
    168        
    169         Specify:
    170          * the Feed stream;
    171          * the Liquid inlet stream;
    172          * the Vapour inlet stream;
    173          * the Vapour outlet flow (OutletV.F);
    174          * the reaction related variables.
    175        
    176         Initial:
    177          * the plate temperature (OutletL.T)
    178          * the liquid height (Level) OR the liquid flow OutletL.F
    179          * (NoComps - 1) OutletL compositions
    180         ";
     162"== Assumptions ==
     163* both phases (liquid and vapour) exists all the time;
     164* thermodymanic equilibrium with Murphree plate efficiency;
     165* no entrainment of liquid or vapour phase;
     166* no weeping;
     167* the dymanics in the downcomer are neglected.
     168       
     169== Specify ==
     170* the Feed stream;
     171* the Liquid inlet stream;
     172* the Vapour inlet stream;
     173* the Vapour outlet flow (OutletV.F);
     174* the reaction related variables.
     175       
     176== Initial ==
     177* the plate temperature (OutletL.T)
     178* the liquid height (Level) OR the liquid flow OutletL.F
     179* (NoComps - 1) OutletL compositions
     180";
    181181
    182182        PARAMETERS
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