Flow in Pipes - Fluids Mechanic

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    FC-CIV MECAFLUI:Fluid Mechanics

    Session 18:

    Flow in Pipes (Part I)

    Eusebio Ingol Blanco, Ph.D.

    Civil Engineering Program, San Ignacio de LoyolaUniversity

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    Objective

    Understand the laminar and turbulent flowin pipes.

    Calculate the major and minor losses

    associated with pipe flow in pipingnetworks

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    Motivation

    Internal flows through pipes, elbows, tees,

    valves, etc., as in this oil refinery, are found

    in nearly every industry.

    Water supply and sanitation

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    Introduction

    Liquid or gas flow through pipes or ducts is commonly

    used in heating and cooling applications and fluiddistribution network.

    The fluid in such applications is usually forced to flow by a

    fan or pump through a flow section.

    Particular attention to friction,which is related to thepressure drop and head loss.

    The pressure drop is then used to determine the pumping

    power requirement

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    Introduction

    Average velocity Vavgis defined as theaverage speed through a cross section. For

    fully developed laminar pipe flow, Vavgis half

    of the maximum velocity.

    The value of the average velocity Vavg at some

    streamwise cross-section is determined fromthe requirement that the conservation of mass

    principle be satisfied

    The average velocity

    for incompressible

    flow in a circular pipeof radiusR

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    Laminar and Turbulent Flow

    Laminar:Smooth streamlines and highlyordered motion.

    Turbulent:Velocity fluctuations and highly

    disordered motion.

    Transition:The flow fluctuates between

    laminar and turbulent flows.Most flows encountered in practice are

    turbulent.

    The behavior of colored fluid injected into theflow in laminar and turbulent flows in a pipe.

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    Reynolds Number

    The transition from laminar to turbulent flow depends on

    the geometry, surface roughness, flow velocity, surfacetemperature, and type of fluid.

    The flow regime depends mainly on the ratio of inertial

    forcesto viscous forces(Reynolds number).

    Critical Reynolds number, Recr: The Reynolds number at

    which the flow becomes turbulent.

    The value of the critical Reynolds number is different for

    different geometries and flow conditions.

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    Reynolds Number

    For flow through noncircular

    pipes, the Reynolds number is

    based on the hydraulic diameter

    For flow in a circular pipe:

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    The Entrance RegionVelocity boundary layer:The region of the flow in which the effects

    of the viscous shearing forces caused by fluid viscosity are felt.

    Boundary layer region:The viscous effects and the velocity changes

    are significant.

    Irrotational (core) flow region:The frictional effects are negligible

    and the velocity remains essentially constant in the radial direction.

    The development of the velocity boundary layer in a pipe..

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    Pressure and wall shear stress

    The variation of wall shear stress in the flow direction for flow in a pipe

    from the entrance region into the fully developed region.

    The pressure drop is higher in the entrance regions of a pipe,

    and the effect of the entrance region is always to increase the

    average friction factor for the entire pipe.

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    Entry Length

    The hydrodynamic entry length is usually taken to be the distance fromthe pipe entrance to where the wall shearstress (and thus the friction

    factor) reaches within about 2 percent of the fully developed value.

    hydrodynamic

    entry length for

    laminar flow

    hydrodynamic

    entry length for

    turbulent flow

    hydrodynamic entry

    length for turbulent flow,

    an approximation

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    Laminar Flow in PipesWe consider steady, laminar, incompressible flow of a fluid with constant properties in

    the fully developed region of a straight circular pipe.

    Free-body diagram of a ring-shaped

    differential fluid element of radius r,thickness dr, and length dx oriented coaxially

    with a horizontal pipe in fully developed

    laminar flow.

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    Laminar Flow in Pipes

    Boundary conditions

    Maximim velocity

    at centerline (r = 0)

    Velocity

    profile

    Average velocity

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    Pressure Drop and Head Loss

    A pressure drop due to viscous effects represents an irreversible pressure

    loss, and it is calledpressure loss PL.

    pressure loss for all

    types of fully developedinternal flows

    dynamic

    pressure

    Circular pipe, laminar

    DarcyWeisbach friction

    factor

    In laminar flow, the friction

    factor is a function of the

    Reynolds number only and is

    independent of the roughness of

    the pipe surface.

    The head loss represents theadditional height that the fluid

    needs to be raised by a pump in

    order to overcome the frictional

    losses in the pipe.

    Substituting this eq. into Vavg expression:, the pressure drop is expressed as:

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    Pressure Drop and Head Loss

    The relation for pressure loss (and head loss) is one of the most

    general relations in fluid mechanics, and it is valid for laminar

    or turbulent flows, circular or noncircular pipes, and pipes with

    smooth or rough surfaces.

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    Pressure Drop and Head Loss

    The required pumping power to overcome the pressure loss in determined :

    Horizontal pipe

    Poiseuilleslaw

    The pumping power requirement for a laminar flow

    piping system can be reduced by a factor of 16 by

    doubling the pipe diameter.

    For a specified flow rate, the pressure drop and thus the

    required pumping power is proportional to the length of

    the pipe and the viscosity of the fluid, but it is inversely

    proportional to the fourth power of the diameterof the

    pipe.

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    Pressure Drop and Head Loss

    The pressure drop P equals the pressure loss PLin the case of a

    horizontal pipe, but this is not the case for inclined pipes or pipeswith variable cross-sectional area.

    This can be demonstrated by writing the energy equation for steady,

    incompressible one-dimensional flow in terms of heads as

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    Effect of Gravity on Velocity and Flow Rate in

    Laminar Flow

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    Laminar Flow in no Circular Pipes

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    Example 8-1

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    Example 8-1

    Solution:

    E l 8 1

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    Example 8-1

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    Example 8-2

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    Example 8-2

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    Example 8-2

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    Problem 8-31

    Water at 10C ( = 999.7 kg/m3 and = 1.307 x

    (10)^-3 kg/m s) is flowing steadily in a 0.20-cm-diameter, 15-m-long pipe at an average velocity of 1.2

    m/s. Determine:

    (a) the pressure drop, (b) the head loss, and (c) the

    pumping power requirement to overcome this pressure

    drop.

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    Problem 8-35

    The velocity profile in fully developed laminar flow

    in a circular pipe of inner radiusR = 2 cm, in m/s, isgivenby u(r) = 4(1 - r^2/R^2). Determine the

    average and maximum velocities in the pipe and the

    volume flow rate.

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    Problem 8-137E

    The velocity profile in a fully developed laminar flow of water

    at 40F in a 80-ft-long horizontal circular pipe, in ft/s, is given

    by u(r) = 0.8(1 625r^2), where r is the radial distance from the

    centerline of the pipe in ft. Determine:

    (a) the volume flow rate of water through the pipe, (b) the

    pressure drop across the pipe, and (c) the useful pumping

    power required to overcome this pressure drop.Assume that the pipe is inclined120 from the horizontal and

    the flow is uphill

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    Summary

    Flow in Pipes: Laminar and turbulentflows.

    The entrance region

    Laminar flow in pipes: Pressure drop and

    head loss Effect of gravity on velocity and flow

    rate

    Examples

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    Homework

    Study sections: 8-1, 8-2, 8-3, 8-4

    Homework 7 is going to be posted soon