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    Component 34: Expander
    In This Topic

    Component 34: Expander


    Specifications

    Line connections

    1

    Inlet

    2

    Saturated steam outlet

    3

    Extraction of condensate

    4

    Injection of cooling water

     

    General       User Input Values       Physics Used       Displays       Example

     

    General

    The inlet condensate introduced into the expander, is eased on a lower pressure level.

    You can choose between two working conditions of the expander:

    1. The saturated steam arising during the expansion is condensed completely with the help of the cooling water shower and is also extracted sub cooled.

    2. The saturated steam arising during the expansion is condensed and the extracted condensate is mixed with cooling water and sub cooled.

     

    This component can also be operated with salt water as the inlet fluid. The evaporation thereby changes the salt content.

    The component can be used for modeling simple desalination processes. However, the component 92 (MSF stage) is needed for a more realistic and stable modeling of complex desalination plants.


    User Input Values

     

    DPN

    Pressure drop (nominal)

    DPN=P1N-P2N   

    DT3S3

    Sub Cooling temperature difference

    DT3S3=T3S-T3

    FMODE

    Flag for calculation mode

    Like in Parent Profile (Sub Profile option only)

    Expression

    =0:  GLOBAL

    =1:  Local off-design

    =-1: Local design

    FP

    Type of pressure calculation

    Like in Parent Profile (Sub Profile option only)

    Expression

    =1: P2 results from P1 and pressure drop DPN

    =2: P2 or P3 are specified from outside (e.g. with the components 1, 12, 36: boundary value, controllers and value transmitter respectively)

    FSPEC

    Water injection

    Like in Parent Profile (Sub Profile option only)

    Expression

    =1: complete condensation of steam and
                    sub cooling of the condensate by M4 to T3=T3S-DT3S3

    =2: Steam separation M2=X(P2=P3,H1)*M1, then
    cooling of the condensate by M4 to T3=T3S-DT3S3

    M1N       

    Mass flow (nominal)

    The parameters marked in blue are reference quantities for the off-design mode. The actual off-design values refer to these quantities in the equations used.  

    Generally, all inputs that are visible are required. But, often default values are provided.

    For more information on colour of the input fields and their descriptions see Edit Component\Specification values

    For more information on design vs. off-design and nominal values see General\Accept Nominal values


    Physics Used

    Equations

    All cases

     

    if GLOBAL = design, then {

    F1 = 1  }

    else {

    F1 = (M1/M1N)**2  }

    DP = DN * F1

    P2 = P1-DP                                           

    P2             from outside (FP = 2)

    P3 = P2                                                  

    if FSPEC = 1 (no steam outlet), then {

      H2 =H’’(P2)                                         

      H3 = f (P3,T3S-DT3S3)                    

      M2 = 0                                                   

      M4 = M1*(H1 - H3) / (H3 - H4)          

      M1 + M4 - M2 - M3 = 0                       

    }

    if FSPEC = 2 (steam outlet), then {

      X  = f(P2,H1)

      H3 = f(P3,T3S-DT3S3)                      

      if X = 1, then {

        M2 = M1                                              

        M4 = 0                                                 

        M1 + M4 - M2 - M3=0                       

        H2 = H1                                              

      }

      if X = 0, then {

        M2 = 0                                                

        M4 = M1* (H1 - H3) / (H3 - H4)      

        M1 + M4 - M2 - M3 = 0                    

        H2 = H’’(P2)                                      

      }

      if 0<X< 1, then {

        M2 = M1 * X                                       

        M33= M1 * (1 - x)

        H33= f(P3,T3S)

        M4 = M33* (H33 - H3) / (H3 - H4)

        M1 + M4- M2- M3 = 0                       

        H2 = H’’(P2)                                      

       }

     

     

    Component Displays

    Display Option 1

    Example

    Click here >> Component 34 Demo << to load an example.

    See Also