MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 5: EQUATIONS OF MOTION OF VISCOUS FLOWS - PowerPoint PPT Presentation

1 / 27
About This Presentation
Title:

MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 5: EQUATIONS OF MOTION OF VISCOUS FLOWS

Description:

MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 5: EQUATIONS OF MOTION OF VISCOUS FLOWS Instructor: Professor C. T. HSU 5.1 Flow Fields and Gradients The continuum ... – PowerPoint PPT presentation

Number of Views:236
Avg rating:3.0/5.0
Slides: 28
Provided by: Mech47
Category:

less

Transcript and Presenter's Notes

Title: MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 5: EQUATIONS OF MOTION OF VISCOUS FLOWS


1
MECH 221 FLUID MECHANICS(Fall 06/07)Chapter 5
EQUATIONS OF MOTION OF VISCOUS FLOWS
  • Instructor Professor C. T. HSU

2
5.1 Flow Fields and Gradients
  • The continuum assumption allows the treatment of
    fluid properties as fields, scalar vector or
    tensor, which are function of space (r) and time
    (t)
  • Scalar fields density
  • pressure
  • temperature
  • Vector fields velocity
  • vorticity
  • Tensor fields total stress
  • viscous stress
  • strain rate

3
5.1 Flow Fields and Gradients
  • Total change of a scalar field, , due to change
    in space only
  • For the position vector given by
    , the change in is only cause by the
    change in r described by

4
5.1 Flow Fields and Gradients
  • The total derivative is then given by
  • where
  • is the gradient of . The gradient is a
    vector along the direction where the magnitude of
    has a maximum.

5
5.1 Flow Fields and Gradients
  • Consider P Q to be 2 points on a surface where
    . These points are chosen so
    that Q is a small distance from P. Then dr is
    tangential to the surface.
  • Now lets move from P to Q. The change in
  • is then given by,
  • since the 2 points are on the surface with the
    same C.

6
5.1 Flow Fields and Gradients
  • Therefore, is perpendicular to dr from P.
  • Since dr may be in any direction from P, as long
    as it is tangential to the surface , we
    conclude that has to be in normal to the
    surface .

7
5.1 Flow Fields and Gradients
  • Example
  • For unsteady flows where may change with
    time, recall that the total derivative is

8
5.2 Conservation of Mass
  • We recall in Chapter 3 that the conservation of
    mass can be understood more easily in the
    Lagrangian frame. It states that the total mass m
    in control volume V has to be conserved if the
    control volume deformed with the flow to confine
    the same fluid particles.

9
5.2 Conservation of Mass
  • We now extend further to include the cases when
    there is a mass source in the control volume. If
  • represents the rate of mass source per unit
    volume, the mass balance then read

10
5.2 Conservation of Mass
  • Above equation is the integral form of the mass
    conservation in the Eulerian description. Note
    that the control volume V can be either fixed or
    varying.
  • The first term on the left hand side is the
    contribution caused by the density change in V
    and the second term caused by the mass flux enter
    the surface that define the control volume. The
    term on the right hand side then represents the
    rate of mass created or annihilated in V

11
5.2 Conservation of Mass
  • To obtain the differential form, we now employ
    the divergence theorem to the second term on the
    left of conservation of mass equation to give

12
5.2 Conservation of Mass
  • Again, as V(t)?0 the integrand is independent of
    V and therefore,
  • which is the differential form of equation for
    mass conservation.
  • Note that in the above equation, all terms are in
    rate of mass change per unit volume.

13
5.2 Conservation of Mass
  • For flow fields without mass sources, the
    integral and differential forms of conservation
    of mass equation reduce to
  • and
  • respectively, which were given in Chapter 3

14
5.2.1 Derivation of the Differential Equation
in Eulerian frame and Cartesian Coordinate
  • Consider the fixed control volume as shown below

15
5.2.1 Derivation of the Differential Equation
in Eulerian frame and Cartesian Coordinate
  • Net mass leaving the control volume/time

16
5.2.1 Derivation of the Differential Equation
in Eulerian frame and Cartesian Coordinate
  • Net mass increase in the control volume/time
  • Conservation of mass states that the net mass
    entering the control volume/unit time is equal to
    the rate of increase of mass in the differential
    control volume

17
5.2.1 Derivation of the Differential Equation
in Eulerian frame and Cartesian Coordinate
18
5.2.2 Special Cases
  • Steady flow,
  • Incompressible flow,
  • Cartesian
  • Polar
  • Spherical
  • 2-D flow,

19
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • In Chapter 3, for inviscid flows, only pressure
    forces act on the control volume V since the
    viscous forces (stress) were neglected and the
    resultant equations are the Eulers equations.
    The equations for conservation of momentum for
    inviscid flows were derived based on Newtons
    second law in the Lagrangian form.

20
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • Here we should include the viscous stresses to
    derive the momentum conservation equations.
  • With the viscous stress, the total stress on the
    fluid is the sum of pressure stress(
    , here the negative sign implies that tension is
    positive) and viscous stress ( ), and is
    described by the stress tensor given by

21
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • Here, we generalize the body force (b) due to all
    types of far field forces. They may include those
    due to gravity , electromagnetic force,
    etc.
  • As a result, the total force on the control
    volume in a Lagrangian frame is given by

22
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • The Newtons second law then is stated as
  • Hence, we have

23
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • By the substitution of the total stress into the
    above equation, we have
  • which is integral form of the momentum
    equation.

24
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • For the differential form, we now apply the
    divergence theorem to the surface integrals to
    reach
  • Hence, V?0, the integrands are independent of V.
    Therefore,
  • which are the momentum equations in differential
    form for viscous flows. These equations are also
    named as the Navier-Stokes equations.

25
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • For the incompressible fluids where
    constant.
  • If the variation in viscosity is negligible
    (Newtonian fluids), the continuity equation
    becomes , then the shear stress tensor
    reduces to .

26
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • The substitution of the viscous stress into the
    momentum equations leads to
  • where is the Laplacian operator
    which in a Cartesian coordinate system reads

27
5.3 Conservation of Momentum (Navier-Stokes
Equations)
  • For inviscid flow where , the above
    equation reduces to the Eulers equation given in
    Chapter 3 where the body force is also taken the
    form due to gravity.
Write a Comment
User Comments (0)
About PowerShow.com