ae 233 (chapter 1) fluid mechanics for chemical engineering

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    FLUID MECHANICS FOR

    CHEMICAL ENGINEERINGChapter 1: Fluid Mechanics andFluid Properties

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    SEQUENCE OF CHAPTER 1Introduction

    Objectives

    1.1 Definition of A Fluid

    Shear stress in moving fluid

    Differences between liquid and gases

    Newtonian and Non-Newtonian Fluid

    1.2 Engineering Units

    1.3 Fluid Properties

    Vapor Pressure

    Engineering significance of vapor pressure

    Surface Tension

    CapillarityExample 1.2

    Example 1.3

    Summary

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    Introduction

    Fluid mechanics is a study of the behavior of fluids,either at rest (fluid statics) or in motion (fluiddynamics).

    The analysis is based on the fundamental laws of

    mechanics, which relate continuity of mass and energywith force and momentum.

    An understanding of the properties and behavior offluids at rest and in motion is of great importance in

    engineering.

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    1. Identify the units for the basic quantities of time,length, force and mass.

    2. Properly set up equations to ensure consistency ofunits.

    3. Define the basic fluid properties.

    4. Identify the relationships between specific weight,specific gravity and density, and solve problems usingtheir relationships.

    Objectives

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    1.1 Definition of Fluid

    Fluid mechanics is a division in applied mechanics related tothe behaviour of liquid or gas which is either in rest or inmotion.

    The study related to a fluid in rest or stationary is referred

    tofluid static, otherwise it is referred to asfluid dynamic. Fluid can be defined as a substance which can deform

    continuously when being subjected to shear stress at anymagnitude. In other words, it can flow continuously as aresult of shearing action. This includes any liquid or gas.

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    1.1 Definition of Fluid

    A fluid is a substance, which deforms continuously, orflows, when subjected to shearing force

    In fact if a shear stress is acting on a fluid it will flowand if a fluid is at rest there is no shear stress acting on

    it.

    Fluid Flow Shear stress Yes

    Fluid Rest Shear stress No

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    1.1 Definition of Fluid

    Thus, with exception to solids, any other matters can becategorised as fluid. In microscopic point of view, thisconcept corresponds to loose or very loose bonding betweenmolecules of liquid or gas, respectively.

    Examples of typical fluid used in engineering applications arewater, oil and air.

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    1.1 Fluid Concept

    In fluid, the molecules can move freely but are constrainedthrough a traction force called cohesion. This force isinterchangeable from one molecule to another.

    For gases, it is very weak which enables the gas to

    disintegrate and move away from its container. For liquids, it is stronger which is sufficient enough to hold

    the molecule together and can withstand high compression,which is suitable for application as hydraulic fluid such as oil.On the surface, the cohesion forms a resultant force directed

    into the liquid region and the combination of cohesion forcesbetween adjacent molecules from a tensioned membraneknown asfree surface.

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    1.1 Definition of Fluid

    Figure 1.1 Comparison Between Solids, Liquids and Gases

    For solid, imagine that the molecules can be fictitiouslylinked to each other with springs.

    (a) Solid (b) Liquid (c) Gas

    k

    kk

    k

    Free surface

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    Shear stress in moving fluid

    If fluid is in motion, shear stress are developed if theparticles of the fluid move relative to each other. Adjacentparticles have different velocities, causing the shape of thefluid to become distorted

    On the other hand, the velocity of the fluid is the same atevery point, no shear stress will be produced, the fluidparticles are at rest relative to each other.

    Moving plate Shear force

    Fluid particles New particle position

    Fixed surface

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    Differences between liquid and gases

    Liquid Gases

    Difficult to compress and often

    regarded as incompressible

    Easily to compress changes of volume

    is large, cannot normally be neglected

    and are related to temperature

    Occupies a fixed volume and will

    take the shape of the container

    No fixed volume, it changes volume to

    expand to fill the containing vessels

    A free surface is formed if the

    volume of container is greater

    than the liquid.

    Completely fill the vessel so that no free

    surface is formed.

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    Example:

    AirWaterOilGasolineAlcoholKeroseneBenzene

    Glycerine

    Fluid Newtons lawof viscosity

    Newtonian fluidsobey refer

    Newtons law of viscosity is given by;

    dy

    du (1.1)

    The viscosity is a function only of the condition of the fluid, particularly itstemperature.

    The magnitude of the velocity gradient (du/dy) has no effect on the magnitude of.

    = shear stress = viscosity of fluiddu/dy = shear rate, rate of strain or velocity gradient

    Newtonian and Non-Newtonian Fluid

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    Fluid Newtons lawof viscosity

    Non- Newtonianfluids

    Do not obey

    The viscosity of the non-Newtonian fluid is dependent on thevelocity gradient as well as the condition of the fluid.

    Newtonian Fluids a linear relationship between shear stress and the velocity gradient (rate

    of shear), the slope is constant the viscosity is constant

    non-Newtonian fluids slope of the curves for non-Newtonian fluids varies

    Newtonian and Non-Newtonian Fluid

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    Figure 1.1

    Shear stress vs.

    velocity gradient

    Bingham plastic : resist a small shear stress but flow easily under large shear

    stresses, e.g. sewage sludge, toothpaste, and jellies.Pseudo plastic : most non-Newtonian fluids fall under this group. Viscosity

    decreases with increasing velocity gradient, e.g. colloidal

    substances like clay, milk, and cement.

    Dilatants : viscosity decreases with increasing velocity gradient, e.g.

    quicksand.

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    1.2 Units and Dimensions

    Theprimary quantities which are also referred to as basicdimensions, such as L for length, T for time, M for mass andQfor temperature.

    This dimension system is known as the MLTsystem where it

    can be used to provide qualitative description for secondaryquantities, or derived dimensions, such as area (L), velocity(LT-1) and density (ML-3).

    In some countries, the FLT system is also used, where thequantity F stands for force.

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    1.2 Units and Dimensions

    An example is a kinematic equation for the velocity Vof auniformly accelerated body,

    V = V0 + at

    where V0

    is the initial velocity, a the acceleration and t thetime interval. In terms for dimensions of the equation, wecan expand that

    LT-1 = LT-1 + LT-2 T

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    Example

    The free vibration of a particle can be simulated by the

    following differential equation:

    where m is mass, u is velocity, t is time andxis

    displacement. Determine the dimension for the stiffness

    variable k.

    0 kxdt

    du

    m

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    Example

    By making the dimension of the first term equal to the

    second term:

    [m] = [k][x]

    Hence,

    [k] = =

    = MT-2

    [ u ]

    [ t]

    [ m ] [ u ]

    [ t] [x]

    M LT-1

    LT

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    Primary Units

    In fluid mechanics we are generally only interested in the top four units from this

    table.

    1.2 Engineering Units

    Quantity SI Unit

    Length Metre, m

    Mass Kilogram, kg

    Time Seconds, s

    Temperature Kelvin, K

    Current Ampere, A

    Luminosity Candela

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    Derived Units

    Quantity SI Unit

    velocity m/s -

    acceleration m/s2

    -force Newton (N) N = kg.m/s2

    energy (or work) Joule (J) J = N.m = kg.m2/s2

    power Watt (W) W = N.m/s = kg.m2/s3

    pressure (or stress) Pascal (P) P = N/m2 = kg/m/s2

    density kg/m3 -

    specific weight N/m3 = kg/m2/s2 N/m3 = kg/m2/s2

    relative density a ratio (no units) dimensionless

    viscosity N.s/m2 N.s/m2 = kg/m/s

    surface tension N/m N/m = kg/s2

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    Unit Cancellation Procedure

    1. Solve the equation algebraically for the desired terms.

    2. Decide on the proper units of the result.

    3. Substitute known values, including units.

    4. Cancel units that appear in both the numerator anddenominator of any term.

    5. Use correct conversion factors to eliminate unwanted unitsand obtain the proper units as described in Step 2.

    6. Perform the calculations.

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    Example

    Given m = 80 kg and a=10 m/s2. Find the force

    Solution

    F = ma

    F = 80 kg x 10 m/s2 = 800 kg.m/s2

    F= 800N

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    1.3 Fluid Properties

    DensityDensity of a fluid, ,

    Definition: mass per unit volume,

    slightly affected by changes in temperature andpressure.

    = mass/volume = m/ (1.2)

    Units: kg/m3

    Typical values:

    Water = 1000 kg/m3; Air = 1.23 kg/m3

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    Fluid Properties(Cont inue)

    Specific weightSpecific weight of a fluid, Definition:weight of the fluid per unit volume Arising from the existence of a gravitational force

    The relationshipand g can be found using the following:

    Since = m/therefore = g (1.3)

    Units:N/m3

    Typical values:Water = 9814 N/m3; Air = 12.07 N/m3

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    Specific gravity

    The specific gravity (or relative density) can be defined in two ways:

    Definition 1: A ratio of the density of a substance to the densityof water at standard temperature (4C) and

    atmospheric pressure, or

    Definition 2: A ratio of the specific weight of a substance to thespecific weight of water at standard temperature(4C) and atmospheric pressure.

    (1.4)

    Unit: dimensionless.

    Cw

    s

    Cw

    sSG

    44 @@

    Fluid Properties(Cont inue)

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    ExampleA reservoir of oil has a mass of 825 kg. The reservoir has a volumeof 0.917 m3. Compute the density, specific weight, and specificgravity of the oil.

    Solution:

    3/900917.0

    825mkg

    m

    volume

    massoil

    3

    oilm/N882981.9x900g

    mg

    volume

    weight

    9.0998

    900

    @

    STPw

    oil

    oilSG

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    Viscosity

    Viscosity,, is the property of a fluid, due to cohesion andinteraction between molecules, which offers resistance to sheardeformation.

    Different fluids deform at different rates under the same shearstress. The ease with which a fluid pours is an indication of itsviscosity. Fluid with a high viscosity such as syrup deforms moreslowly than fluid with a low viscosity such as water. The viscosity isalso known as dynamic viscosity.

    Units: N.s/m2 or kg/m/s

    Typical values:

    Water = 1.14x10-3 kg/m/s; Air = 1.78x10-5 kg/m/s

    Fluid Properties(Cont inue)

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    Kinematic viscosity, Definition: is the ratio of the viscosity to the density;

    will be found to be important in cases in which significant

    viscous and gravitational forces exist.

    Units: m2/s

    Typical values:

    Water = 1.14x10-6 m2/s; Air = 1.46x10-5 m2/s;

    In general,

    viscosity of liquids with temperature, whereas

    viscosity of gases with in temperature.

    /

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    Bulk Modulus

    All fluids are compressible under the application of an externalforce and when the force is removed they expand back to theiroriginal volume.

    The compressibility of a fluid is expressed by its bulk modulus ofelasticity, K, which describes the variation of volume with change

    of pressure, i.e.

    Thus, if the pressure intensity of a volume of fluid,, is increasedbyp and the volume is changed by, then

    Typical values:Water = 2.05x109 N/m2; Oil = 1.62x109 N/m2

    strainvolumetric

    pressureinchangeK

    /

    pK

    pK

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    Vapor Pressure

    A liquid in a closed container is subjected to a partialvapor pressure in the space above the liquid due to theescaping molecules from the surface;

    It reaches a stage of equilibrium when this pressure

    reaches saturated vapor pressure. Since this depends upon molecular activity, which is a

    function of temperature, the vapor pressure of a fluidalso depends on its temperature and increases with it.

    If the pressure above a liquid reaches the vapor pressureof the liquid, boiling occurs; for example if the pressureis reduced sufficiently boiling may occur at roomtemperature.

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    Engineering significance of vapor pressure

    In a closed hydraulic system, Ex. in pipelines or pumps, water vaporizesrapidly in regions where the pressure drops below the vapor pressure.

    There will be local boiling and a cloud of vapor bubbles will form.

    This phenomenon is known as cavitations, and can cause seriousproblems, since the flow of fluid can sweep this cloud of bubbles on

    into an area of higher pressure where the bubbles will collapsesuddenly.

    If this should occur in contact with a solid surface, very seriousdamage can result due to the very large force with which the liquid hitsthe surface.

    Cavitationscan affect the performance of hydraulic machinery such aspumps, turbines and propellers, and the impact of collapsing bubbles

    can cause local erosion of metal surface.

    Cavitations in a closed hydraulic system can be avoided bymaintaining the pressure above the vapor pressure everywhere in thesystem.

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    Surface Tension

    Liquids possess the properties of cohesion and adhesion due to molecular attraction. Due to the property of cohesion, liquids can resist small tensile forces at the

    interface between the liquid and air, known as surface tension, .

    Surface tension is defined asforce per unit length, and its unit is N/m.

    The reason for the existence of this force arises from intermolecular attraction. Inthe body of the liquid (Fig. 1.2a), a molecule is surrounded by other molecules andintermolecular forces are symmetrical and in equilibrium.

    At the surface of the liquid (Fig. 1.2b), a molecule has this force acting only through180.

    This imbalance forces means that the molecules at the surface tend to be drawntogether, and they act rather like a very thin membrane under tension.

    This causes a slight deformation at the surface of the liquid (the meniscus effect).

    Figure 1.2: Surface Tension

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    A steel needle floating on water, the spherical shape ofdewdrops, and the rise or fall of liquid in capillary tubes isthe results of the surface tension.

    Surface tension is usually very small compared with otherforces in fluid flows (e.g. surface tension for water at 20C is0.0728 N/m).

    Surface tension,, increases the pressure within a droplet ofliquid. The internal pressure, P, balancing the surfacetensional force of a spherical droplet of radius r, is given by

    r

    2P

    (1.7)

    2R = pR2

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    Capillarity

    The surface tension leads to the phenomenon known as capillarity

    where a column of liquid in a tube is supported in the absence ofan externally applied pressure.

    Rise or fall of a liquid in a capillary tube is caused by surfacetension and depends on the relative magnitude of cohesion of theliquid and the adhesion of the liquid to the walls of the containingvessels.

    Liquid rise in tubes if they wet a surface (adhesion > cohesion),such as water, and fall in tubes that do not wet (cohesion >adhesion), such as mercury.

    Capillarity is important when using tubes smaller than 10 mm (3/8in.).

    For tube larger than 12 mm (1/2 in.) capillarity effects arenegligible.

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    Figure 1.3

    Capillary actions

    r

    cos2h

    (1.8)

    whereh= height of capillary rise (or depression)= surface tension= wetting (contact) angle= specific weight of liquidr= radius of tube

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    A reservoir of oil has a mass of 825 kg. The reservoir has avolume of 0.917 m3. Compute the density, specific weight,and specific gravity of the oil.

    Solution:

    3/900917.0

    825mkg

    m

    volume

    massoil

    3

    oil m/N882981.9x900g

    mg

    volume

    weight

    9.01000

    900SG

    C4@w

    oiloil

    Example

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    Water has a surface tension of 0.4 N/m. In a 3-mm diametervertical tube, if the liquid rises 6 mm above the liquid outside thetube, calculate the wetting angle.

    SolutionCapillary rise due to surface tension is given by;

    r

    cos2h

    = 83.7

    4.0x2

    006.0x0015.0x9810

    2

    rhcos

    Example

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    This chapter has summarized on the aspect below:

    Understanding of a fluid

    The differences between the behaviours of liquid and gases

    Newtonian and non-Newtonian fluid were identified Engineering unit of SI unit were discussed

    Fluid properties of density, specific weight, specificgravity, viscosity and bulk modulus were outlined andtaken up.

    Discussion on the vapor pressure of the liquid

    Surface tension

    Capillarity phenomena

    Summary