c. bernoullis theorem demonstration

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KNC 1101: CHEMICAL ENGINEERING LABORATORY I LABORATORY MANUAL EXPERIMENT C Bernoulli’s Theorem Demonstration Faculty of Engineering Department of Chemical Engineering & Energy Sustainability Semester 2_ 2013/2014

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  • KNC 1101: CHEMICAL ENGINEERING LABORATORY I

    LABORATORY MANUAL

    EXPERIMENT C

    Bernoullis Theorem

    Demonstration

    Faculty of Engineering

    Department of Chemical Engineering & Energy Sustainability

    Semester 2_ 2013/2014

  • KNC 1101: Chemical Engineering Laboratory I 2013/2014

    Prepared by Mohamed Afizal Mohamed Amin 2

    INTRODUCTION

    Bernoulli's law states that if a non-viscous fluid is flowing along a pipe of varying

    cross section, then the pressure is lower at constrictions where the velocity is

    higher, and the pressure is higher where the pipe opens out and the fluid

    stagnate. Many people find this situation paradoxical when they first encounter

    it (higher velocity, lower pressure). This is expressed with the following equation:

    Constant *hzg

    v

    g

    p

    2

    2

    Where,

    p = Fluid static pressure at the cross section

    = Density of the flowing fluid

    g = Acceleration due to gravity

    v = Mean velocity of fluid flow at the cross section

    z = Elevation head of the center at the cross section with respect

    to a datum

    h* = Total (stagnation) head

    The terms on the left-hand-side of the above equation represent the pressure

    head (h), velocity head (hv ), and elevation head (z), respectively. The sum of

    these terms is known as the total head (h*). According to the Bernoullis theorem

    of fluid flow through a pipe, the total head h* at any cross section is constant. In

    a real flow due to friction and other imperfections, as well as measurement

    uncertainties, the results will deviate from the theoretical ones.

    In this experimental setup, the centerline of all the cross sections are considering

    lie on the same horizontal plane (which we may choose as the datum, z = 0, and

    thus, all the z values are zeros so that the above equation reduces to:

    Constant *hg

    v

    g

    p

    2

    2

    This represents the total head at a cross section

  • KNC 1101: Chemical Engineering Laboratory I 2013/2014

    Prepared by Mohamed Afizal Mohamed Amin 3

    Objective of the Experiment

    1) To demonstrate Bernoullis Theorem

    Prior Knowledge

    1) Fluid dynamics (fluid in motion)

    2) Bernoullis law : Venturi Meter

    Materials and Equipment

    1) Bernoullis Theorem Demonstration Unit (Model: FM24)

    2) Tap water

    Figure 1: Parts Identification Diagram

    1. Manometer Tubes

    2. Test Section

    3. Water Inlet

    4. Unions

    5. Air Bleed Screw

    6. Flow Control Valve

    7. Gland Nut

    8. Hypodermic Probe

    9. Adjustable Feet

    5

    1

    2

    3

    4

    6

    7

    8

    9

  • KNC 1101: Chemical Engineering Laboratory I 2013/2014

    Prepared by Mohamed Afizal Mohamed Amin 4

    Gland Nut

    Hypodermic probe

    Adjustable feetTest sectionWater inlet

    Unions

    Manometer tubes

    Air bleed screw

    Figure 2: Front View of Bernoullis Theorem Demonstration Unit

    Additional tapping

    Flow control valve

    Water outlet

    Figure 3: Top View of Bernoullis Theorem Demonstration Unit

    The unit consists of the followings:

    a) Venturi

    The venturi meter is made of transparent acrylic with the following

    specifications:

    Throat diameter : 16 mm

    Upstream Diameter : 26 mm

    Designed Flow Rate : 20 LPM

    b) Manometer

    There are eight manometer tubes; each length 320 mm, for static

    pressure and total head measuring along the venturi meter.

    The manometer tubes are connected to an air bleed screw for air

    release as well as tubes pressurization.

  • KNC 1101: Chemical Engineering Laboratory I 2013/2014

    Prepared by Mohamed Afizal Mohamed Amin 5

    c) Baseboard

    The baseboard is epoxy coated and designed with 4 height adjustable

    stands to level the venturi meter.

    d) Discharge Valve

    One discharge valve is installed at the venturi discharge section for flow

    rate control.

    e) Connections

    Hose Connections are installed at both inlet and outlet.

    f) Hydraulic Bench

    Sump tank : 120 litres

    Volumetric tank : 100 litres

    Centrifugal pump : 0.37 kW, 50 LPM

    METHODOLOGY

    A. General Start-up Procedures

    The Bernoullis Theorem Demonstration (Model: FM 24) is supplied ready for

    use and only requires connection to the Hydraulic Bench (Model: FM 110) as

    follows:

    1. Ensure that the clear acrylic test section is installed with the converging

    section upstream. Also check that the unions are tighten (hand tight only).

    If necessary to dismantle the test section then the total pressure probe

    must be withdrawn fully (but not pulled out of its guide in the

    downstream coupling) before releasing the couplings.

    2. Locate the apparatus on the flat top of the bench.

    3. Attach a spirit level to baseboard and level the unit on top of the bench by

    adjusting the feet.

    4. Fill water into the volumetric tank of the hydraulic bench until

    approximately 90% full.

    5. Connect the flexible inlet tube using the quick release coupling in the bed

    of the channel.

    6. Connect a flexible hose to the outlet and make sure that it is directed into

    the channel.

    7. Partially open the outlet flow control valve at the Bernoullis Theorem Demonstration unit.

    8. Fully close the bench flow control valve, V1 then switch on the pump.

    9. Gradually open V1 and allow the piping to fill with water until all air has

    been expelled from the system.

    10. Also check for Trapped Bubbles in the glass tube or plastic transfer tube. You would need to remove them from the system for better accuracy.

  • KNC 1101: Chemical Engineering Laboratory I 2013/2014

    Prepared by Mohamed Afizal Mohamed Amin 6

    Note:

    To remove air bubbles, you will have to bleed the air out as follow:

    a. Get a pen or screw driver to press the air bleed valve at the top right

    side of manometer board.

    b. Press air bleed valve lightly to allow fluid and trapped air to escape

    out. (Take care or you will wet yourself or the premise).

    Allow sufficient time for bleeding until all bubbles escape.

    11. At this point, you will see water flowing into the venturi and discharge

    into the collection tank of hydraulic bench.

    12. Proceed to increase the water flowrate. When the flow in the pipe is steady

    and there is no trapped bubble, start to close the discharge valve to reduce

    the flow to the maximum measurable flow rate.

    13. You will see that water level in the manometer tubes will begin to display

    different level of water heights. If the water level in the manometer board

    is too low where it is out of visible point, open V1 to increase the static

    pressure. If the water level is too high, open the outlet control valve to

    lower the static pressure.

    Note: The water level can be adjusted facilitate by the air bleed valve.

    14. Adjust V1 and outlet control valve to obtain a flow through the test section

    and observe that the static pressure profile along the converging and

    diverging sections is indicated on its respective manometers. The total

    head pressure along the venture tube can be measured by traversing the

    hypodermic tube.

    Note:

    The manometer tube connected to the tapping adjacent to the outlet flow

    control valve is used as a datum when setting up equivalent conditions for

    flow through test section.

    15. The actual flow of water can be measured using the volumetric tank with

    a stop watch.

    B. Experiment

    1. Perform the General Start-up Procedures in Section A.

    2. Check that all manometer tubings are properly connected to the

    corresponding pressure taps and are air-bubble free.

    3. Adjust the discharge valve to a high measurable flow rate.

    4. After the level stabilizes, measure the water flow rate using volumetric

    method.

    5. Gently slide the hypodermic tube (total head measuring) connected to

    manometer #G, so that its end reaches the cross section of the Venturi

    tube at #A. Wait for some time and note down the readings from

    manometer #G and #A. The reading shown by manometer #G is the sum of

  • KNC 1101: Chemical Engineering Laboratory I 2013/2014

    Prepared by Mohamed Afizal Mohamed Amin 7

    the static head and velocity heads, i.e. the total (or stagnation) head (h*),

    because the hypodermic tube is held against the flow of fluid forcing it to a

    stop (zero velocity). The reading in manometer #A measures just the

    pressure head (hi) because it is connected to the Venturi tube pressure tap,

    which does not obstruct the flow, thus measuring the flow static pressure.

    6. Repeat step 5 for other cross sections (#B, #C, #D, #E and #F).

    7. Repeat step 3 to 6 with three other decreasing flow rates by regulating the

    venturi discharge valve.

    8. Calculate the velocity, ViB using the Bernoullis equation where;

    )(2 8 ii hhgV

    9. Calculate the velocity, ViC using the continuity equation where

    Vi_Con = Qav / Ai

    10. Determined the difference between two calculated velocities.

    C. General Shut-down Procedures

    1. Close water supply valve and venturi discharge valve.

    2. Turn off the water supply pump.

    3. Drain off water from the unit when not in use.

    RESULTS AND DISCUSSION

    Cross Section

    Using Bernoulli Equation Using Continuity Equation Difference

    h*=hG

    (mm)

    hi

    (mm)

    ViB =

    [2*g*(h* - hi )]

    (m/s)

    Ai =

    Di2 / 4

    (m2)

    ViC =

    Qav / Ai

    (m/s)

    ViB-ViC

    (m/s)

    A

    B

    C

    D

    E

    F

    Additional Information:

    Throat Diameter, D3 (mm) = 16.0

    Inlet Diameter, D3 (mm) = 26.0

    Throat Area, At (m2) = 2.011 x 10-4

    Inlet Area, Ai (m2) = 5.309 x 10-4

    g (m/s2) = 9.81

    (kg/m3) = 1000