Lecture02 Pipeflow Handout

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  • 7/26/2019 Lecture02 Pipeflow Handout

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    VE2400: Pipeflow - Lecture 2 09/04/200

    School of Civil EngineeringFACULTY OF ENGINEERING

    Fluid Flow in Pipes: Lecture 2

    Dr Andrew Sleigh

    Dr Ian Goodwill

    CIVE2400: Fluid Mechanics

    www.efm.leeds.ac.uk/CIVE/FluidsLevel2Fluid Mechanics: Pipe Flow Lecture 2

    Laminar

    Turbulent

    tw is almost impossible to measure

    2

    Pressure loss velocity relationship

    Fluid Mechanics: Pipe Flow Lecture 2 3

    Pressure loss in Laminar Flow

    In laminar flow it is possible to do theoretical

    analysis

    fluid particles move in straight lines

    Hagen-Poiseuille equation

    See level 1 fluids notes

    In terms of head loss

    2

    32

    d

    Lup

    2

    32

    gd

    Luhf

    ghp

    Fluid Mechanics: Pipe Flow Lecture 2

    Laminar flow example

    Determine the diameter of a pipe that is to convey 0.057 cumecs(m3/s) of oil a horizontal distance of 300m, if the pressure loss is not

    to be greater than 140 kN/m2.

    At the operating temperature the relative density of the oil is 0.9 and

    the dynamic viscosity is 1.43 Ns/m2.

    Flow velocity

    Hagen-Poiseuille

    Equate

    Check Re:

    2

    32

    d

    Lup

    222

    198.1030043.132

    1000140

    32d

    d

    L

    pdu

    222

    0726.0

    142.3

    4057.0

    4/ ddd

    Qu

    md

    dd

    29.0

    198.100726.0 2

    2

    86.00726.0

    2

    du

    157

    43.1

    29.086.010009.0Re

    ud

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    VE2400: Pipeflow - Lecture 2 09/04/200

    Fluid Mechanics: Pipe Flow Lecture 2 7

    Introduction of Friction factor

    To make use of this equation we must introduce

    afriction factor, f

    Equating and rearranging gives

    For a circular pipe,

    Giving

    2

    2uf

    tL

    ghm

    f

    t

    gm

    fLuhf

    2

    2

    4

    4/2 d

    d

    d

    P

    Am

    gd

    fLuhf

    2

    4 2

    Fluid Mechanics: Pipe Flow Lecture 2 8

    Darcy-Weisbach equation

    This is the Darcy-Weisbach equation

    Gives head loss due to friction in a circular pipe

    Often referred to as the Darcy equation

    In terms of Q

    In metric terms, g=9.81m2/s then

    Or

    ud

    AuQ4

    2

    gd

    fLuhf 2

    4 2

    2

    4

    d

    Qu

    5

    2

    2

    64

    dg

    fLQhf

    5

    2

    03.3 d

    fLQhf

    5

    2

    3d

    fLQhf

    Fluid Mechanics: Pipe Flow Lecture 2 9

    Darcy-Weisbach equation

    Have an equation to describe head-loss due to

    friction

    In terms of velocity u

    Of discharge Q

    And a friction factor, f

    The value of fis crucial to calculation of hf

    How do we find this?

    gd

    fLuhf

    2

    4 2

    5

    2

    3d

    fLQhf

    Fluid Mechanics: Pipe Flow Lecture 2 10

    f, American fand

    The fdescribed here is that common in UK

    (in text books and practice)

    In US (and some text book) fameri can

    = 4f,

    so

    To try and avoid confusion this is sometime

    written as ,

    BE CAREFULL!

    When using any book, look at the equation for hf

    gd

    fLuhf

    2

    4 2

    5

    2

    3d

    LQ

    hfl

    gd

    fLuhf

    2

    2

    Fluid Mechanics: Pipe Flow Lecture 2 11

    Pipeline Analysis

    Two reservoirs have a height diff erence 15m.

    They are connected by a pipeline 350 mm in diameter and 1000 m long with a friction

    factor fof 0.005. What is the flow in the pipe? (ignore all local losses)

    fexitLLentryLpumpBA hhhhhzz expansion

    15m

    L=1000m

    f =0.005

    d=0.35m

    slitressmQ

    QQ

    d

    fLQ

    /217/217.00473.0

    33.31735.03

    1000005.0

    315

    3

    2

    5

    2

    5

    2

    Fluid Mechanics: Pipe Flow Lecture 2 12

    What is f dependent on?

    The friction factor depends on many physical things

    hf

    L

    hfv2

    hf1/d

    hfdepends on surface roughness of pipes,

    k = size, k spacing, a = shape of particles

    hfdepends on fluid density and viscosity

    hf independent of pressure difference in pipe

    Cannot be constant!

    Can be written:

    a

    ,

    ',,d

    k

    d

    kudf

    fis complex !!

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    VE2400: Pipeflow - Lecture 2 09/04/200

    13

    Todays lecture:

    Friction Head loss, hf

    Laminar and Turbulent

    Darcy Weisbach Eqn

    In terms of Q

    First application of analysis of pipeline

    gd

    fLuhf

    2

    4 2

    5

    2

    3d

    fLQhf