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2007 IntroBiomechanics-- W5 2007/10/8 1 1 Bio-fluid Mechanics I Viscosity, Re, Vortices, Forces of Flow, and Bernoulli’s Principles Introduction to Biomechanics 2008/10/22 2 I. Viscosity 3 Contrast b/w solid and fluid Bernoulli’s principle Cons. of energy Principle of continuity Cons. of mass Drag Frictional force Momentum flux change Force Velocity gradient Shearing plane Streamline Interface Viscosity Elastic modulus Density Mass Fluids Solids … resist to deform … defining boundary 4 Important properties - Density (m/V): air ~ 1.2 kg/m 3 , water ~ 1000 kg/m 3 - Viscosity: Viscous dense, e.g. ρ motor oil < ρ water t k F θ = Fluids: … how fast sheared; shape not returned dz dv S F μ τ = = (unit: kg/m·s or Pa·s) 5 Viscosity : Measuring kinematic viscosity e.g. Ostwald (capillary) viscometer www.greentree.com.tw www.oil.net.tw/lbg2006 /chapter/3-1.htm ρ μ η = ' ' η η = t t 6 ρ μ η =

Bio-fluid Mechanics I - 國立中興大學ezphysics.nchu.edu.tw/chi/2008f_IntroBiomechanics/20… ·  · 2009-02-24Bio-fluid Mechanics I Viscosity, Re, ... fluid mechanics of spinning

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  • 2007 IntroBiomechanics-- W5 2007/10/8

    1

    1

    Bio-fluid Mechanics IViscosity, Re, Vortices, Forces of Flow,

    and Bernoullis Principles

    Introduction to Biomechanics 2008/10/22

    2

    I. Viscosity

    3

    Contrast b/w solid and fluid

    Bernoullis principleCons. of energy

    Principle of continuityCons. of mass

    DragFrictional force

    Momentum flux changeForce

    Velocity gradientShearing plane

    StreamlineInterface

    ViscosityElastic modulus

    DensityMass

    FluidsSolids

    resist to deform defining boundary

    4

    Important properties

    - Density (m/V): air ~ 1.2 kg/m3, water ~ 1000 kg/m3

    - Viscosity: Viscous dense, e.g. motor oil < water

    tkF =Fluids: how fast sheared; shape not returned

    dzdv

    SF == (unit: kg/ms or Pas)

    5

    Viscosity: Measuring kinematic viscosity

    e.g. Ostwald (capillary) viscometer

    www.greentree.com.tw

    www.oil.net.tw/lbg2006/chapter/3-1.htm

    =

    ''

    =tt

    6

    =

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    7

    In this class, assuming.

    1. Incompressible fluids

    2. No-slip condition

    3. Newtonian fluids (i.e. constant viscosity)

    4. Steady flow (i.e. same v @ same location)

    5. No fluid-fluid interfaces

    8

    II. Flow Regimes

    9

    Flow regimes

    Laminar flow(predictable, orderly)

    Turbulent flow

    Major difference NOT the presence of vortex

    When fluids pass through an obstacle

    10

    Transition: laminar turbulent

    Two forces involve: inertial & viscous forces

    lSvma

    FF

    viscous

    inertial

    =

    (individuality) (groupiness)

    Re===

    lv

    lSvtSlv

    Reynolds number

    11

    lv

    =Re, of the fluid (medium)

    l Characteristic lengthConvention: mostly in the direction of the flow

    Exception:

    Osborne Reynolds (1883): In circular pipe of certain length, turbulent occurs when

    Re > 2000 (l = d=2r) or Re > 1000 (l = r) (our circulatory system, still laminar when Re ~ 4000)

    12

    =

    In water vs. air

    for a given size, same velocity: Rewater > Reairbut usually vair > vwater, Rebird ~ Refish if similar size

    lv

    =Re

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    13

    Note: Re is just a crude number, so only look at its order of magnitude (usually significant digits < 2)

    14

    A useful tool for making models:

    For two geometrically similar situations, equality of Re Equality of the patterns of flow, whatever the individual

    values of length, speed, density, and viscosity

    Other use for Re

    Examples

    15

    Re & Consequences of the No-slip condition

    @ low Re, viscous force dominates; with no-slip condition shallow velocity gradient

    (semi-stagnant fluid surrounding object)

    Daphnia

    rake or paddle?

    by Koehl

    Male moths antenna

    Leakiness: 8~18% (Vogel, 1983) 16

    III. Vortices

    17

    Streamlines and the Appearance of Flows

    S1 S2dl1

    dl2

    1v2v

    At the same time, volume in = volume out

    dtdlS

    dtdlS 2211 =

    2211 vSvS = Principle of continuity

    Conservation of mass

    Incompressible flow in a rigid pipe

    18

    Path of each fluid particle

    (pathline)

    Particles wont cross Virtual wall

    3D ~ in tube (Principle of Continuity holds)

    2211 vsvs =

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    19

    Fig. 6.7: Flow around a circular cylinder

    20

    Asymmetrical vortices shedding subject vibrates

    Some problems

    Antenna of the car vibrates use spiral around to break the vortices

    Chimney, bridge, tree problematic if vibrating frequency caused by vortices shedding = natural frequency

    21

    Some vortex phenomena & examples

    Various vortices

    Fig. 6.10

    22

    Von Karman trail vs. vortices behind a swimming fish

    Removes momentum from the fluid

    Impart momentum to the fluid

    [Some vortex phenomena & examples]

    23 24

    Ground-Level Vortices

    Ground

    Wind What happens behind the chimney?

    Viscous entrainment

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    25

    e.g. A black fly larva

    Use of Ground-Level Vortices

    Fig. 6.12 (a)Fig. 6.12 (a)

    26

    [Use of Ground-Level Vortices]

    e.g. Phalarope

    Fig. 6.12 (b)

    Obst, et al. 1996. Kinematics and fluid mechanics of spinning in phalaropes. Nature (+ cover photo). 384: 121.

    27

    http://content.ornith.cornell.edu/UEWebApp/images/fig2_1305.gif

    http://www.mbari.org/seminars/1998/jan28_hamner.html

    [More on phalarope]

    28

    Shear motion within a velocity gradient rotation in solid body or fluid itself

    Fig. 6.13

    29

    IV. Forces of Flow

    30

    Force as Momentum Change

    Main forces: Drag ()(Ch7), Lift ()(Ch12), Thrust ()(Ch13)

    Force:

    maF =

    tmv

    tvmF

    =

    =

    )(dt

    dvmF =

    rate of momentum change

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    31

    2SvtvSl

    tmv == Eq. 4.9

    For flowing fluids, the dimension

    211

    222 vSvSt

    mvF =

    =

    Fig. 7.1a

    If v2 > v1,

    by Principle of Continuity(S1v1 = S2v2)

    S2 < S1

    32

    For a propeller or fan Force exerted on the mounting

    For a propeller on a craft Thrust

    For a passive body Drag (v1 > v2)

    211

    222 vSvSF =

    From amount of constriction or v:

    But in real case, v2 is rarely uniform across the flow

    33

    How to measure drag?

    Fig. 7.1b

    211

    222 vSvSF =

    To get vFlow sensorNeutrally buoyant particles (photographs, videorecording)

    34

    (Digital) Particle Image Velocimetry

    (PIV or DPIV)

    35

    Example: Liao et al., 2003, Science.

    36

    V. Pressure in the Flow & Bernoullis Principle

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    37

    Static + Dynamic pressure ( = total head) sd ppH +=

    21

    21 22 vp

    Vmv d

    ==

    Kinetic energy per unit volume

    dynamic pressure

    Dynamic Pressure

    Incompressible fluid stop at the wall exerts pressure

    38

    Two Principles

    Principle of Continuity applied all the time (even viscosity)

    Bernoullis Principle some assumptions:

    1. Viscosity negligible (i.e. Ideal fluid)

    2. Steady flow

    3. Incompressible fluid

    4. Gravity can be ignored

    39

    Bernoullis Principle (Conservation of Energy)

    SSdlm =

    dp

    dzdtdvSdlma

    gdzSSdpF

    ==

    =

    Divided by mass & rearrange 0=++dtdv

    dldzg

    dldp

    Newtons 2nd Law:

    40

    0=++dtdv

    dldzg

    dldp

    to get rid of t, assuming steady flow vdldt =

    0=++dl

    vdvdldzg

    dldp

    .21 2 constvgzp =++

    assuming const. density

    Integrate

    .21 2 constvgzp =++ OR

    0)(21 2

    12

    2 =++ vvzgp

    41

    Flow-induced pressure difference (as ventilation system)

    Fig. 7.5

    Ex1: Prairie dog burrow

    (Work done by Vogel use geometrically similar model (i.e. same Re) (p. 126 of text)

    Applications of Bernoullis Principle

    42

    Ex2: Keyhole limpet

    [Applications of Bernoullis Principle]

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    43

    Ex3: Fish nose How does water get in?

    Ventral view

    Shark:

    [Applications of Bernoullis Principle]

    44

    Dye released upstream of the nares in a dead shark

    Experiment setup:

    45

    PPv

    v

    Unidirectional flow

    A slope exists between incurrent and excurrent nares:

    Velocity gradient creates a pressure difference (Bernoullis Principle)

    Results:

    46

    VI. Drag

    47

    Pressure & Drag

    Fluid flows from high P to low P

    At some point, upstream

    flow occurs

    Fig. 7.8

    Separation of flow

    22

    2

    21 v

    p

    v

    p

    =

    48Fig. 6.7

    Flow separation vs. Drag

    Flow separation indirect cause

    of high drag (asym. pressure)

    At higher velocity (Re), more

    momentum to turn

    Separation point further aft

    (less pressure difference)

    Narrow wake

    Less drag

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    49

    Two types of drag

    1.Skin friction: from viscosity (Re < 10), Total surface area

    Dominates @ low Re Streamlining does no good

    2. Pressure drag: due to pressure distribution

    Drag Dynamic pressure ( )

    Depends on frontal area, shape, Re ( )

    2

    21 v

    v

    lv

    50

    Drag coefficient

    2

    2vpCp

    = 2

    2vSDCd

    =pSD =Q

    For a given shape,

    Cd varies only with Re

    (graphs available to look up)

    Fig. 7.9

    51

    III III

    vD 2vD

    11 Re

    vCvD

    d

    I

    00

    2

    Re

    vCvD

    d

    II

    5.05.0

    5.1

    Re

    vCvD

    d

    Streamlining:

    52

    Drag coefficients for various shapes (from Denny, 1988)

    sphere hollow hemisphere solid hemisphere

    47.0=dC 38.0 42.1 42.0 17.1

    cylinder hollow half-cylinder half-rectangular solid

    17.1=dC 20.1 30.2 55.1 98.1

    long, flat plate

    v

    v

    53

    2

    21 SvCD d =

    Area S Different convention for different shapes

    High-drag bodies frontal (projected) area

    Streamlined bodies total surface (wetted) area

    Lift-producing bodies plan form area

    Blimps & organisms (eg. fish) Volume2/3

    Same drag different Cd if different S is used

    Have to be consistent54

    Tricks for dropping ones drag

    Streamlining

    Dimpling golf balls go further than smooth ones

    (permit fluid to flow further around before

    separation narrower wake less drag)

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    55

    Flow-wise ribbing e.g. shark skin, scallop shells,

    Riblets for racing boats

    by breaking up cross-flow vortices near the surface

    skin friction at high Re56

    Mucus long-chain polymeric molecules

    (gentler velocity gradient less surface shear)

    The issues

    (1) Well documented in pipes and for flow over test

    body: kinds of molecules (fishes & some animals seem to

    have the right kind)

    (2) Drag reduction by mucus in Nature is difficult to

    demonstrate: cost of production + other functions of

    mucus just complicate the situations

    57

    Compliant surfaces, e.g. dolphin skin (a long story)

    58

    Other mechanisms:

    Surface heating by skin friction, but calculations suggest it negligible

    Injection of fast water along the surface from

    opercula, drag 10% for a trout at top speed

    Surface roughening in critical regions seems possible

    for some fast fishes

    Active control pressure detectors allow a fish to fine-

    tune its head turning to drag

    [Good reviews see Bushnell & Moore (1991) and Fish (1998)]

    59

    TO BEAR IN MIND

    A claim of drag reduction in a biol. system should be viewed

    with skepticism until

    (1) plausible physical mechanism

    (2) shown to work on physical models under biol. relevant

    conditions

    (3) shown to work by some direct test on real organisms

    under controlled and reproducible conditions

    60

    http://web.mit.edu/fluids/www/Shapiro/ncfmf.html

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    61 62

    63 64

    Stanislav Gorb

    Leader of Evolutionary Biomaterials Group

    Max-Planck-Institute for Metals Research

    65 66

    Paper written by Professor Stanislav Gorb:

    1. Arzt, E., Gorb, S. and Spolenak, R. (2003). From micro to nanocontacts in biological attachment devices. PNAS 100, 10603-10606.

    2. Arzt, E., Gorb, S. and Spolenak, R. (2003). From micro to nanocontacts in biological attachment devices. PNAS 100, 10603-10606.

    3. Gorb, S., Varenberg, M., Peressadko, A. and Tuma, J. (2007). Biomimetic mushroom-shaped fibrillar adhesive microstructure. J. R. Soc. Interface 4, 271-275.

    4. Gorb, S. N. and Varenberg, M. (2007). Mushroom-shaped geometry of contact elements in biological adhesive systems. J. Adh. Sci. & Tech. 21, 1175-1183.

    5. Jiao, Y., Gorb, S. and Scherge, M. (2000). Adhesion measured on the attachment pads of Tettigonia viridissima (Orthoptera, insecta). JEB 203, 1887-1895.

    3-page report on 1 paper due on 12/3

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    67 68

    1. Read this paper

    paper reading worksheet due on 11/26

    2. Do motion analyses on 12/3

    present on 12/10