Changeset 262


Ignore:
Timestamp:
Jun 15, 2007, 7:21:14 PM (15 years ago)
Author:
Paula Bettio Staudt
Message:

Updated ATTRIBUTES section

Location:
trunk/eml/stage_separators
Files:
6 edited

Legend:

Unmodified
Added
Removed
  • trunk/eml/stage_separators/batch_dist.mso

    r176 r262  
    1313* available at http://www.enq.ufrgs.br/alsoc.
    1414*
    15 *-------------------------------------------------------------------
    16 * Model of a Batch Distillation (or Differential Distilation)
    17 *--------------------------------------------------------------------
    18 *
    19 *       Streams:
    20 *               * a liquid inlet stream
    21 *               * a vapour outlet stream
    22 *               * a inlet stream
    23 *
    24 *       Assumptions:
    25 *               * perfect mixing of both phases
    26 *               * thermodynamics equilibrium
    27 *               * no liquid entrainment in the vapour stream
    28 *
    29 *       Specify:
    30 *               * the inlet stream
    31 *               * the liquid inlet stream
    32 *               * the molar flow of the vapour outlet stream
    33 *
    34 *       Initial:
    35 *               * the distillator temperature (T)
    36 *               * the distillator liquid level (Ll)
    37 *               * (NoComps - 1) compositions in the distillator
    38 *                                       or in the OutletV
    39 *               
    40 *
    4115*----------------------------------------------------------------------
    4216* Author: Maurício Carvalho Maciel
     
    4620       
    4721Model Diff_Dist
     22        ATTRIBUTES
     23        Pallete         = true;
     24        Icon            = "BatchDist";
     25        Brief           = "Model of a Batch Distillation.";
     26        Info            =
     27        "Assumptions:
     28         * perfect mixing of both phases;
     29         * thermodynamics equilibrium;
     30         * no liquid entrainment in the vapour stream.
    4831       
     32        Specify:
     33         * the inlet stream;
     34         * the liquid inlet stream;
     35         * the molar flow of the vapour outlet stream.
     36       
     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        ";
     42
    4943        PARAMETERS
    5044outer PP                as Plugin       (Brief = "External Physical Properties", Type="PP");
  • trunk/eml/stage_separators/column.mso

    r243 r262  
    4141#*----------------------------------------------------------------------
    4242* Model of a  column section with:
    43 *       - NTrays=number of trays trays.
     43*       - NTrays=number of trays.
    4444*
    4545*---------------------------------------------------------------------*#
    4646Model Section_Column
     47        ATTRIBUTES
     48        Pallete         = true;
     49        Icon            = "SectionColumn";
     50        Brief           = "Model of a column section.";
     51        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        ";
     66       
    4767        PARAMETERS
    4868        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    85105*---------------------------------------------------------------------*#
    86106Model Distillation_kettle_cond
     107        ATTRIBUTES
     108        Pallete         = true;
     109        Icon            = "DistillationKettleCond";
     110        Brief           = "Model of a distillation column with dynamic condenser and dynamic reboiler.";
     111        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        ";
     134       
    87135        PARAMETERS
    88136        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    156204* ------------------------------------------------------------------*#
    157205Model Distillation_thermosyphon_subcooling
     206        ATTRIBUTES
     207        Pallete         = true;
     208        Icon            = "DistillationThermosyphonSubcooling";
     209        Brief           = "Model of a distillation column with steady condenser and steady reboiler.";
     210        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        ";
     234       
    158235        PARAMETERS
    159236        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    232309* ------------------------------------------------------------------*#
    233310Model Distillation_thermosyphon_cond
     311        ATTRIBUTES
     312        Pallete         = true;
     313        Icon            = "DistillationThermosyphonCond";
     314        Brief           = "Model of a distillation column with dynamic condenser and steady reboiler.";
     315        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        ";
     338
    234339        PARAMETERS
    235340        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    304409* ------------------------------------------------------------------*#
    305410Model Distillation_kettle_subcooling
     411        ATTRIBUTES
     412        Pallete         = true;
     413        Icon            = "DistillationKettleSubcooling";
     414        Brief           = "Model of a distillation column with steady condenser and dynamic reboiler.";
     415        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        ";
     439       
    306440        PARAMETERS
    307441        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    371505*---------------------------------------------------------------------*#
    372506Model Rectifier
     507        ATTRIBUTES
     508        Pallete         = true;
     509        Icon            = "RefluxedCond";
     510        Brief           = "Model of a rectifier column with dynamic condenser.";
     511        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        ";
     530
    373531        PARAMETERS
    374532        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    427585* ------------------------------------------------------------------*#
    428586Model Rectifier_subcooling
     587        ATTRIBUTES
     588        Pallete         = true;
     589        Icon            = "RefluxedSubcooling";
     590        Brief           = "Model of a rectifier column with steady condenser.";
     591        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        ";
     611       
    429612        PARAMETERS
    430613        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    482665*---------------------------------------------------------------------*#
    483666Model Refluxed_Stripping
     667        ATTRIBUTES
     668        Pallete         = true;
     669        Icon            = "RefluxedCond";
     670        Brief           = "Model of a refluxed stripping column with dynamic condenser.";
     671        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        ";
     690       
    484691        PARAMETERS
    485692        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    538745* ------------------------------------------------------------------*#
    539746Model Refluxed_Stripping_subcooling
     747        ATTRIBUTES
     748        Pallete         = true;
     749        Icon            = "RefluxedSubcooling";
     750        Brief           = "Model of a refluxed stripping column with steady condenser.";
     751        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        ";
     771       
    540772        PARAMETERS
    541773        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    593825*---------------------------------------------------------------------*#
    594826Model Refluxed_Absorption
     827        ATTRIBUTES
     828        Pallete         = true;
     829        Icon            = "RefluxedCond";
     830        Brief           = "Model of a refluxed absorption column with dynamic condenser.";
     831        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        ";
     850       
    595851        PARAMETERS
    596852        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    650906* ------------------------------------------------------------------*#
    651907Model Refluxed_Absorption_subcooling
     908        ATTRIBUTES
     909        Pallete         = true;
     910        Icon            = "RefluxedSubcooling";
     911        Brief           = "Model of a refluxed absorption column with steady condenser.";
     912        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        ";
     932       
    652933        PARAMETERS
    653934        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    705986* ------------------------------------------------------------------*#
    706987Model Reboiled_Stripping_kettle
     988        ATTRIBUTES
     989        Pallete         = true;
     990        Icon            = "ReboiledKettle";
     991        Brief           = "Model of a reboiled stripping column with dynamic reboiler.";
     992        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        ";
     1009
    7071010        PARAMETERS
    7081011        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    7611064* ------------------------------------------------------------------*#
    7621065Model Reboiled_Stripping_thermosyphon
     1066        ATTRIBUTES
     1067        Pallete         = true;
     1068        Icon            = "ReboiledThermosyphon";
     1069        Brief           = "Model of a reboiled stripping column with steady reboiler.";
     1070        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        ";
     1088       
    7631089        PARAMETERS
    7641090        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    8191145* ------------------------------------------------------------------*#
    8201146Model Reboiled_Absorption_kettle
     1147        ATTRIBUTES
     1148        Pallete         = true;
     1149        Icon            = "ReboiledKettle";
     1150        Brief           = "Model of a reboiled absorption column with dynamic reboiler.";
     1151        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        ";
     1168       
    8211169        PARAMETERS
    8221170        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    8751223* ------------------------------------------------------------------*#
    8761224Model Reboiled_Absorption_thermosyphon
     1225        ATTRIBUTES
     1226        Pallete         = true;
     1227        Icon            = "ReboiledThermosyphon";
     1228        Brief           = "Model of a reboiled absorption column with steady reboiler.";
     1229        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        ";
     1247       
    8771248        PARAMETERS
    8781249        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    9291300* ------------------------------------------------------------------*#
    9301301Model ReactiveDistillation
     1302        ATTRIBUTES
     1303        Pallete         = true;
     1304        Icon            = "DistillationKettleCond";
     1305        Brief           = "Model of a reactive distillation column with dynamic condenser and reboiler.";
     1306        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        ";
     1330       
    9311331        PARAMETERS
    9321332        outer PP as Plugin(Type="PP");
  • trunk/eml/stage_separators/condenser.mso

    r243 r262  
    1212* EMSO is distributed under the therms of the ALSOC LICENSE as
    1313* available at http://www.enq.ufrgs.br/alsoc.
    14 *
    15 *-------------------------------------------------------------------
    16 * Model of a dynamic condenser
    17 *--------------------------------------------------------------------
    18 *
    19 *       Streams:
    20 *               * a vapour inlet stream
    21 *               * a liquid outlet stream
    22 *
    23 *       Assumptions:
    24 *               * perfect mixing of both phases
    25 *               * thermodynamics equilibrium
    26 *
    27 *       Specify:
    28 *               * the Inlet stream
    29 *               * the Outlet flows
    30 *
    31 *       Initial:
    32 *               * the condenser temperature (OutletL.T)
    33 *               * the condenser level (Ll)
    34 *               * (NoComps - 1) Outlet compositions
    3514*
    3615*----------------------------------------------------------------------
     
    4221
    4322Model condenser
     23        ATTRIBUTES
     24        Pallete         = true;
     25        Icon            = "Condenser";
     26        Brief           = "Model of a dynamic condenser.";
     27        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        ";     
     42       
    4443        PARAMETERS
    4544        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    108107*---------------------------------------------------------------------*#
    109108Model condenserSteady
     109        ATTRIBUTES
     110        Pallete         = true;
     111        Icon            = "CondenserSteady";
     112        Brief           = "Model of a  Steady State condenser with no thermodynamics equilibrium.";
     113        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        ";
     123       
    110124        PARAMETERS
    111125        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    134148*--------------------------------------------------------------------*#
    135149Model condenserReact
     150        ATTRIBUTES
     151        Pallete         = true;
     152        Icon            = "Condenser";
     153        Brief           = "Model of a Condenser with reaction in liquid phase.";
     154        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        ";
     171       
    136172        PARAMETERS
    137173        outer PP as Plugin(Type="PP");
  • trunk/eml/stage_separators/flashPH.mso

    r218 r262  
    1414*
    1515*-------------------------------------------------------------------
    16 * Model of a static PH flash
     16*
    1717*--------------------------------------------------------------------
    1818*       - Streams
     
    2525*
    2626*       - Specify:
    27 *               * the feed stream;
    28 *               * the heat duty
    29 *       * the outlet pressure
     27*               *
     28*               *
     29*       *
    3030*
    3131*----------------------------------------------------------------------
     
    3737
    3838Model FlashPHSteady
     39        ATTRIBUTES
     40        Pallete         = true;
     41        Icon            = "Flash";
     42        Brief           = "Model of a static PH flash.";
     43        Info            =
     44        "Assumptions:
     45         * perfect mixing of both phases;
     46
     47        Specify:
     48         * the feed stream;
     49         * the heat duty;
     50         * the outlet pressure.
     51        ";     
     52       
    3953        PARAMETERS
    4054outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
  • trunk/eml/stage_separators/reboiler.mso

    r243 r262  
    1313* available at http://www.enq.ufrgs.br/alsoc.
    1414*
    15 *-------------------------------------------------------------------
    16 * Model of a dynamic reboiler
    17 *--------------------------------------------------------------------
    18 *
    19 *       Streams:
    20 *               * a liquid inlet stream
    21 *               * a liquid outlet stream
    22 *               * a vapour outlet stream
    23 *               * a feed stream
    24 *
    25 *       Assumptions:
    26 *               * perfect mixing of both phases
    27 *               * thermodynamics equilibrium
    28 *               * no liquid entrainment in the vapour stream
    29 *
    30 *       Specify:
    31 *               * the Feed stream
    32 *               * the Liquid inlet stream
    33 *               * the outlet flows: OutletV.F and OutletL.F
    34 *
    35 *       Initial:
    36 *               * the reboiler temperature (OutletL.T)
    37 *               * the reboiler liquid level (Ll)
    38 *               * (NoComps - 1) OutletL (OR OutletV) compositions
    39 *
    40 *
    4115*----------------------------------------------------------------------
    4216* Author: Paula B. Staudt
     
    4721
    4822Model reboiler
     23        ATTRIBUTES
     24        Pallete         = true;
     25        Icon            = "Reboiler";
     26        Brief           = "Model of a dynamic reboiler - kettle.";
     27        Info            =
     28        "Assumptions:
     29         * perfect mixing of both phases;
     30         * thermodynamics equilibrium;
     31         * no liquid entrainment in the vapour stream.
     32       
     33        Specify:
     34         * the inlet stream;
     35         * the liquid inlet stream;
     36         * the outlet flows: OutletV.F and OutletL.F;
     37         * the heat supply.
     38       
     39        Initial Conditions:
     40         * the reboiler temperature (OutletL.T);
     41         * the reboiler liquid level (Level);
     42         * (NoComps - 1) OutletL (OR OutletV) compositions.
     43        ";     
     44       
    4945        PARAMETERS
    5046        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    118114*---------------------------------------------------------------------*#
    119115Model reboilerSteady
     116        ATTRIBUTES
     117        Pallete         = true;
     118        Icon            = "ReboilerSteady";
     119        Brief           = "Model of a  Steady State reboiler with no thermodynamics equilibrium - thermosyphon.";
     120        Info            =
     121        "Assumptions:
     122         * perfect mixing of both phases;
     123         * no thermodynamics equilibrium;
     124         * no liquid entrainment in the vapour stream.
     125       
     126        Specify:
     127         * the InletL stream;
     128         * the heat supply OR the outlet temperature (OutletV.T);
     129        ";     
     130
    120131        PARAMETERS
    121132        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    154165*---------------------------------------------------------------------*#
    155166Model reboilerSteady_fakeH
     167        ATTRIBUTES
     168        Pallete         = true;
     169        Icon            = "ReboilerSteady";
     170        Brief           = "Model of a  Steady State reboiler with fake calculation of outlet conditions.";
     171        Info            =
     172        "Model of a  Steady State reboiler with fake calculation of
     173        vaporisation fraction and output temperature, but with a real
     174        calculation of the output stream enthalpy.
     175        ";
     176       
    156177        PARAMETERS
    157178        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     
    190211*-------------------------------------------------------------------*#
    191212Model reboilerReact
     213        ATTRIBUTES
     214        Pallete         = true;
     215        Icon            = "Reboiler";
     216        Brief           = "Model of a dynamic reboiler with reaction.";
     217        Info            =
     218        "Assumptions:
     219         * perfect mixing of both phases;
     220         * thermodynamics equilibrium;
     221         * no liquid entrainment in the vapour stream;
     222         * the reaction takes place only in the liquid phase.
     223       
     224        Specify:
     225         * the kinetics variables;
     226         * the inlet stream;
     227         * the liquid inlet stream;
     228         * the outlet flows: OutletV.F and OutletL.F;
     229         * the heat supply.
     230       
     231        Initial Conditions:
     232         * the reboiler temperature (OutletL.T);
     233         * the reboiler liquid level (Level);
     234         * (NoComps - 1) OutletL (OR OutletV) compositions.
     235        ";
     236       
    192237        PARAMETERS
    193238        outer PP as Plugin(Type="PP");
  • trunk/eml/stage_separators/tray.mso

    r243 r262  
    5656
    5757        PARAMETERS
    58         outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
    59         outer NComp as Integer;
     58outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
     59outer NComp as Integer;
    6060        V as volume(Brief="Total Volume of the tray");
    6161        Q as heat_rate (Brief="Rate of heat supply");
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