Fluid Mechanics Chapter 2 Part II - PowerPoint PPT Presentation

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Fluid Mechanics Chapter 2 Part II

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Title: Fluid Mechanics Chapter 2 Part II


1
Fluid Mechanics Chapter 2
  • Fundamental Concepts

2
Stress field
  • Each fluid particle experiences surface forces (
    pressure and Friction ) are generated in contact
    with other particles or solids
  • And body forces (gravity and electromegnatic)
  • Surface forces lead to stresses
  • Stresses in fluid are mostly generated by motion
  • The stress at any specified point may be
    expressed by nine components
  • The first subscript indicates surface
    perpendicular to a particular axis and second
    show direction

3
Concepts of Normal and shear stress
4
Notation for stresses
5
Viscosity
  • Where do stresses come from?
  • For a solid, stresses develop when the material
    is elastically deformed or strained
  • for a fluid, shear stresses arise due to viscous
    flow
  • Hence we say solids are elastic, and fluids are
    viscous
  • Many biological tissues are viscoelastic, meaning
    they combine features of a solid and a fluid)

6
Deformation of Fluids
7
Newtonian Fluids
  • Fluids in which shear stress is directly
    proportional to rate of deformation are called
    Newtonian fluids
  • Most common fluids such as water, air, and
    gasoline are Newtonian under normal conditions
  • If a fluid is Newtonian then
  • The constant of proportionality is called
    Absolute or Dynamic viscosity denoted by
  • The ratio of absolute viscosity to density is
    called Kinematic Viscosity and is denoted by

8
Non Newtonian Fluids
  • Fluids in which shear stress is not directly
    proportional to deformation rate are non-
    Newtonian
  • Examples are toothpaste and Lucite5 paint.
  • The paint is very thick when in the can, but
    becomes thin when sheared by brushing.
  • Toothpaste behaves as a fluid when squeezed
    from the tube. However, it does not run out by
    itself when the cap is removed.
  • There is a threshold or yield stress below which
    toothpaste behaves as a solid

9
(a) Shear stress, t, and (b) apparent viscosity,
?, as a function of deformation rate for
one-dimensional flow of various non-Newtonian
fluids.
10
Apparent Viscosity
  • The viscosity is normally constant but apparent
    viscosity depends upon shear rate and may be much
    higher at certain shear rates for non Newtonian
    fluids
  • Mathematically

11
Types of Non Newtonian fluids
  • Fluids in which the apparent viscosity decreases
    with increasing deformation rate (nlt1) are called
    pseudoplastic (or shear thinning) fluids.
  • Examples are polymer solutions, colloidal
    suspensions, and paper pulp in water
  • If the apparent viscosity increases with
    increasing deformation rate (ngt1) the fluid is
    termed dilatant (or shear thickening).
    Suspensions of starch and of sand are examples of
    dilatant fluids
  • On the beachif you walk slowly (and hence
    generate a low shear rate) on very wet sand, you
    sink into it, but if you jog on it (generating a
    high shear rate), its very firm.

12
Types of Non Newtonian fluids
  • A fluid that behaves as a solid until a minimum
    yield stress, ty, is exceeded and subsequently
    exhibits a linear relation between stress and
    rate of deformation is referred to as an ideal or
    Bingham plastic. The corresponding shear stress
    model is
  • Clay suspensions, drilling muds, and toothpaste
    are examples of substances exhibiting this
    behavior

13
Types of Non Newtonian fluids
  • Thixotropic fluids Non-Newtonian fluids in which
    apparent viscosity may be time-dependent i.e.
    show a decrease in ? with time under a constant
    applied shear stress many paints are
    thixotropic.
  • Rheopectic Non Newtonian fluids that show an
    increase in ? with time hence called Rheopectic.
  • Viscoelastic After deformation some fluids
    partially return to their original shape when the
    applied stress is released such fluids are
    called viscoelastic (many biological fluids work
    this way).

14
Surface tension
15
Surface tension
16
Surface tension
17
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18
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19
Viscous and Invicid flows
20
Reynolds No
  • A number given by
  • It is used to predict whether viscous forces
    acting on a body are negligible as compared to
    pressure forces or not
  • If Re is high, viscous forces are negligible
  • If it is low then the viscous forces are not
    negligible
  • If it is neither small nor large, no general
    conclusion can be drawn

21
Reynolds No
22
Various concepts
  • Inviscid Flow A friction less flow is called
    inviscid flow. It has no Viscosity effects
  • Viscous Flow A flow which involves force of
    friction is called viscous flow
  • Stagnation points where velocity is zero

23
Boundary layer
24
Boundary layer
25
Boundary layer over a streamlined object
26
Laminar and Turbulent Flows
27
Laminar and Turbulent Flows
28
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29
Compressible and incompressible flows
30
Compressible and incompressible flows
31
Compressible and incompressible flows
32
Internal and External Flows
33
Summary and Useful equations
34
Summary and Useful equations
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