Pharos University - PowerPoint PPT Presentation

1 / 47
About This Presentation
Title:

Pharos University

Description:

Pharos University ME 259 Fluid Mechanics for Electrical Students Application of Bernoulli Equation * * Bernoulli Equation Consider steady flow along streamline s is ... – PowerPoint PPT presentation

Number of Views:119
Avg rating:3.0/5.0
Slides: 48
Provided by: alfa155
Category:

less

Transcript and Presenter's Notes

Title: Pharos University


1
  • Pharos University
  • ME 259 Fluid Mechanics for Electrical Students
  • Application of Bernoulli Equation

2
  • Eulers equation of motion
  • Bernoulli equation

3
INTRODUCTION
  • The three equations commonly used in fluid
    mechanics are
  • the mass, Bernoulli, and energy equations.
  • The mass equation is an expression of the
    conservation of mass principle.
  • The Bernoulli equation Conservation of kinetic,
    potential, and flow energies ( viscous forces are
    negligible.)

4
Fluid Motion
  • Two ways to describe fluid motion
  • Lagrangian
  • Follow particles around
  • Eularian
  • Watch fluid pass by a point or an entire region
  • Flow pattern
  • Streamlines velocity is tangent to them

5
STEADY AND UNSTEADY FLOW
  • Steady flow the flow in which conditions at any
    point do not change with time is called steady
    flow.
  • Then, etc.
  • Unsteady flow the flow in which conditions at
    any point change with time, is called unsteady
    flow.
  • Then, etc.

6
UNIFORM AND NON-UNIFORM
  • The flow in which the conditions at all points
    are the same at the same instant is uniform flow.
  • The flow in which the conditions vary from point
    to point at the
  • same instant is non-uniform flow.

7
ACCELERATION
  • Acceleration rate of change of velocity
  • Components
  • Normal changing direction
  • Tangential changing speed

8
ACCELERATION
  • Cartesian coordinates
  • In steady flow ?u/?t 0 , local acceleration is
    zero.
  • In unsteady flow ?u/?t ? 0 local acceleration
    Occurs.

9
Example
  • Valve at C is opened slowly
  • The flow at B is non uniform
  • The flow at A is uniform

10
Laminar vs Turbulent Flow
  • Turbulent
  • Laminar

11
Flow Rate
  • Volume rate of flow
  • Constant velocity over cross-section
  • Variable velocity
  • Mass flow rate

12
Flow Rate
  • Only x-direction component of velocity (u)
    contributes to flow through cross-section

13
CV Inflow Outflow
  • Area vector always points outward from CV

14
Examples
  • Discharge in a 25-cm pipe is 0.03 m3/s. What is
    the average velocity?
  • A pipe whose diameter is 8 cm transports air with
    a temp. of 20oC and pressure of 200 kPa abs. At
    20 m/s. What is the mass flow rate?

15
Example The velocity distribution in a circular
duct is , where r is
the radial location in the duct, R is the duct
radius, and Vo is the velocity on the axis. Find
the ratio of the mean velocity to the velocity on
the axis.
  • Find

16
Example Air (? 1.2 kg/m3) enters the duct
shown
  • Find
  • V/10y/.5 ? V20y
  • dA1dy

17
Example In this flow passage the discharge is
varying with time according to the following
expression . At time t0.5
s, it is known that at section A-A the velocity
gradient in the S direction is 2m/s per meter.
Given that Qo, Q1, and to are constants with
values of 0.985 m3/s, 0.5 m3/s, and 1 s,
respectively, and assuming that one-dimensional
flow, answer the following questions for time
t0.5 s.a. What is the velocity a A-A?b. What
is the local acceleration at A-A?c. What is the
convective acceleration at A-A?
18
Example
19
Systems, Control Volume, and Control Surface
  • System (sys)
  • A fluid system contains the
  • same fluid particles.
  • Mass does not cross the
  • system boundaries.
  • Thus the mass of the system
  • is constant.

Control Volume (C.V) A control volume
is a selected volumetric region in space. Its
shape and position may change with time.(Open
System)
Control Surface (C.S) The surface
enclosing the control volume is called the
control surface.
20
Systems, Control Volume, and Control Surface
(continued )
  • Consider the tank shown, assume
  • the control volume is defined by the tank walls
    and the top of the liquid.
  • The control surface that encloses the control
    volume is designated by the dashed line.
  • The liquid in the tank at time t is elected as
    the system and is indicated by the solid line.
  • At this instant in time, the system completely
    occupies the control volume and is contained by
    the control surface. Thus, at this time

During the same period some liquid has entered
the control volume from the left, the amount
being
After a time some liquid has flowed out of
the control volume to the right. The amount that
flowed out is
21
Systems, Control Volume, and Control Surface
(continued )
  • Now the system has been deformed as shown in Fig.
    (b).
  • Part of the system is the liquid that has flowed
    out across the control surface.
  • The system remaining in the control volume has
    been deformed by the mass that has flowed in
    across the control surface.
  • Also, the height of the control volume has
    changed to accommodate the net flow into the
    tank.
  • The mass of the system at time t ?t can be
    determined by taking the mass in the control
    volume, subtracting the mass that entered, and
    adding the mass that left.

Subtracting (1) from (2), we have
Dividing by ?t and taking the limit as ?t ?0
yields
The equation relates the rate of change of the
mass of the system to the rate of change of mass
in the control volume plus the net outflow
(efflux) across the control surface
22
Systems, Control Volume, and Control Surface
(continued )
  • By definition, the mass of the system is constant
    so

  • Lagrangian statement
  • And Eq. (3) becomes
  • The corresponding Eulerian statement and can be
    written as

This equation states that there is an increasing
mass in the control volume if there is a net mass
influx through the control surface and decreasing
mass if there is a net mass efflux. This is
identified as the continuity equation.
23
Systems
  • Laws of Mechanics
  • Written for systems
  • System arbitrary quantity of mass of fixed
    identity
  • Fixed quantity of mass, m
  • Conservation of Mass
  • Mass is conserved and does not change
  • Momentum
  • If surroundings exert force on system, mass will
    accelerate
  • Energy
  • If heat is added to system or work is done by
    system, energy will change

24
Control Volumes
  • Solid Mechanics
  • Follow the system, determine what happens to it
  • Fluid Mechanics
  • Consider the behavior in a specific region or
    Control Volume
  • Convert System approach to CV approach
  • Look at specific regions, rather than specific
    masses
  • Reynolds Transport Theorem
  • Relates time derivative of system properties to
    rate of change of property in CV

25
CV Inflow Outflow
26
Continuity Equation
  • In the case of the continuity equation, the
    extensive property in the control volume equation
    is the mass of the system, Msys, and the
    corresponding intensive variable, b, is the mass
    per unit mass, or
  • Substituting b equal to unity in the control
    volume equation yields the general form of the
    continuity equation.
  • This is sometimes called the integral form of the
    continuity equation.

27
Continuity Equation
  • The term on the left is the rate of change of the
    mass of the system. However, by definition, the
    mass of a system is constant. Therefore the
    left-hand side of the equation is zero, and the
    equation can be written as
  • This is the general form of the continuity
    equation. It states that the net rate of the
    outflow of mass from the control volume is equal
    to the rate of decrease of mass within the
    control volume.
  • The continuity equation involving flow streams
    having a uniform velocity across the flow section
    is given as

28
Example at a certain time rate of rising is 0.1
cm/s
  • Continuity equation

29
Example Both pistons are moving to the left, but
piston A has a speed twice as great as that of
piston B. Then the water level in the tank is a)
rising, b) not moving up or down, c) falling.
  • Select a CV that moves up and down with the water
    surface
  • Continuity Equation

h
30
Euler Equation
  • Fluid element accelerating in l direction acted
    on by pressure and weight forces only (no
    friction)
  • Newtons 2nd Law

31
Example 1
  • Given Steady flow. Liquid is decelerating at a
    rate of 0.3g.
  • Find Pressure gradient in flow direction in
    terms of specific weight.

32
Example 2
  • Given g 10 kN/m3, pB-pA12 kPa.
  • Find Direction of fluid acceleration.

33
Example 3
  • Given Steady flow. Velocity varies linearly
    with distance through the nozzle.
  • Find Pressure gradient ½-way through the nozzle

V1/2(8030)/2 ft/s 55 ft/s
dV/dx (80-30) ft/s /1 ft 50 ft/s/ft
34
Bernoulli Equation
  • Consider steady flow along streamline
  • s is along streamline, and t is tangent to
    streamline

35
An alternative form of the Bernoulli equation is
expressed in terms of heads as The sum of the
pressure, velocity, and elevation heads is
constant along a streamline.
The Bernoulli equation states that the sum of the
kinetic, potential, and flow energies of a fluid
particle is constant along a streamline during
steady flow.
36
Example 4
  • Given Velocity in outlet pipe from reservoir is
    6 m/s and h 15 m.
  • Find Pressure at A.
  • Solution Bernoulli equation

Point 1
Point A
37
Example 5
  • Given D30 in, d1 in, h4 ft
  • Find VA
  • Solution Bernoulli equation

38
Static, Stagnation, Dynamic, and Total Pressure
Bernoulli Equation
Hydrostatic Pressure
Dynamic Pressure
Static Pressure
Static Pressure moves along the fluid static
to the motion.
Dynamic Pressure due to the mean flow going to
forced stagnation.
Hydrostatic Pressure potential energy due to
elevation changes.
Following a streamline
Follow a Streamline from point 1 to 2
0
0, no elevation
0, no elevation
Total Pressure Dynamic Pressure Static
Pressure
Note
H gt h
In this way we obtain a measurement of the
centerline flow with piezometer tube.
39
  • Bernoulli equation The sum of flow, kinetic, and
    potential energies of a fluid particle along a
    streamline is constant.
  • Each term in this equation has pressure units,
    and thus each term represents Energy per unit
    volune
  • P is the static pressure.
  • ?V2/2 is the dynamic pressure.
  • ? gz is the hydrostatic pressure
  • The sum of the static, dynamic, and hydrostatic
    pressures is called the total pressure. Bernoulli
    equation states that the total pressure along a
    streamline is constant.
  • The sum of the static and dynamic pressures is
    called the stagnation pressure, and it is
    expressed as

40
  • The static, dynamic, and stagnation pressures are
    shown.
  • When static and stagnation pressures are measured
    at a specified location, the fluid velocity at
    that location can be calculated from

41
Stagnation Tube
42
Stagnation Tube in a Pipe
43
Pitot Tube
44
Example Venturi Tube
  • Given Water 20oC, V12 m/s, p150 kPa, D6 cm,
    d3 cm
  • Find p2 and p3
  • Solution Continuity Eq.
  • Bernoulli Eq.

Nozzle velocity increases, pressure decreases
Diffuser velocity decreases, pressure increases
Similarly for 2 ? 3, or 1 ? 3
Pressure drop is fully recovered, since we
assumed no frictional losses
Knowing the pressure drop 1 ? 2 and d/D, we can
calculate the velocity and flow rate
45
Ex
  • Given Velocity in circular duct 30 m/s, air
    density 1.2 kg/m3.
  • Find Pressure change between circular and
    square section.
  • Solution Continuity equation
  • Bernoulli equation

Air conditioning ( 60 oF)
46
Ex
  • Given r 1000 kg/m3 V1 30 m/s, and A2/A10.5,
    gm20000 N/m3
  • Find Dh
  • Solution Continuity equation
  • Bernoulli equation

Heating ( 170 oF)
  • Manometer equation

47
Pitot Tube Application
Write a Comment
User Comments (0)
About PowerShow.com