EBSILON®Professional Online Documentation
In This Topic
    Component 54: Drain of Gas Streams
    In This Topic

    Component 54: Drain of gas streams


    Specifications

    Line connections

    1

    Inlet

    2

    Outlet

    3

    Water extraction

     

    General       User Input Values       Physics Used       Displays       Example

     

    General

    Component 54 checks whether there is liquid water in a pipe of any classical fluid type (air, flue gas, fuel gas, coal, oil,  user-defined fluid or crude gas) as a result of the partial pressures. This liquid phase will be extracted, either completely or partially. It is possible to specify either the drying factor (specification value DRAIN) or the mass flow of the extracted water (by a measurement point on the pipe 3).

    The following examples illustrate the use of the drier:

    If a gas mass flow having a humidity of 8%, is to be dried, a water mass flow of 4% will be extracted.

    Model 

    Default:

    X1i=M1i/M1,  X1H2OL=M1H2OL/M1 (water in M1 by M1)

    X2i=M2i/M2,  etc.

    i stands for the components

     

    The mass flow of the extracted water results from the degree of drying and the weight fraction X1H2OL of  the liquid water (H2OL) at line 1(inlet)

    M3 = Drying factor * X1H2OL * M1

     

    Line 3 contains water as the only component. The relations of the mass flows and the components at line 2 result in 

    M2 = M1 * [1 - X1H2OL * Drying ]

    M2H2OL = M1H2OL * (1-Drying)

    { X2i          = X1i / [1 - X1H2OL*Drying]  for all parts except water}

     

    The pressure is assumed to be constant

    P1 = P2 = P3

     

    The enthalpies result from the total of the specific enthalpies Hi with the temperatures

    T1 = T2 = T3

    and the components Xi

     

    H2 = S[H2i * X2i], H2i at (T2,P2)

    H3 =  H(H2OL), H at (T3,P3)

     

    Similar components:

    Component 4 (splitter):

    The branching mass flow 3 must be defined (e.g. by the component 33), or else must be known in the system by other means.

    Component 17  (splitter):

    The branching mass flow 3 must be defined by a characteristic line, which specifies the branching depending upon the incoming mass flow.

    Component 18  (splitter):

    The branching mass flow 3 is indicated as a fraction of the incoming mass flow. The relationship does not change for the off-design mode.

    Component 19  (Drier for wet steam):

    The extracted wetness results by specifying the portion, by which the humidity available in the wet steam is to be reduced.

    Component 52  (selective line junction):

    This component enables the separation of the particles from a gaseous fluid. For instance, gas purifiers like cyclones, Venturi washers, etc. can be modelled with the help of this component.


    User Input Values

     

    DRAIN

    Drying of water in M1 (relative)

    (M3 as fraction of liquid water in M1)

    FM

    Mass flow distribution

     

    Like in Parent Profile (Sub Profile option only)

    Expression

    =2: M2>=M3

    =3: M3>=M2

    -1: M3 specified externally

    FTABLE

    Handling the property set differences:

    Like in Parent Profile (Sub Profile option only)

    Expression

    =0: Temperature equilibrium maintained

    =1: Energy equilibrium maintained

     

    The flag FTABLE has the following background: in water and steam lines, the complete water/steam-property set is used (e.g. according to IAPWS-IF97). On the other hand, in the air/flue gas lines, other material values are used for the gaseous water (e.g. for ideal gas with FDBR-polynomials). This results in a small property difference: at a specified pressure and temperature, a slightly different enthalpy is calculated in the air line as in a water/steam line, at a specified pressure and enthalpy, however, there is no difference in the temperature. Normally, these differences do not affect the end result at all.

    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

    Under unfavorable circumstances (e.g. while modeling a mill), convergence problems arise when the extracted water is fed at another point again and the table differences can build up iteratively. This flag is included only for these special cases, so that one can specifically control, whether differences should appear in the enthalpy or in the temperature.


    Physics Used

    Equations

    All cases

     

    P2  = P1                                        

     

    P3  = P1                                        

     

    M3H2OL = M1H2OL * Drying

     

    M3  = M3H2OL                             

     

    M2 = M1 - M3                                

     

    X2i=M2i/M2 from the mass balance for all components

     

    H2 = f (p2,t2,X2i)                          

     

    H3 = f (p3,t3,H2OL)                     

     

     

     

     


    Component Displays

    Display Option 1

    Example

    Click here >> Component 54 Demo << to load an example.

    See Also

    CoalGasification