FM230-Hydraulics Lab 2 2010 Small Rig ADL

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    Fluid Mechanics 230 Laboratory Session 2

    Faculty of Science & Engineering, Curtin University of Technology

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    Unit: Fluid Mechanics 230Activity type: LaboratoryTitle of Activity: (Lab-Experiments)Credit for Activity: (10% of Unit)Note for guidance: It is expected that an average student will take 5-6hours

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    Fluid Mechanics 230 Laboratory Session 2

    discussion ofresults

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    Marker: ____________________Date of Return:____________________LABORATORY NUMBER 2

    FLOW THROUGH PIPES1. Introduction:

    This experiment is designed to permit the study of flow in pipes, not only ineach of the laminar and turbulent regimes but also in the transitionalregime between laminar and turbulent flow. The pressure gradient in thepipe will be measured and the pipes friction factor evaluated for differentflow rates.

    2. Objectives

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    Fluid Mechanics 230 Laboratory Session 2

    Figure 1. Laboratory equipment for the study of flow through a pipe

    4. Procedure

    Refer to the equipment layout shown in Figures 5 and 6 in the Appendix.

    First check that the apparatus is leveled so that the manometers stand vertically. Because of the

    large range of head differences, the readings are taken in two sets: those for lower flow rates

    with the water manometer, and those for high flow rates using the mercury manometer. In total,

    take 30 eadi g t e the la i a t a iti al a d t b le t fl egi e a f ll

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    Fluid Mechanics 230 Laboratory Session 2

    Turn off the needle valve (to stop the flow) to check that mercury levels in the twobranches of the manometer are level.

    Use the needle valve to regulate the flow rate in the pipe. Small head difference should

    correspond to the transitional flow. It is advisable to overlap the first few mercurymanometer readings with those of water manometer readings in Section 4.1 above..

    Take the readings of mercury manometers h1 and h2.

    Calculate the flow rates in the same way that you did for water-manometer cases.

    5. Data Collection and Results

    5.1 Properties of water, mercury and pipe

    Density of water(kg/m3) 1,000

    Dynamic viscosity of water at 200C (N.s/m2) 1.002 10-3

    Diameter of pipe (mm) 3

    Length of pipe between piezometer tappings (mm) 524

    Roughness height of pipe wall material k (mm) 0 0015

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    Fluid Mechanics 230 Laboratory Session 2

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    Mercury Manometer Readings

    TestNo.

    Qty(ml)

    t

    (s)

    Flowrate

    (m3/s)

    V (m/s)

    h1(mm)

    h2(mm)

    Hydraulicgradient,

    i131415

    16171819202122

    2324252627282930

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    Fluid Mechanics 230 Laboratory Session 2

    161718

    19202122232425

    2627282930

    6.1 Analysis and Report

    For the analysis,

    1. Plot hydraulic gradient, i, against the mean velocity of the flow, V,

    and identif the flo speed regions of laminar and t rb lent flo

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    APPENDIX:Formulae and Figures 2-7

    A1. Useful formulae for the analysis of pipe flows

    The head loss due to friction can be calculated using Darcy-Weisbachequation:

    g

    V

    D

    Lfh

    L 2

    2

    = (Eq

    1)

    Hydraulic gradient

    Dg

    Vf

    L

    hi L

    2

    2

    == (Eq 2 )

    For Water manometer:

    L

    hhi

    )( 21 = (Eq 3 )

    where the units ofh1, h2and L are the same.

    For mercury manometer:hh

    i

    )15.13)(( 21

    (E 4)

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    2 L = Distance between two piezometer points

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    A2. Figures 2-7

    Figure 2. Typical laminar flow Figure 3. Typical turbulent flow

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    Fi 5 Di ti t f th t (S ll i )

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    Air valve

    Mercury U-tube

    Water manometer

    Testing pipe

    Air valve

    Mercury U-tube

    Water manometer

    Testing pipe

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    Fluid Mechanics 230 Laboratory Session 2

    Fig. 7: Moody diagram

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