Unit Operation 1

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    Masangkay, RamonNoche, SandyOrdillano, Graziela

    Pacia, Rose Mardie

    Mechanical energy lossesdue to straight and fittings

    in a viscous pipe flowsystem

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    Objectives:

    To measure the energy lossesthrough the straight pipe andfittings in a pipe flow system.

    To determine the relation of energylosses to the volumetric flow rate ina pipe flow system from actual data.

    To measure the performance of thefluid flow system in the lab bycomparing the design calculationswith the experimental data.

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    Introduction

    Pipe flows belong to a broader classof flows, called internal flows, wherethe fluid is completely bounded by

    solid surfaces.

    The nature of pipe flow isdependent on whether the flow is

    turbulent or laminar and this is due tothe differences in the nature of theshear stress in laminar and turbulentflows.

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    Consequently, the physicalproperties of the shear stress isdifferent for laminar than for turbulent

    flow. For laminar flow, it isindependent of density, thus, leavingthe viscosity as the very importantproperty; while for turbulent flow,density is an important property.

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    When a fluid flows through a pipe,there is a loss of pressure in the fluid,because energy is required to overcomethe viscous or frictional forces exerted

    by the walls of the pipe on the movingfluid. This can be seen in theMechanicalenergy balance equation:

    PE + KE+ P + F =Ws

    - P = F

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    In addition to the energy lost due tofrictional forces, the flow also losesenergy (or pressure) as it goes throughfittings, such as valves, elbows,

    contractions and expansions.

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    Equipments/ Materials:

    -Fluid flow unit

    -U-tube manometer

    -Water hose

    -Water

    -Ruler

    -Pail

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    Procedure

    Start Up

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    Experimental Procedure

    Close otherisolatingvalves

    Set the openingof the entryvalve to thedesignated

    degree

    Measure the steadystate static

    pressures using theU-tube manometer

    Locate thedesignatedhorizontal

    run

    Repeat steps 2 and3 for a different

    volumetric flow rate

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    Shut Down

    Open allisolatingvalves

    Slowly reducethe flow rateby reducing

    the degree ofopening of the

    entry valve

    Switch off thepump

    Open thedrain valve

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    Data and Results:

    Rm F26.67 2.61

    25.67 2.52

    23 2.25

    22 2.16

    20 1.96

    18.67 1.83

    17.67 1.73

    16 1.57

    15 1.47

    14.33 1.40

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    Sample Calculations:

    Experimental

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    Theoretical:

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    Flow rate (gal/hr) Velocity( m/s) f F

    800 1.715 0.0216 2.34

    750 1.608 0.022 2.14

    700 1.501 0.0223 1.89

    650 1.394 0.0227 1.66

    600 1.286 0.0231 1.44

    550 1.179 0.0236 1.236

    500 1.072 0.0241 1.044

    450 0.965 0.0248 0.870

    400 0.858 0.0255 0.707

    350 0.750 0.0263 0.557

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    References:

    Munson, B. R., Young, D.F., and Okiishi, T.H., Fundamentals of Fluid Mechanics, 3rded., John Wiley and Sons, Inc., 1998.

    http://www.eng.fsu.edu/~alvi/EML4304L/webpage/

    http://www.eng.fsu.edu/~alvi/EML4304L/webpage/experiment_5.htmhttp://www.eng.fsu.edu/~alvi/EML4304L/webpage/experiment_5.htm
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    ThankYou!