Boundary Layer Velocity Profile

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    Boundary Layer Velocity Profile

    z

    zU

    Viscous sublayer

    Buffer zone

    Logarithmic

    turbulent zone

    Ekman Layer, or

    Outer region

    (velocity defect layer)

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    But first.. a definition:

    2*ub

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    1. Viscous Sublayer - velocities are low, shear stress

    controlled by molecular processes

    As in the plate example, laminar flow dominates,

    z

    ub

    Put in terms of u*

    integrating,

    boundary conditions,

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    When do we see a viscous sublayer?

    v

    = f (u*, , ks)

    where ks== characteristic height of bed

    roughness

    Roughness Re:

    R*> 70 rough turbulent

    no viscous sublayer

    R*< 5 smooth turbulent

    yes, viscous sublayer

    sku

    R *

    *

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    2. Log Layer:

    Turbulent case, Azis NOT constant inz

    Azis a property of the flow, not just the fluid

    To describe the velocity profile we need to develop a

    profile ofAz.

    Mixing Lengthformulation Prandtl (1925) which is

    a qualitative argument discussed in more detail

    Boundary Layer Analysis by Shetz, 1993

    Assume that water masses act independently over adistance, l

    Within la change in momentum causes a fluctuation

    to adjacent fluid parcels.

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    At l,

    Make assumption of isotropic turbulence:

    |u| ~ |v| ~ |w|

    Therefore, |u| ~ |w| ~

    Through the Reynolds Stress formulation,

    dzud

    ul

    '~

    dz

    ud

    l dz

    ud

    l

    2

    2~

    ''

    dz

    udl

    wu

    zx

    zx

    Prandtl Mixing Length

    Formulation

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    Von Karmen (1930) hypothesized that close to a boundary,

    the turbulent exchange is related to distance from the

    boundary.

    lz

    l=Kz

    where K is a universal turbulent momentum exchangecoefficient == von Karmens constant.

    Khas been found to be 0.41

    Near the bed,

    dz

    udKzu

    dz

    udzK

    zx

    *

    2

    22

    in terms of u*

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    Solving for the velocity profile:

    ln z

    Intercept, b, depends on roughness of the

    bed - f (R*)

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    Rename b, based on boundary condition:

    z=zo at = 0

    Karmen-Prandtl Eq.

    or Law of the Wall

    o

    z

    z

    z

    Ku

    uln

    1

    *

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    Hydraulic Roughness Length,zo

    zois the vertical intercept at which

    z= 0

    zo= f ( viscous sublayer,

    grain roughness,

    ripples & other bedforms,

    stratification)

    This leads to two forms of the Karmen-Prandtl Equation

    1) with viscous sublayer HSF

    2) without viscous sublayer HRF

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    Can evaluate which case to use with R*

    where ks== roughness length scale

    in glued sand, pipe flow experiments

    ks=D

    in real seabeds with no bedforms,

    ks=D75

    in bedforms, characteristic bedform scale

    ks~ height of ripples

    skuR *

    *

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    1. Hydraulically Smooth Flow (HSF) 50 *

    *

    Sku

    R

    ** boundary layer is

    turbulent, but there is

    a viscous sublayer

    zo

    is a fraction of the

    viscous sublayer

    thickness:

    Karmen-Prandtl equation

    becomes:

    For turbulent flow over a

    hydraulically smooth boundary

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    2. Hydraulically Rough Flow (HRF) 70*

    *

    Sku

    R

    ** no viscous sublayerzois a function of theroughness elements

    Nikaradze pipe flow

    experiments:

    Karmen-Prandtl equation

    becomes:

    For turbulent flow over a

    hydraulically rough boundary with

    no bedforms, no stratification, etc.

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    Notes on zoin HRF

    Grain Roughness:

    Nikuradze (1930s) - glued sand grains on pipe flow

    zo=D/30

    Kamphius (1974) - channel flow experiments

    zo=D/15

    Bedforms:

    Wooding (1973)

    whereHis the ripple height

    and is the ripple wavelengthSuspended Sediment:

    Smith (1977)

    zo= f (excess shear stress, andzofrom ripples)

    4.1

    20

    HHz

    o

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    3. Hydraulically Transitional Flow (HTF) 705 **

    Sku

    R

    zois both fraction of the viscous sublayer thickness and afunction of bed roughness.

    Karmen-Prandtl equation is

    defined as:

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    Bed Roughness is never well known or characterized, but fortunately

    not necessary to determine u*

    If you only have one velocity measurement (at a single elevation), usethe formulations above.

    If you can avoid it.. do so.

    With multiple velocity measurements, use the Law of the Wall to

    get u*

    o

    z

    z

    z

    Ku

    uln

    1

    *ln z

    z

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    To determine b(or u*) from a velocity profile:

    1. Fit line to data

    2. Find slope -

    3. Evaluate

    )(

    lnln

    12

    12

    uu

    zzm

    mu

    K

    *