Drag Coefficient Report

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    INTRODUCTION

    In fluid dynamics, the drag coefficient is a dimensionless quantity that is used to quantify the

    drag or resistance of an object in a fluid environment such as air or water. It is used in the drag

    equation where lower drag coefficient indicates the object will have less aerodynamic or

    hydrodynamic drag. The drag coefficient is always associated with a particular surface area.

    figure 1: Measured drag Coefficient

    The drag coefficient of any object comprises the effects of the two basic contributors to fluid

    dynamic drag: skin friction and form drag. The drag coefficient of a lifting airfoil orhydrofoil also

    includes the effects oflift-induced drag.

    The drag coefficient of a complete structure such as an aircraft also includes the effects

    ofinterference drag.

    The drag equation:

    is essentially a statement that the drag force on any object is proportional to the density of the

    fluid and proportional to the square of the relative speed between the object and the fluid.

    http://en.wikipedia.org/wiki/Fluid_dynamicshttp://en.wikipedia.org/wiki/Fluid_dynamicshttp://en.wikipedia.org/wiki/Skin_frictionhttp://en.wikipedia.org/wiki/Form_draghttp://en.wikipedia.org/wiki/Airfoilhttp://en.wikipedia.org/wiki/Hydrofoilhttp://en.wikipedia.org/wiki/Lift-induced_draghttp://en.wikipedia.org/wiki/Interference_draghttp://en.wikipedia.org/wiki/Drag_(physics)http://en.wikipedia.org/wiki/Forcehttp://en.wikipedia.org/wiki/Speedhttp://en.wikipedia.org/wiki/Fluid_dynamicshttp://en.wikipedia.org/wiki/Fluid_dynamicshttp://en.wikipedia.org/wiki/Skin_frictionhttp://en.wikipedia.org/wiki/Form_draghttp://en.wikipedia.org/wiki/Airfoilhttp://en.wikipedia.org/wiki/Hydrofoilhttp://en.wikipedia.org/wiki/Lift-induced_draghttp://en.wikipedia.org/wiki/Interference_draghttp://en.wikipedia.org/wiki/Drag_(physics)http://en.wikipedia.org/wiki/Forcehttp://en.wikipedia.org/wiki/Speed
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    Cd is not a constant but varies as a function of speed, flow direction, object position, object size,

    fluid density and fluid viscosity. Speed, kinematic viscosity and a characteristic length scale of

    the object are incorporated into a dimensionless quantity called the Reynolds numberor .

    is thus a function of . In compressible flow, the speed of sound is relevant and is also a

    function ofMach number .

    For a certain body shape the drag coefficient only depends on the Reynolds number ,

    Mach number and the direction of the flow. For low Mach number , the drag coefficient

    is independent of Mach number. Also the variation with Reynolds number within a practical

    range of interest is usually small, while for cars at highway speed and aircraft at cruising speed

    the incoming flow direction is as well more-or-less the same. So the drag coefficient can

    often be treated as a constant.

    For a streamlined body to achieve a low drag coefficient the boundary layeraround the body

    must remain attached to the surface of the body for as long as possible, causing the wake to be

    narrow. A high form drag results in a broad wake. The boundary layer will transition from

    laminar to turbulent providing the Reynolds numberof the flow around the body is high enough.

    Larger velocities, larger objects, and lowerviscosities contribute to larger Reynolds numbers.

    For other objects, such as small particles, one can no longer consider that the drag

    coefficient is constant, but certainly is a function of Reynolds number. At a low Reynolds

    number, the flow around the object does not transition to turbulent but remains laminar, even up

    to the point at which it separates from the surface of the object. At very low Reynolds numbers,without flow separation, the drag force is proportional to instead of ; for a sphere this is

    known as Stokes law. Reynolds number will be low for small objects, low velocities, and high

    viscosity fluids.

    Figure 2: Flow past a Circular Cylinder at various Reynolds Numbers, continued

    http://en.wikipedia.org/wiki/Viscosityhttp://en.wikipedia.org/wiki/Kinematic_viscosityhttp://en.wikipedia.org/wiki/Length_scalehttp://en.wikipedia.org/wiki/Reynolds_numberhttp://en.wikipedia.org/wiki/Mach_numberhttp://en.wikipedia.org/wiki/Boundary_layerhttp://en.wikipedia.org/wiki/Wakehttp://en.wikipedia.org/wiki/Reynolds_numberhttp://en.wikipedia.org/wiki/Viscosityhttp://en.wikipedia.org/wiki/Stokes_lawhttp://en.wikipedia.org/wiki/Viscosityhttp://en.wikipedia.org/wiki/Kinematic_viscosityhttp://en.wikipedia.org/wiki/Length_scalehttp://en.wikipedia.org/wiki/Reynolds_numberhttp://en.wikipedia.org/wiki/Mach_numberhttp://en.wikipedia.org/wiki/Boundary_layerhttp://en.wikipedia.org/wiki/Wakehttp://en.wikipedia.org/wiki/Reynolds_numberhttp://en.wikipedia.org/wiki/Viscosityhttp://en.wikipedia.org/wiki/Stokes_law
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    Figure 3 :Flow past a Circular Cylinder at various Reynolds Numbers

    A equal to 1 would be obtained in a case where all of the fluid approaching the object is

    brought to rest, building up stagnation pressure over the whole front surface. The top figure

    shows a flat plate with the fluid coming from the right and stopping at the plate. The graph to the

    left of it shows equal pressure across the surface. In a real flat plate the fluid must turn around

    the sides, and full stagnation pressure is found only at the center, dropping off toward the edges

    as in the lower figure and graph. Only considering the front size, the of a real flat plate wouldbe less than 1; except that there will be suction on the back side: a negative pressure (relative

    to ambient). The overall of a real square flat plate perpendicular to the flow is often given as

    1.17. Flow patterns and therefore for some shapes can change with the Reynolds number

    and the roughness of the surfaces.

    http://en.wikipedia.org/wiki/Stagnation_pressurehttp://en.wikipedia.org/wiki/Stagnation_pressure
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    THEORY

    It is a general experience that a body meets some resistance when it is forced to move through

    a fluid especially liquid, such as difficulty to walk in water because of the much greater

    resistance it present rather than air.

    It is found that drag coefficient much convenient to work with dimensionless unit as it a function

    of Reynolds number. The part of drag that is directly to wall shear stress is called skin friction

    drag(or friction drag)as it caused by frictional effects, and the part is directly due pressure is

    known as pressure drag(known as form drag due to strong dependence on the form or the

    shape of the body).

    Drag coefficient:

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    Friction drag coefficient:

    Pressure drag coefficient:

    When the friction and pressure drag coefficients or forces are presented, total drag coefficients

    or drag force can be determined. The drag force is the net force exerted by a fluid on a body in

    the direction of flow due to the combined effects of wall shear and pressure forces.

    Total drag coefficients;

    Total drag force;

    The contribution of friction drag is less at higher Reynolds number or might negligible at very

    high Reynolds number due to pressure drag. While at low Reynolds number, especially highly

    streamlined bodies case such as airfoils, is due to friction drag, bodies with larger surface area

    result a larger friction drag, since friction drag is proportional to the surface area.

    The pressure drag is proportional to the frontal area and to the difference between the pressure

    acting on the front and back of the immersed body. The pressures drag most significant when

    the velocity of the fluid is too high for the fluid to follow the curve of the body, and at some point,the fluids break away from the body and create a very low pressure region in the back, in this

    case, due to large pressure difference between front and back sides of the body.

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    Consideration of the physical factors which influence the drag force leads to the listing of the

    following as principal variables:

    FD the drag force on the sphere

    D the diameter of the sphere

    u the free stream velocity of the fluid

    the density of the fluid

    the viscosity of the fluid

    Therefore, the following may be written:

    ),,,,(

    = uDfFD (0)

    or, supplying some constants,

    .dcba

    D uCDF = (0)

    Using the mass-length-time systems of units and substituting the proper dimensions,

    .32

    dcb

    a

    LT

    M

    L

    M

    T

    LL

    T

    ML

    = (0)

    Since the dimensions must be the same on both sides of the equation, the exponents must be

    the same for each unit. Thus,

    For M: dc+=1

    For L: dcba += 31

    For T: .2 db=

    Solving these equations in terms ofd,

    .1;2;2 dcdbda ===

    Thus,

    .122 dddd

    D uCDF

    = (0)

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    Now, grouping variables according to exponents,

    ,22

    d

    D

    DuuCDF

    =

    (0)

    where

    Du is a dimensionless group called the Reynolds number. Regrouping, this equation

    can be rewritten in the general form

    ( ),Re22

    fuD

    FD =

    (0)

    that effectively reduces the number of variables to two dimensionless groups, which are, in turn,

    functions of density, viscosity, diameter, and velocity. By varying any one or more of these

    parameters, a correlation between the two groups can be formed.

    An expression for the drag force on a body is usually given in the form

    c

    DDg

    uACF

    2

    2

    =

    (0)

    where,

    CD is a dimensionless drag coefficient,

    A is the frontal area of the body exposed to the flow (D2/4 for a sphere),

    gcis the gravitational constant which allows the left hand side to be expressed in units of

    force.

    This expression can be related to equation 0 by solving for the drag coefficient:

    ( ).Re82

    222f

    uD

    gF

    uA

    gFC cDcDD =

    ==

    (0)

    Therefore, the drag coefficient itself is a function of the Reynolds number.

    Based on experiments on to measure drag coefficient of sphere

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    Calculation of air density

    Assuming ideal gas conditions, the density of air can be calculated using

    =

    Where R is the gas constant for air, R= 53.34

    Calculation of velocity pressure from manometer reading

    P= h

    Calculation of free stream air velocity

    By neglecting compressibility effects, the free stream air velocity can be derived from the

    Bernoulli equation as:

    Calculation of Reynolds number

    The Reynolds number based on the sphere diameter is defined by the equation

    Re =

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    OBJECTIVE

    To measure drag coefficient of sphere as a function of reynolds number.

    DISCUSSION

    TYPE OF DRAG COEFFICENT MEASUREMENT

    Cylinder

    A water tunnel is used to analyze the effects of fluid flow over a cylinder. As the water circulates

    through the closed-loop system, the cylinder obstructs the path of the fluid flow causing the

    water to deviate from its otherwise uninterrupted flow path. The uniform velocity profile of the

    flow becomes non-uniform as the fluid passes by the cylinder. The drag caused by the cylinder

    can be calculated through two different methods: control surface analysis consisting of pressure

    measurements around the cylinder, and control volume analysis consisting of velocity

    measurements taken before and after the cylinder. These experimentally obtained pressure and

    velocity measurements provide the necessary data required to find the coefficient of drag of the

    cylinder for this experiment. With these two methods of obtaining the drag coefficient, the fluid

    flow around the cylinder can be observed, analyzed, and compared.

    Sphere

    The Handbuch values are based on experiments with falling or fixed spheres; and differences in

    drag for rising and falling spheres have been previously observed by Hes selberg and Birkeland

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    and others. It thus seems that the flow around a rising sphere is somehow different from that

    around a falling one.

    EXAMPLE OF EXPERIMENT

    Description of Experimental Setup

    Figure 1 Low speed wind tunnel

    A manually controlled variable speed wind tunnel similar to that shown in Figure 1 was used in

    this experiment. The wind tunnel was equipped with an integral force balance which measured

    both drag and lift forces and a multistation manometer tube bank to measure the velocity of the

    air stream. A separate pitot tube was used to verify the calibration of the built-in manometer. A

    mercury barometer was used to measure the atmospheric pressure and a thermometer was

    used to measure the air temperature.

    APPARATUS

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    1. Flotek 250 wind tunnel located in the Mechanical Engineering Laboratory (S/N FT250-2784)

    2. 2.5-inch diameter smooth calibration sphere wind tunnel accessory

    3. Pitot tube and differential manometer (Property tag BSW365-22984)

    4. Mercury barometer fixed to the wall near the wind tunnel.

    5. Mercury thermometer (Sargent brand, no tag or serial number)

    APPLICATION

    Drag coefficients are used in the calculation of particle terminal settling velocity of solids and

    therefore used where the suspension or settling of solids particle will occur in chemical unit

    operations. There are hundred of correlations relating the drag coefficient to the particle

    Reynolds number and some form of measure of the particle shape (i.e sphericity). The particle

    terminal settling velocity in turn can be used to calculate the hindered settling velocity, so it can

    be used to help design solid-liquid mixers, clarifiers, thickeners, slurry transport in pipe

    (i.e design a slurry pump), solid-liquid filters, it can also be used to design pneumatic transport

    lines to name but a few. It can be used to help design unit operations where solid -fluid (liquid or

    gas) will need to be mixed, transported or separated.

    This topic is under the Fluid Mechanics branch. The drag force can be applied in many

    things with regard for chemical engineering. for example, in a stream of air Oxygen can beabsorbed by another media, now knowing the drag force for air that will indicate along with

    diffusion rate of Oxygen into the media how much Oxygen has been transferred also. To

    calculate the temperature profile for some application that uses air as a cooling media, drag

    force can be used. In separation drag force will tell how much component A has moved a long

    with component B depending on the drag force of B.

    ADVANTAGE AND DISADVANTAGE

    Less road spray (i.e. better visibility for other road users)

    Reduced dirt deposition on the tractor and semi-trailer

    Reduced sensitivity to crosswinds, hence better steering

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    Stability, less tyre wear and tear and improved driving comfort

    Better safety (additional crumple zones, better protection against blind spot accidents)

    Lower noise

    MODELLING OF AERODYNAMIC

    The drag coefficient (Cd) of a car tells you how well it cuts through the air. In other words, how

    aerodynamically efficient it is. A low Cd figure brings three main benefits higher top speed,

    better fuel consumption and quieter cruising.

    A Lexus car spends thousands of hours in the wind tunnel during its aerodynamic development.

    Yet achieving the optimum body shape is only the first of the refinements that ensure the car

    slips through the air with the minimum of effort.

    The precise and narrow gaps in Lexus bodywork also contribute significantly. So do flush-fittingwindows and trim, tyre spoilers behind the front wheels and ahead of the rear wheels, under-

    body panels that streamline chassis components, and rear spoilers that reduce turbulence as

    the airflow leaves the car.

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    REFERENCES

    D. M. Smiadak.2008. ,Fluid Mechanic: Drag Coefficient of a Sphere.

    G. Bruschi, T. Nishioka, K.Tsang and R. Wang.,2003. A Comparison Of Analytical Methods.

    Drag Coefficient Of A Cylinder.

    A.W. Preukschat, 1962. Measurements of Drag Coefficients for Falling And Rising Spheres In

    Free Motion. California Institute of Technology Pasadena, California

    Joe, 2002. Determination of the Drag Coefficient of a Sphere.College of Engenieering and

    Sciences,Louisiana Tech University.