Ignore:
Timestamp:
Jul 28, 2007, 9:41:04 PM (15 years ago)
Author:
Argimiro Resende Secchi
Message:

Set icons positions for most devices.

Location:
trunk/eml/stage_separators
Files:
6 edited

Legend:

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

    r318 r325  
    4848       
    4949        VARIABLES
    50 in      Inlet   as stream (Brief="Feed stream");
    51 in      InletL  as stream (Brief="Liquid inlet stream");
    52 out     OutletV as vapour_stream (Brief="Vapour outlet stream");
    53 in      InletQ  as energy_stream (Brief="Heat supplied");
     50in      Inlet   as stream (Brief="Feed stream", PosX=0, PosY=0.9385);
     51in      InletL  as stream (Brief="Liquid inlet stream", PosX=0.5, PosY=0.1984); # FIXME
     52out     OutletV as vapour_stream (Brief="Vapour outlet stream", PosX=1, PosY=0.1984);
     53in      InletQ  as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.9578);
    5454
    5555        M(NComp)        as mol                  (Brief="Molar Holdup in the distillator");
  • trunk/eml/stage_separators/condenser.mso

    r310 r325  
    4848
    4949        VARIABLES
    50 in      InletV as stream(Brief="Vapour inlet stream");
    51 out     OutletL as liquid_stream(Brief="Liquid outlet stream");
    52 out     OutletV as vapour_stream(Brief="Vapour outlet stream");
    53 in      InletQ as energy_stream (Brief="Heat supplied");
     50in      InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0);
     51out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1);
     52out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0);
     53in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311);
    5454
    5555        M(NComp) as mol (Brief="Molar Holdup in the tray");
     
    127127
    128128        VARIABLES
    129 in      InletV as stream(Brief="Vapour inlet stream");
    130 out     OutletL as liquid_stream(Brief="Liquid outlet stream");
    131 in      InletQ as energy_stream (Brief="Heat supplied");
     129in      InletV as stream(Brief="Vapour inlet stream", PosX=0.3431, PosY=0);
     130out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.34375, PosY=1);
     131in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.5974);
    132132        DP as press_delta (Brief="Pressure Drop in the condenser");
    133133
     
    181181
    182182        VARIABLES
    183 in      InletV as stream(Brief="Vapour inlet stream");
    184 out     OutletL as liquid_stream(Brief="Liquid outlet stream");
    185 out     OutletV as vapour_stream(Brief="Vapour outlet stream");
    186 in      InletQ as energy_stream (Brief="Heat supplied");
     183in      InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0);
     184out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1);
     185out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0);
     186in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311);
    187187
    188188        M(NComp) as mol (Brief="Molar Holdup in the tray");
  • trunk/eml/stage_separators/flash.mso

    r323 r325  
    5050
    5151        VARIABLES
    52 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5);
    53 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.5, PosY=0.5);
    54 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5, PosY=0);
    55 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.75);
     52in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
     53out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
     54out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
     55in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
    5656
    5757        M(NComp) as mol (Brief="Molar Holdup in the tray");
     
    140140       
    141141        VARIABLES
    142 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5);
    143 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.5, PosY=0.5);
    144 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5, PosY=0);
    145 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.75);
     142in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
     143out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
     144out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
     145in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
    146146        vfrac as fraction;
    147147
     
    191191
    192192        VARIABLES
    193 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5);
    194 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.5, PosY=0.5);
    195 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5, PosY=0);
    196 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.75);
     193in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
     194out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
     195out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
     196in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
    197197        vfrac as fraction(Brief="Real vaporization fraction");
    198198        h as enth_mol(Brief="Mixture enthalpy");
     
    249249
    250250        VARIABLES
    251 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5);
    252 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.5, PosY=0.5);
    253 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5, PosY=0);
    254 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.75);
     251in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
     252out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
     253out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
     254in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
    255255        vfrac as fraction(Brief="Real vaporization fraction");
    256256        vsat as Real(Lower=-0.1, Upper=1.1, Brief="Vaporization fraction if saturated");
  • trunk/eml/stage_separators/reboiler.mso

    r310 r325  
    5656
    5757        VARIABLES
    58 in      Inlet as stream(Brief="Feed Stream");
    59 in      InletL as stream(Brief="Liquid inlet stream");
    60 out     OutletL as liquid_stream(Brief="Liquid outlet stream");
    61 out     OutletV as vapour_stream(Brief="Vapour outlet stream");
    62 in      InletQ as energy_stream (Brief="Heat supplied");
     58in      Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0);
     59in      InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254);
     60out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1);
     61out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0);
     62in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123);
    6363
    6464        M(NComp) as mol (Brief="Molar Holdup in the tray");
     
    141141
    142142        VARIABLES
    143 in      InletL as stream(Brief="Liquid inlet stream");
    144 out     OutletV as vapour_stream(Brief="Vapour outlet stream");
    145 in      InletQ as energy_stream (Brief="Heat supplied");
     143in      InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1);
     144out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0);
     145in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111);
    146146        vV as volume_mol (Brief="Vapour Molar volume");
    147147        rhoV as dens_mass (Brief="Vapour Density");
     
    188188       
    189189        VARIABLES
    190 in      InletL as stream(Brief="Liquid inlet stream");
    191 out     OutletV as stream(Brief="Vapour outlet stream");
    192 in      InletQ as energy_stream (Brief="Heat supplied");
     190in      InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1);
     191out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0);
     192in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111);
    193193
    194194        EQUATIONS
     
    252252
    253253        VARIABLES
    254 in      Inlet as stream(Brief="Feed Stream");
    255 in      InletL as stream(Brief="Liquid inlet stream");
    256 out     OutletL as liquid_stream(Brief="Liquid outlet stream");
    257 out     OutletV as vapour_stream(Brief="Vapour outlet stream");
    258 
    259 in      InletQ as energy_stream (Brief="Heat supplied");
     254in      Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0);
     255in      InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254);
     256out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1);
     257out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0);
     258in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123);
     259
    260260        M(NComp) as mol (Brief="Molar Holdup in the tray");
    261261        ML as mol (Brief="Molar liquid holdup");
  • trunk/eml/stage_separators/tank.mso

    r313 r325  
    5959       
    6060        VARIABLES
    61 in      Inlet as stream;
    62 out     Outlet as liquid_stream;
    63 
    64 in      InletQ as energy_stream (Brief="Rate of heat supply");
     61in      Inlet  as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0);
     62out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1);
     63in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859);
    6564        Level    as length(Brief="Tank level");
    6665        M(NComp) as mol (Brief="Molar Holdup in the tank");
     
    120119       
    121120        VARIABLES
    122 in      Inlet as stream;
    123 out     Outlet as liquid_stream;
    124 
    125 in      InletQ as energy_stream (Brief="Rate of heat supply");
     121in      Inlet  as stream (Brief = "Inlet stream", PosX=0.1825, PosY=0);
     122out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1);
     123in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.6160);
    126124        Level    as length(Brief="Tank level");
    127125        Across as area (Brief="Tank cross section area", Default=2);
     
    176174        VARIABLES
    177175        Level as length(Brief="Tank level");
    178 in      Fin  as flow_vol(Brief="Input flow");
    179 out     Fout as flow_vol(Brief="Output flow");
     176in      Fin  as flow_vol(Brief="Input flow", PosX=0.3037, PosY=0);
     177out     Fout as flow_vol(Brief="Output flow", PosX=1, PosY=1);
    180178
    181179        EQUATIONS
     
    211209       
    212210        VARIABLES
    213 in      Feed as stream;
    214 in      Inlet as stream;
    215 out     Outlet as liquid_stream;
    216 
    217 in      InletQ as energy_stream (Brief="Rate of heat supply");
     211in      Feed as stream (Brief = "Feed stream", PosX=0.32, PosY=0);     
     212in      Inlet  as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0);
     213out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1);
     214in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859);
     215
    218216        Level    as length(Brief="Tank level");
    219217        M(NComp) as mol (Brief="Molar Holdup in the tank");
  • trunk/eml/stage_separators/tray.mso

    r300 r325  
    4545       
    4646        VARIABLES
    47 in      Inlet as stream;
    48 in      InletL as stream;
    49 in      InletV as stream;
    50 out     OutletL as liquid_stream;
    51 out     OutletV as vapour_stream;
     47in      Inlet as stream (Brief="Feed stream", PosX=0, PosY=0.4932);
     48in      InletL as stream (Brief="Inlet liquid stream", PosX=0.5195, PosY=0);
     49in      InletV as stream (Brief="Inlet vapour stream", PosX=0.4994, PosY=1);
     50out     OutletL as liquid_stream (Brief="Outlet liquid stream", PosX=0.8277, PosY=1);
     51out     OutletV as vapour_stream (Brief="Outlet vapour stream", PosX=0.8043, PosY=0);
    5252
    5353        M(NComp) as mol (Brief="Molar Holdup in the tray");
     
    202202       
    203203        VARIABLES
    204 in      Inlet as stream;
    205 in      InletL as stream;
    206 in      InletV as stream;
    207 out     OutletL as liquid_stream;
    208 out     OutletV as vapour_stream;
     204in      Inlet as stream (Brief="Feed stream", PosX=0, PosY=0.4932);
     205in      InletL as stream (Brief="Inlet liquid stream", PosX=0.5195, PosY=0);
     206in      InletV as stream (Brief="Inlet vapour stream", PosX=0.4994, PosY=1);
     207out     OutletL as liquid_stream (Brief="Outlet liquid stream", PosX=0.8277, PosY=1);
     208out     OutletV as vapour_stream (Brief="Outlet vapour stream", PosX=0.8043, PosY=0);
    209209
    210210        yideal(NComp) as fraction;
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