Changeset 355 for trunk/eml


Ignore:
Timestamp:
Aug 30, 2007, 7:17:39 PM (15 years ago)
Author:
gerson bicca
Message:

Adding symbol for latex.

Location:
trunk/eml/heat_exchangers
Files:
2 edited

Legend:

Unmodified
Added
Removed
  • trunk/eml/heat_exchangers/HEX_Engine.mso

    r346 r355  
    3131T                       as temperature          (Brief="Average  Temperature",Lower=50);
    3232P                       as pressure                     (Brief="Average  Pressure",Default=1, Lower=1e-10, Upper=2e4, DisplayUnit='kPa');
    33 rho             as dens_mass            (Brief="Stream Density" ,Default=1000, Lower=1e-3, Upper=5e5);
    34 Mu              as viscosity            (Brief="Stream Viscosity",Lower=0.0001);
     33rho             as dens_mass            (Brief="Stream Density" ,Default=1000, Lower=1e-3, Upper=5e5, Symbol = "\rho");
     34Mu              as viscosity            (Brief="Stream Viscosity",Lower=0.0001, Symbol = "\mu");
    3535Cp              as cp_mol                       (Brief="Stream Molar Heat Capacity", Upper=1e10);
    3636K                       as conductivity         (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500);
     
    4848VARIABLES
    4949Fw              as flow_mass            (Brief="Stream Mass Flow");
    50 rho             as dens_mass            (Brief="Stream Density" ,Default=1000, Lower=1e-3, Upper=5e5);
    51 Mu              as viscosity            (Brief="Stream Viscosity",Default=1, Lower=1e-5, Upper=1e5);
     50rho             as dens_mass            (Brief="Stream Density" ,Default=1000, Lower=1e-3, Upper=5e5, Symbol = "\rho");
     51Mu              as viscosity            (Brief="Stream Viscosity",Default=1, Lower=1e-5, Upper=1e5, Symbol = "\mu");
    5252Cp                      as cp_mol                       (Brief="Stream Molar Heat Capacity", Upper=1e10);
    5353K                       as conductivity         (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500);
     
    6565VARIABLES
    6666
    67 Mu              as viscosity            (Brief="Stream Viscosity",Default=1, Lower=1e-5, Upper=1e5);
     67Mu              as viscosity            (Brief="Stream Viscosity",Default=1, Lower=1e-5, Upper=1e5, Symbol = "\mu");
    6868Twall           as temperature  (Brief="Wall Temperature",Lower=50);
    6969
     
    8080VARIABLES
    8181
    82 Inlet                   as Properties_In_Out            (Brief="Properties at Inlet Stream");
    83 Average         as Properties_Average   (Brief="Properties at Average Temperature");
    84 Outlet          as Properties_In_Out            (Brief="Properties at Outlet Stream");
    85 Wall                    as Properties_Wall                      (Brief="Properties at Wall Temperature");
     82Inlet                   as Properties_In_Out            (Brief="Properties at Inlet Stream", Symbol = "^{in}");
     83Average         as Properties_Average   (Brief="Properties at Average Temperature", Symbol = "^{avg}");
     84Outlet          as Properties_In_Out            (Brief="Properties at Outlet Stream", Symbol = "^{out}");
     85Wall                    as Properties_Wall                      (Brief="Properties at Wall Temperature", Symbol = "^{wall}");
    8686
    8787end
     
    445445HeatTransfer            as PHE_HeatTransfer             (Brief="PHE Heat Transfer");
    446446PressureDrop    as PHE_PressureDrop             (Brief="PHE Pressure Drop");
    447 Properties              as Physical_Properties          (Brief="PHE Properties");
     447Properties              as Physical_Properties          (Brief="PHE Properties", Symbol = " ");
    448448
    449449end
     
    462462Cmax    as positive                                     (Brief="Maximum Heat Capacity",Lower=1e-10,Default=1e3,Unit='W/K');
    463463NTU     as positive                                     (Brief="Number of Units Transference",Default=0.05,Lower=1e-10);
    464 Eft             as positive                             (Brief="Effectiveness",Default=0.5,Lower=1e-8,Upper=1);
     464Eft             as positive                             (Brief="Effectiveness",Default=0.5,Lower=1e-8,Upper=1, Symbol = "\epsilon");
    465465Q                       as power                                        (Brief="Heat Transfer", Default=7000, Lower=1e-6, Upper=1e10);
    466466Uc              as heat_trans_coeff     (Brief="Overall Heat Transfer Coefficient Clean",Default=1,Lower=1e-6,Upper=1e10);
  • trunk/eml/heat_exchangers/PHE.mso

    r354 r355  
    3636
    3737== References ==
    38    
     38
    3939[1] E.A.D. Saunders, Heat Exchangers: Selection, Design and
    40 Construction, Longman, Harlow, 1988.
    41    
     40 Construction, Longman, Harlow, 1988.
     41
    4242[2] J.A.W. Gut, J.M. Pinto, Modeling of plate heat exchangers
    43 with generalized configurations, Int. J. Heat Mass Transfer
    44 46 (14) (2003) 2571\2585.
     43 with generalized configurations, Int. J. Heat Mass Transfer
     44 46 (14) (2003) 2571\2585.
    4545";
    4646
     
    8888out OutletCold          as streamPH     (Brief="Outlet Cold Stream", PosX=1, PosY=0.2793, Symbol="_{outCold}");
    8989
    90         HotSide                 as Main_PHE             (Brief="Plate Heat Exchanger Hot Side");
    91         ColdSide                as Main_PHE             (Brief="Plate Heat Exchanger Cold Side");
    92         Thermal                 as Thermal_PHE  (Brief="Thermal Results");
     90        HotSide                 as Main_PHE             (Brief="Plate Heat Exchanger Hot Side", Symbol="_{hot}");
     91        ColdSide                as Main_PHE             (Brief="Plate Heat Exchanger Cold Side", Symbol="_{cold}");
     92        Thermal                 as Thermal_PHE  (Brief="Thermal Results", Symbol = " ");
    9393
    9494 SET
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