Changeset 352


Ignore:
Timestamp:
Aug 30, 2007, 2:39:11 AM (15 years ago)
Author:
Argimiro Resende Secchi
Message:

Adding more symbol for latex.

Location:
trunk/eml
Files:
16 edited

Legend:

Unmodified
Added
Removed
  • trunk/eml/electrical/electrical.mso

    r325 r352  
    4343
    4444        VARIABLES
    45 in      inlet  as wire (Brief = "Inlet", PosX=0.3831, PosY=0);
    46 out     outlet as wire (Brief = "Outlet", PosX=0.3529, PosY=1);
     45in      inlet  as wire (Brief = "Inlet", PosX=0.3831, PosY=0, Symbol="_{in}");
     46out     outlet as wire (Brief = "Outlet", PosX=0.3529, PosY=1, Symbol="_{out}");
    4747
    4848        EQUATIONS
     
    6262        VARIABLES
    6363        q as charge;
    64 in      inlet  as wire (Brief = "Inlet", PosX=0.3978, PosY=0);
    65 out     outlet as wire (Brief = "Outlet", PosX=0.3965, PosY=1);
     64in      inlet  as wire (Brief = "Inlet", PosX=0.3978, PosY=0, Symbol="_{in}");
     65out     outlet as wire (Brief = "Outlet", PosX=0.3965, PosY=1, Symbol="_{out}");
    6666
    6767        EQUATIONS
     
    8181
    8282        VARIABLES
    83 in      inlet  as wire (Brief = "Inlet", PosX=0.4638, PosY=0);
    84 out     outlet as wire (Brief = "Outlet", PosX=0.4638, PosY=1);
     83in      inlet  as wire (Brief = "Inlet", PosX=0.4638, PosY=0, Symbol="_{in}");
     84out     outlet as wire (Brief = "Outlet", PosX=0.4638, PosY=1, Symbol="_{out}");
    8585
    8686        EQUATIONS
     
    100100
    101101        VARIABLES
    102 in      inlet  as wire (Brief = "Inlet", PosX=0.3923, PosY=0);
    103 out     outlet as wire (Brief = "Outlet", PosX=0.3984, PosY=1);
     102in      inlet  as wire (Brief = "Inlet", PosX=0.3923, PosY=0, Symbol="_{in}");
     103out     outlet as wire (Brief = "Outlet", PosX=0.3984, PosY=1, Symbol="_{out}");
    104104
    105105        EQUATIONS
  • trunk/eml/heat_exchangers/DoublePipe.mso

    r325 r352  
    5757VARIABLES
    5858
    59 in  InletInner          as stream               (Brief="Inlet Inner Stream", PosX=0, PosY=0.5225);     
    60 in  InletOuter          as stream               (Brief="Inlet Outer Stream", PosX=0.2805, PosY=0);
    61 out OutletInner         as streamPH     (Brief="Outlet Inner Stream", PosX=1, PosY=0.5225);
    62 out OutletOuter         as streamPH     (Brief="Outlet Outer Stream", PosX=0.7264, PosY=1);
     59in  InletInner          as stream               (Brief="Inlet Inner Stream", PosX=0, PosY=0.5225, Symbol="_{inInner}");
     60in  InletOuter          as stream               (Brief="Inlet Outer Stream", PosX=0.2805, PosY=0, Symbol="_{inOuter}");
     61out OutletInner         as streamPH     (Brief="Outlet Inner Stream", PosX=1, PosY=0.5225, Symbol="_{outInner}");
     62out OutletOuter         as streamPH     (Brief="Outlet Outer Stream", PosX=0.7264, PosY=1, Symbol="_{outOuter}");
    6363
    6464        Details         as Details_Main         (Brief="Some Details in the Heat Exchanger");
  • trunk/eml/heat_exchangers/HeatExchangerDetailed.mso

    r325 r352  
    3333VARIABLES
    3434
    35 in  InletTube   as stream               (Brief="Inlet Tube Stream", PosX=0, PosY=0.4915);
    36 out OutletTube  as streamPH     (Brief="Outlet Tube Stream", PosX=1, PosY=0.4915);
    37 in  InletShell  as stream               (Brief="Inlet Shell Stream", PosX=0.5237, PosY=1);
    38 out OutletShell as streamPH     (Brief="Outlet Shell Stream", PosX=0.5237, PosY=0);
     35in  InletTube   as stream               (Brief="Inlet Tube Stream", PosX=0, PosY=0.4915, Symbol="_{inTube}");
     36out OutletTube  as streamPH     (Brief="Outlet Tube Stream", PosX=1, PosY=0.4915, Symbol="_{outTube}");
     37in  InletShell  as stream               (Brief="Inlet Shell Stream", PosX=0.5237, PosY=1, Symbol="_{inShell}");
     38out OutletShell as streamPH     (Brief="Outlet Shell Stream", PosX=0.5237, PosY=0, Symbol="_{outShell}");
    3939       
    4040        Details         as Details_Main         (Brief="Details in Heat Exchanger");
  • trunk/eml/heat_exchangers/HeatExchangerSimplified.mso

    r325 r352  
    3636VARIABLES
    3737
    38 in  InletHot    as stream               (Brief="Inlet Hot Stream", PosX=0, PosY=0.4915);
    39 out OutletHot   as streamPH     (Brief="Outlet Hot Stream", PosX=1, PosY=0.4915);
    40 in  InletCold   as stream               (Brief="Inlet Cold Stream", PosX=0.5237, PosY=1);
    41 out OutletCold  as streamPH     (Brief="Outlet Cold Stream", PosX=0.5237, PosY=0);
     38in  InletHot    as stream               (Brief="Inlet Hot Stream", PosX=0, PosY=0.4915, Symbol="_{inHot}");
     39out OutletHot   as streamPH     (Brief="Outlet Hot Stream", PosX=1, PosY=0.4915, Symbol="_{outHot}");
     40in  InletCold   as stream               (Brief="Inlet Cold Stream", PosX=0.5237, PosY=1, Symbol="_{inCold}");
     41out OutletCold  as streamPH     (Brief="Outlet Cold Stream", PosX=0.5237, PosY=0, Symbol="_{outCold}");
    4242
    4343        xh(NComp)       as fraction             (Brief = "Liquid Molar Fraction in Hot Side");
  • trunk/eml/heat_exchangers/Mheatex.mso

    r325 r352  
    3838VARIABLES
    3939
    40 in  InletHot(Nhot)      as stream       (Brief="Inlet Hot Streams", PosX=0, PosY=0.7156);       
    41 out OutletHot(Nhot)     as streamPH (Brief="Outlet Hot Streams", PosX=1, PosY=0.7156);
    42 in  InletCold(Ncold)    as stream       (Brief="Inlet Cold Streams", PosX=1, PosY=0.2793);
    43 out OutletCold(Ncold)   as streamPH     (Brief="Outlet Cold Streams", PosX=0, PosY=0.2793);
     40in  InletHot(Nhot)      as stream       (Brief="Inlet Hot Streams", PosX=0, PosY=0.7156, Symbol="_{inHot}");   
     41out OutletHot(Nhot)     as streamPH (Brief="Outlet Hot Streams", PosX=1, PosY=0.7156, Symbol="_{outHot}");
     42in  InletCold(Ncold)    as stream       (Brief="Inlet Cold Streams", PosX=1, PosY=0.2793, Symbol="_{inCold}");
     43out OutletCold(Ncold)   as streamPH     (Brief="Outlet Cold Streams", PosX=0, PosY=0.2793, Symbol="_{outCold}");
    4444
    4545        Method  as LMTD_Basic   (Brief="Log Mean Temperature Difference Method");
  • trunk/eml/heat_exchangers/PHE.mso

    r325 r352  
    8383 VARIABLES
    8484
    85 in  InletHot        as stream           (Brief="Inlet Hot Stream", PosX=0, PosY=0.7156);       
    86 in  InletCold       as stream           (Brief="Inlet Cold Stream", PosX=1, PosY=0.7156);
    87 out OutletHot           as streamPH     (Brief="Outlet Hot Stream", PosX=0, PosY=0.2793);
    88 out OutletCold          as streamPH     (Brief="Outlet Cold Stream", PosX=1, PosY=0.2793);
     85in  InletHot        as stream           (Brief="Inlet Hot Stream", PosX=0, PosY=0.7156, Symbol="_{inHot}");     
     86in  InletCold       as stream           (Brief="Inlet Cold Stream", PosX=1, PosY=0.7156, Symbol="_{inCold}");
     87out OutletHot           as streamPH     (Brief="Outlet Hot Stream", PosX=0, PosY=0.2793, Symbol="_{outHot}");
     88out OutletCold          as streamPH     (Brief="Outlet Cold Stream", PosX=1, PosY=0.2793, Symbol="_{outCold}");
    8989
    9090        HotSide                 as Main_PHE             (Brief="Plate Heat Exchanger Hot Side");
  • trunk/eml/heat_exchangers/heater.mso

    r326 r352  
    3838        Lfrac                   as fraction             (Brief = "Liquid fraction Outlet Stream");
    3939        Kvalue(NComp)   as Real                         (Brief = "Phase Equilibrium K-values");
    40 in  Inlet(Ninlet )  as stream                   (Brief="Inlet Streams", PosX=0, PosY=0.4833);
    41 out Outlet              as streamPH                     (Brief="Outlet Stream", PosX=1, PosY=0.4782);
     40in  Inlet(Ninlet )  as stream                   (Brief="Inlet Streams", PosX=0, PosY=0.4833, Symbol="_{in}");
     41out Outlet              as streamPH                     (Brief="Outlet Stream", PosX=1, PosY=0.4782, Symbol="_{out}");
    4242       
    4343 EQUATIONS
     
    8585
    8686 VARIABLES
    87 in  InletQ              as energy_stream        (Brief ="Inlet Heat Stream", PosX=0.1662, PosY=1);
     87in  InletQ              as energy_stream        (Brief ="Inlet Heat Stream", PosX=0.1662, PosY=1, Symbol="_{out}");
    8888
    8989 EQUATIONS
     
    102102
    103103 VARIABLES
    104 in  InletQ              as energy_stream        (Brief ="Inlet Heat Stream", PosX=0.8245, PosY=1);
     104in  InletQ              as energy_stream        (Brief ="Inlet Heat Stream", PosX=0.8245, PosY=1, Symbol="_{out}");
    105105
    106106 EQUATIONS
  • trunk/eml/reactors/batch.mso

    r325 r352  
    3838VARIABLES
    3939
    40 in      Inlet      as stream (Brief="Inlet stream", PosX=0, PosY=0);
     40in      Inlet      as stream (Brief="Inlet stream", PosX=0, PosY=0, Symbol="_{in}");
    4141        C(NComp) as conc_mol (Brief="Components concentration");
    4242        r(NReac) as reaction_mol (Brief = "Reaction rates");
  • trunk/eml/reactors/cstr.mso

    r325 r352  
    3737VARIABLES
    3838
    39 in      Inlet   as stream       (Brief="Inlet Stream", PosX=0, PosY=0);
    40 out     Outlet  as streamPH     (Brief="Outlet Stream", PosX=1, PosY=1);
     39in      Inlet   as stream       (Brief="Inlet Stream", PosX=0, PosY=0, Symbol="_{in}");
     40out     Outlet  as streamPH     (Brief="Outlet Stream", PosX=1, PosY=1, Symbol="_{out}");
    4141
    4242        q                       as heat_rate    (Brief="Heat");
  • trunk/eml/reactors/pfr.mso

    r325 r352  
    5050VARIABLES
    5151
    52 in      Inlet   as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5076);
    53 out     Outlet  as stream       (Brief = "Outlet Stream", PosX=1, PosY=0.5236);
     52in      Inlet   as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5076, Symbol="_{in}");
     53out     Outlet  as stream       (Brief = "Outlet Stream", PosX=1, PosY=0.5236, Symbol="_{out}");
    5454
    5555        str(NDisc+1) as streamPH;
  • trunk/eml/stage_separators/batch_dist.mso

    r325 r352  
    4848       
    4949        VARIABLES
    50 in      Inlet   as stream (Brief="Feed stream", PosX=0, PosY=0.9385);
    51 in      InletL  as stream (Brief="Liquid inlet stream", PosX=0.5, PosY=0.1984); # FIXME
    52 out     OutletV as vapour_stream (Brief="Vapour outlet stream", PosX=1, PosY=0.1984);
    53 in      InletQ  as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.9578);
     50in      Inlet   as stream (Brief="Feed stream", PosX=0, PosY=0.9385, Symbol="_{in}");
     51in      InletL  as stream (Brief="Liquid inlet stream", PosX=0.5, PosY=0.1984, Symbol="_{inL}"); # FIXME
     52out     OutletV as vapour_stream (Brief="Vapour outlet stream", PosX=1, PosY=0.1984, Symbol="_{outV}");
     53in      InletQ  as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.9578, Symbol="_{in}");
    5454
    5555        M(NComp)        as mol                  (Brief="Molar Holdup in the distillator");
  • trunk/eml/stage_separators/condenser.mso

    r325 r352  
    4848
    4949        VARIABLES
    50 in      InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0);
    51 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1);
    52 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0);
    53 in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311);
     50in      InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0, Symbol="_{inV}");
     51out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1, Symbol="_{outL}");
     52out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0, Symbol="_{outV}");
     53in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311, Symbol="_{in}");
    5454
    5555        M(NComp) as mol (Brief="Molar Holdup in the tray");
     
    127127
    128128        VARIABLES
    129 in      InletV as stream(Brief="Vapour inlet stream", PosX=0.3431, PosY=0);
    130 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.34375, PosY=1);
    131 in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.5974);
     129in      InletV as stream(Brief="Vapour inlet stream", PosX=0.3431, PosY=0, Symbol="_{inV}");
     130out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.34375, PosY=1, Symbol="_{outL}");
     131in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.5974, Symbol="_{in}");
    132132        DP as press_delta (Brief="Pressure Drop in the condenser");
    133133
     
    181181
    182182        VARIABLES
    183 in      InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0);
    184 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1);
    185 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0);
    186 in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311);
     183in      InletV as stream(Brief="Vapour inlet stream", PosX=0.1164, PosY=0, Symbol="_{inV}");
     184out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4513, PosY=1, Symbol="_{outL}");
     185out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4723, PosY=0, Symbol="_{outV}");
     186in      InletQ as energy_stream (Brief="Cold supplied", PosX=1, PosY=0.6311, Symbol="_{in}");
    187187
    188188        M(NComp) as mol (Brief="Molar Holdup in the tray");
  • trunk/eml/stage_separators/flash.mso

    r334 r352  
    5050
    5151        VARIABLES
    52 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
    53 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
    54 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
    55 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
     52in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}");
     53out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}");
     54out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}");
     55in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}");
    5656
    5757        M(NComp) as mol (Brief="Molar Holdup in the tray");
     
    6363        Level as length (Brief="liquid height");
    6464        Across as area (Brief="Flash Cross section area");
    65         vfrac as positive (Brief="Vapourization fraction");
     65        vfrac as positive (Brief="Vapourization fraction", Symbol="\phi");
    6666
    6767        EQUATIONS
     
    146146       
    147147        VARIABLES
    148 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
    149 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
    150 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
    151 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
    152         vfrac as fraction (Brief="Vapourization fraction");
     148in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}");
     149out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}");
     150out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}");
     151in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}");
     152        vfrac as fraction (Brief="Vapourization fraction", Symbol="\phi");
    153153
    154154        EQUATIONS
     
    198198
    199199        VARIABLES
    200 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
    201 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
    202 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
    203 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
    204         vfrac as fraction(Brief="Vaporization fraction");
     200in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}");
     201out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}");
     202out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}");
     203in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}");
     204        vfrac as fraction(Brief="Vaporization fraction", Symbol="\phi");
    205205        h as enth_mol(Brief="Mixture enthalpy");
    206206
     
    256256
    257257        VARIABLES
    258 in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421);
    259 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1);
    260 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0);
    261 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559);
    262         vfrac as fraction(Brief="Vaporization fraction");
    263         vsat as Real(Lower=-0.1, Upper=1.1, Brief="Vaporization fraction if saturated");
     258in      Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}");
     259out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}");
     260out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}");
     261in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}");
     262        vfrac as fraction(Brief="Vaporization fraction", Symbol="\phi");
     263        vsat as Real(Lower=-0.1, Upper=1.1, Brief="Vaporization fraction if saturated", Symbol="\phi_{sat}");
    264264        Tsat as temperature(Lower=173, Upper=1473, Brief="Temperature if saturated");
    265265        xsat(NComp) as Real(Lower=0, Upper=1, Brief="Liquid composition if saturated");
  • trunk/eml/stage_separators/reboiler.mso

    r325 r352  
    5656
    5757        VARIABLES
    58 in      Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0);
    59 in      InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254);
    60 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1);
    61 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0);
    62 in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123);
     58in      Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0, Symbol="_{in}");
     59in      InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254, Symbol="_{inL}");
     60out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1, Symbol="_{outL}");
     61out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0, Symbol="_{outV}");
     62in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123, Symbol="_{in}");
    6363
    6464        M(NComp) as mol (Brief="Molar Holdup in the tray");
     
    141141
    142142        VARIABLES
    143 in      InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1);
    144 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0);
    145 in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111);
     143in      InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1, Symbol="_{inL}");
     144out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0, Symbol="_{outV}");
     145in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111, Symbol="_{in}");
    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", PosX=0.3345, PosY=1);
    191 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0);
    192 in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111);
     190in      InletL as stream(Brief="Liquid inlet stream", PosX=0.3345, PosY=1, Symbol="_{inL}");
     191out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.3369, PosY=0, Symbol="_{outV}");
     192in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6111, Symbol="_{in}");
    193193
    194194        EQUATIONS
     
    252252
    253253        VARIABLES
    254 in      Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0);
    255 in      InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254);
    256 out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1);
    257 out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0);
    258 in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123);
     254in      Inlet as stream(Brief="Feed Stream", PosX=0.8127, PosY=0, Symbol="_{in}");
     255in      InletL as stream(Brief="Liquid inlet stream", PosX=0, PosY=0.5254, Symbol="_{inL}");
     256out     OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.2413, PosY=1, Symbol="_{outL}");
     257out     OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.5079, PosY=0, Symbol="_{outV}");
     258in      InletQ as energy_stream (Brief="Heat supplied", PosX=1, PosY=0.6123, Symbol="_{in}");
    259259
    260260        M(NComp) as mol (Brief="Molar Holdup in the tray");
  • trunk/eml/stage_separators/tank.mso

    r325 r352  
    5959       
    6060        VARIABLES
    61 in      Inlet  as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0);
    62 out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1);
    63 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859);
     61in      Inlet  as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0, Symbol="_{in}");
     62out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1, Symbol="_{out}");
     63in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859, Symbol="_{in}");
    6464        Level    as length(Brief="Tank level");
    6565        M(NComp) as mol (Brief="Molar Holdup in the tank");
     
    119119       
    120120        VARIABLES
    121 in      Inlet  as stream (Brief = "Inlet stream", PosX=0.1825, PosY=0);
    122 out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1);
    123 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.6160);
     121in      Inlet  as stream (Brief = "Inlet stream", PosX=0.1825, PosY=0, Symbol="_{in}");
     122out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1, Symbol="_{out}");
     123in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.6160, Symbol="_{in}");
    124124        Level    as length(Brief="Tank level");
    125125        Across as area (Brief="Tank cross section area", Default=2);
     
    209209       
    210210        VARIABLES
    211 in      Feed as stream (Brief = "Feed stream", PosX=0.32, PosY=0);     
    212 in      Inlet  as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0);
    213 out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1);
    214 in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859);
     211in      Feed as stream (Brief = "Feed stream", PosX=0.32, PosY=0, Symbol="_{feed}");   
     212in      Inlet  as stream (Brief = "Inlet stream", PosX=0.3037, PosY=0, Symbol="_{in}");
     213out     Outlet as liquid_stream (Brief = "Outlet liquid stream", PosX=1, PosY=1, Symbol="_{out}");
     214in      InletQ as energy_stream (Brief="Rate of heat supply", PosX=1, PosY=0.7859, Symbol="_{in}");
    215215
    216216        Level    as length(Brief="Tank level");
  • trunk/eml/streams.mso

    r346 r352  
    156156
    157157        VARIABLES
    158         out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256);
     158        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}");
    159159        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction");
    160160        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction");
     
    246246       
    247247        VARIABLES
    248         out Outlet                      as stream               (Brief = "Outlet stream", PosX=1, PosY=0.5256);
     248        out Outlet                      as stream               (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}");
    249249        x(NComp)                        as fraction             (Brief = "Liquid Molar Fraction");
    250250        y(NComp)                        as fraction             (Brief = "Vapour Molar Fraction");
     
    308308       
    309309        VARIABLES
    310         in Inlet                as stream               (Brief = "Inlet Stream", PosX=0, PosY=0.5308);
     310        in Inlet                as stream               (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Symbol="_{in}");
    311311        v                               as fraction             (Brief = "Vapourization fraction");
    312312        x(NComp)                as fraction             (Brief = "Liquid Molar Fraction");
     
    369369       
    370370        VARIABLES
    371         in Inlet                as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5308);
     371        in Inlet                as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Symbol="_{in}");
    372372end
    373373
     
    392392
    393393        VARIABLES
    394         out OutletQ             as energy_stream (Brief = "Outlet energy stream", PosX=1, PosY=0.5349);
    395 end
     394        out OutletQ             as energy_stream (Brief = "Outlet energy stream", PosX=1, PosY=0.5349, Symbol="_{out}");
     395end
Note: See TracChangeset for help on using the changeset viewer.