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MTH- 486: Fluid Mechanics
Instructor:
Dr. Fahad Munir Abbasi
Assistant Professor
Department of Mathematics
Comsats Institute of Information Technology
Islamabad, Pakistan
Layout of lecture # 5
Summary of the previous lecture
Newtonian and non-Newtonian fluids
Types of non-Newtonian fluids
Flow between two plates: Solved examples
Summary
Previously we studied…
Velocity of the fluid at a point: local and particle rate of change
Viscosity of a fluid
Real and Ideal fluids
MTH-486, Fluid Mechanics Lec. # 05
Newtonian fluids:
Fluids in which the shear stress is directly proportional to the rate of
deformation are called the β€œNewtonian fluids”.
For such fluids, the Newton’s law of viscosity holds, i.e.
𝒅𝒖
𝒔𝒉𝒆𝒂𝒓 𝒔𝒕𝒓𝒆𝒔𝒔 ∝
π’…π’š
Ο„π’™π’š
𝒅𝒖
=ΞΌ
π’…π’š
(1)
Where the constant of proportionality β€œΞΌβ€ is known as the viscosity of the
fluid.
MTH-486, Fluid Mechanics Lec. # 05
Non-Newtonian fluids:
Fluid in which the shear stress is not directly proportional to the rate of
deformation are called the β€œnon-Newtonian fluid”.
Examples: Toothpaste, blood, ketchups, paint, drilling mud, biological
fluids, etc.
For such fluids, the β€œPower law model” holds, i.e.:
𝒅𝒖
𝒔𝒉𝒆𝒂𝒓 𝒔𝒕𝒓𝒆𝒔𝒔 ∝
π’…π’š
Ο„π’™π’š
𝒏
𝒅𝒖
=π’Œ
π’…π’š
,
𝒏 β‰  𝟏.
𝒏
(2)
MTH-486, Fluid Mechanics Lec. # 05
Where
β€œn” is flow behavior index,
β€œk” the consistency index.
Note that Eq. (2) reduces to Newton’s law of viscosity for n = 1 and k = ΞΌ.
Also from Eq. (2)
Ο„π’™π’š
𝒅𝒖
=Ξ·
,
π’…π’š
(3)
Where
𝒅𝒖
Ξ·=π’Œ
π’…π’š
Is the apparent viscosity.
π’βˆ’πŸ
(4)
MTH-486, Fluid Mechanics Lec. # 05
The rod climbing or the Weissenberg effect
When a rod is rotated in a beaker containing a polymer (non-Newtonian)
solution. The solution moves in the opposite direction of the motion of the
rod and climbs up the rod. This effect is known as the β€œrod climbing effect”
or the β€œWeissenberg effect”. For a beginner, this is a simple test to
differentiate between the Newtonian and non-Newtonian fluid.
MTH-486, Fluid Mechanics Lec. # 05
Types of non-Newtonian fluids:
The non-Newtonian fluids are divided into three broad groups:
Non-Newtonian
Fluids
Time independent
fluids
Time dependent
fluids
Viscoelastic fluids
MTH-486, Fluid Mechanics Lec. # 05
.
Time independent
fluids
Pseudoplastic or
shear thinning
fluids (n < 1)
Dilatant or shear
thickening fluids
(n >1)
Ideal or Bingham
plastic fluids
MTH-486, Fluid Mechanics Lec. # 05
.
Time dependent
fluids
Thixotropic fluids
Rheopectic fluids
MTH-486, Fluid Mechanics Lec. # 05
Time independent non-Newtonian fluids:
1. Pseudoplastic (or shear thinning) fluids:
Fluids in which the apparent viscosity decreases with increasing
deformation rate, i.e. n < 1.
Examples: Polymer solution such as rubber, Colloidal suspensions and
paper pulp In water, blood, milk etc.
2. Dilatant (or shear thickening) fluids:
Fluids in which the apparent viscosity increases with increasing
deformation rate, i.e. n > 1.
Examples: suspensions of starch and of sand, butter, printing ink, suger in
water etc.
MTH-486, Fluid Mechanics Lec. # 05
3. Ideal or Bingham plastic fluids:
Fluids that behave as solids until a minimum yield strength, Ο„π’š is exceeded
and subsequently exhibits a linear relation between stress and rate of
deformation. Mathematically
Ο„π’™π’š
𝒅𝒖
= Ο„π’š + μ𝒑
π’…π’š
Examples: Drilling muds, toothpaste and clay suspensions, jellies etc.
MTH-486, Fluid Mechanics Lec. # 05
Time dependent non-Newtonian fluids:
1. Thixotropic fluids:
Fluids that show a decrease in Ξ· with time under a constant applied shear
stress.
Examples: Lipstick, some paints and enamels, etc.
2. Rheopectic fluids:
Fluids that show an increase in Ξ· with time under a constant applied shear
stress.
Examples: gypsum suspension in water and bentonite solution, etc.
MTH-486, Fluid Mechanics Lec. # 05
Viscoelastic non-Newtonian fluids:
Some fluid after deformation partially return to their original shape when
the applied stress is released. Such fluids are named as β€œviscoelastic
fluids.”
Viscoelastic fluids have two major types: linear viscoelastic fluids e.g. the
Maxwell and Jeffery’s fluids, and non-linear viscoelastic fluids e.g. Walter’s
A and B fluid, Oldroyed A and B etc.
MTH-486, Fluid Mechanics Lec. # 05
Graphical representation:
Fig. 1: Flow curves for time independent fluids.
MTH-486, Fluid Mechanics Lec. # 05
Graphical representation:
Fig. 2: Flow curves for time dependent fluids
MTH-486, Fluid Mechanics Lec. # 05
Graphical representation:
Fig. 3: Flow curves for time dependent fluids
MTH-486, Fluid Mechanics Lec. # 05
Flow between two plates:
An infinite plate is moved over a second plate on a layer of liquid.
For small gap width, h = 0.3mm, we assume a linear velocity
distribution in the liquid, U = 0.3 m/sec. The liquid viscosity is 0.65 X
π‘²π’ˆ
βˆ’πŸ‘
𝟏𝟎
π’Ž.𝒔𝒆𝒄
i)
and its specific gravity is 0.88. Find:
The kinematic viscosity of the fluid.
ii) The shear stress on lower plate.
iii) Indicate the direction of shear stress.
MTH-486, Fluid Mechanics Lec. # 05
Flow between two plates:
MTH-486, Fluid Mechanics Lec. # 05
density
MTH-486, Fluid Mechanics Lec. # 05
Now,
i) Ξ½ =
ΞΌ
ρ
=
𝟎.πŸ”πŸ“ 𝑿 πŸπŸŽβˆ’πŸ‘
𝟎.πŸ–πŸ– 𝑿 πŸπŸŽπŸ‘
ii) Ο„π’šπ’™ = Ο„π’π’π’˜π’†π’“ =
=βˆ’βˆ’ βˆ’
𝒅𝒖
ΞΌ
π’…π’š
=
𝑼
ΞΌ
𝒉
π’ŽπŸ
𝒔𝒆𝒄
=
π‘²π’ˆ
𝟎. πŸ”πŸ“
π’Ž.π’”π’†π’„πŸ
iii) Since the Ο„π’šπ’™ is positive so the direction of shear stress is along
positive x-axis.
MTH-486, Fluid Mechanics Lec. # 05
Example # 02:
Suppose that the fluid being sheared between to plates is SAE 30 oil
(ΞΌ = 0.29
π‘²π’ˆ
)
π’Ž.𝒔𝒆𝒄
at 20°C. Compute the shear stress
in the oil if V=3 m/s and h = 2 cm.
Solution:
π‘²π’ˆ
π’Ž
𝒅𝒖
𝑽 𝟎. πŸπŸ— π’Ž. 𝒔𝒆𝒄 𝑿 πŸ‘. 𝟎 𝒔𝒆𝒄
Ο„=ΞΌ
=ΞΌ =
π’…π’š
𝒉
𝟎. 𝟎𝟐 π’Ž
π‘²π’ˆ
𝑡
= 𝟎. πŸ’πŸ‘
= πŸ’πŸ‘ 𝟐 = πŸ’πŸ‘π‘·π’‚
𝟐
π’Ž. 𝒔𝒆𝒄
π’Ž
Summary
Newtonian and non-Newtonian fluids
Types of non-Newtonian fluids
Solved examples
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