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Distributed Resistance Models

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    Analysis Characteristics

    • Steady-state
    • Three Dimensional Internal Flow
    • Turbulent
    • Incompressible Flow
    • Distributed Resistance Models

    Reference

    White, F.M., “Fluid Mechanics”, McGraw-Hill, New York, 1979, pp. 305-360

    Idelchik, I.E., “Handbook of Hydraulic Resistance”, CRC Press, 1994, pp. 523

    Problem Description

    Air flows through a 3D channel with slip walls with a filter (or some flow obstruction) in the center of the channel. The pressure drop across the channel is due to only the obstruction because the walls have slip conditions.

    All 4 distributed resistance models are tested:

    1. Constant K factor:

    K = 1.97748

    At the specified pressure drop, this K factor should result in a flow rate of 0.2 m3/s.

    2. Pipe friction loss:

    where is the friction factor for which we use a Blasius formula for the friction factor. L = 41.99 is the pipe length to be represented, and DH = 0.2 is hydraulic diameter of the pipe. The Blasius formula used to determine the friction factor is:

    where a is 0.316 and b is 0.25. These values should result in an equivalent K-factor value of 1.97748. Hence, we can expect a flow rate 0.2 m³/s.

    3. Free area ratio

    For this resistance type, we use the formula from page 516 in Idelchik:

    where FAR is the free area ratio. For a free area ratio of 0.62, we get a K factor of 1.9774 and thus a flow rate of 0.2 m³/s.

    4. Head-loss table K factor:

    We use the following table of values:

    Flow Rate (m3/sec) Pressure Head (Pa)
    0.15 35000
    0.25 45000

    Geometry and Boundary Conditions

    Results

    Distributed Resistance Type Benchmark 2013: Build 20120131 % Error
    Constant K 0.2 m3/s 0.1995 0.262
    Pipe Friction Loss 0.2 m3/s 0.1996 0.184
    Free Area Ratio 0.2 m3/s 0.1995 0.262
    Head Loss Table 0.2 m3/s 0.1986 0.702