flow regimes and drag force

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    18 January 2007 1

    Drag on a Sphere and Settling Velocity

    DragOne of basic concepts in Hydraulicsand Fluid Mechanics

    Drag on a sphereA simple caseNo general theoretical solutionsStill a challenging topic

    18 January 2007 2

    Drag on a Sphere

    Sediment transport

    Sludge transport

    Air pollution

    Food processing

    Water purification

    L Applications

    A

    B

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    18 January 2007 3

    What is Drag?

    DragLift

    Drag is a hydro-/aero-dynamicforce that opposes an object's

    motion through a fluid

    18 January 2007 4

    Two kind of Drags

    P

    = dscosPDP

    = dssinDf Pressure Drag

    Friction Drag

    V

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    18 January 2007 5

    Two kind of Drags

    Pressure Drag depends on the shape of the object,

    and also called Form Drag.

    Friction Drag is related to the surface roughnessand the boundary layer. It is also called SurfaceDrag.

    18 January 2007 6

    Drag Coefficient

    Consider a flow with velocity V approaching an object

    V

    a b

    p

    2

    fp C*A*2

    V

    D =A

    Stagnation point

    V

    Pressure head b = Velocity head a(Bernoulli equation)

    g

    V

    g

    P a

    f

    b

    2

    2

    =

    Projected area normal to the flow

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    18 January 2007 7

    V

    D

    2

    fD C*A*2

    VF =

    Drag Coefficient

    Drag

    Drag Coefficient

    A

    18 January 2007 8

    Force Balance (Simplified BBO Equation)

    FW

    FBFD

    FD + FB = FW

    3

    6DgFB

    =

    24

    22 w

    DCF DD

    =

    3

    6DgF pW

    =

    32

    2

    6)(

    24Dg

    wDC pD

    =

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    18 January 2007 9

    Settling Velocity & Drag Coefficient

    32

    2

    6)(

    24Dg

    wDC pD

    =

    DC

    gDw

    =

    3

    4

    23

    4

    w

    gDCD

    = Here = (p - )/

    18 January 2007 10

    Re = wD/v

    CD

    1 2*105

    Laminar BL Turbulent BL

    General Relationship: CD ~ Re

    No inertial

    effect

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    18 January 2007 11

    Re

    CD

    1

    Theoretical Solution

    No inertial

    effect

    For creeping flow (Re = wD/v 2*105, Turbulent boundary layer,Wake size reduces,

    Drag sharply decreases

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    18 January 2007 13

    Flow over a Circular Cylinder

    Creeping Flow, Steady, Symmetric Streamlines

    (Van Dyke, 1982)

    18 January 2007 14

    Laminar Flow, Steady, Separated Flow

    (Van Dyke, 1982)

    Flow over a Circular Cylinder

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    18 January 2007 15

    Laminar Flow, Steady, Separated Flow

    (Van Dyke, 1982)

    Flow over a Circular Cylinder

    18 January 2007 16

    Unsteady Transitional Flow, Karman Vortex Street

    (Van Dyke, 1982)

    Flow over a Circular Cylinder

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    18 January 2007 17

    Unsteady, Turbulent Flow

    (Van Dyke, 1982)

    Flow over a Circular Cylinder

    18 January 2007 18

    Unsteady, Turbulent Flow

    (Van Dyke, 1982)

    Flow over a Circular Cylinder

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    18 January 2007 19

    Settling Velocity of a Sphere

    =

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    18 January 2007 21

    )(RefCD =

    )(3

    42

    v

    wDf

    w

    gD=

    (Iteration neededfor computing w)

    *

    3/1

    2

    3/1

    2

    4

    3DD

    gRe

    CD

    =

    )( *DfRe =

    )(Dfw =

    18 January 2007 22

    ( )

    =

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    18 January 2007 23

    Settling Velocity of Naturally Worn Particles

    ReCD

    32=

    2/32/3

    1+32

    =Re

    CD

    For Stokes range, it reduces to

    18 January 2007 24

    1

    10

    100

    1000

    10000

    100000

    1000000

    10000000

    100000000

    1E-07 1E-06 1E-05 0.0001 0.001 0.01 0.1 1 10 100 1000

    Re

    CD

    Experiment

    Computation

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    18 January 2007 25

    0.0000001

    0.000001

    0.00001

    0.0001

    0.001

    0.01

    0.1

    1

    10

    100

    1000

    10000

    0.01 0.1 1 10 100 1000

    D*

    Re

    Measurement

    Cheng (1997)

    5.12

    * )52.125( += DD

    w

    18 January 2007 26

    Km cw

    w)1( =

    Particle Concentration Effect on Settling Velocity

    75.0

    75.0

    175.01

    42.065.4

    +

    +

    =

    wD

    wD

    K

    Wm = w

    if c = 0