Chapter 1 Fundamentals · 2018. 4. 20. · • state: solid. liquid increasing spacing increasing...
Transcript of Chapter 1 Fundamentals · 2018. 4. 20. · • state: solid. liquid increasing spacing increasing...
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Chapter 1
Fundamentals
No-slip of real fluid
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Chapter 1 Fundamentals
Contents1.1 Scope of Fluid Mechanics
1.2 Historical Perspective
1.3 Physical Characteristics of the Fluid State
1.4 Units and Density
1.5 Compressibility, Elasticity
1.6 Viscosity
1.7 Surface Tension, Capillarity
1.8 Vapor Pressure
Objectives
- Present concept of fluidity
- Introduce fundamental properties of fluid
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1.1 Scope of Fluid Mechanics
• Problems of water supply
flood prevention
navigation need to know fluid phenomena
water power
irrigation
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1.2 Historical Perspective
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1.2 Historical Perspective
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1.2 Historical Perspective
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1.2 Historical Perspective
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1.2 Historical Perspective
• d'Alembert (1744)
"The theory of fluids must necessarily be based upon experiment"
• d'Alembert paradox theory - ideal, inviscid fluid
practice - real fluid (viscous)
• Two schools theoretical group → hydrodynamics
practical group → hydraulics
• Navier and Stokes
→ general equations for viscous fluid → equation of motion
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1.2 Historical Perspective
[Re] Navier-Stokes equation
Claude-Louis Navier (1785-1836, French engineer) and George Gabriel
Stokes (1819-1903, UK mathematician & physicist)
- one continuity equation + three momentum equations
- model the weather, ocean currents, water flow in a pipe, the air's flow
around a wing, and motion of stars inside a galaxy
- design of aircraft and cars, the study of blood flow, the design of power
stations, the analysis of pollution,
- exact solution - one of the seven most important open problems in
mathematics → “Gifted (2017)”
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1.2 Historical Perspective
( )2 2 2
2 2 2
13x x
p u u ug aqx xx y z
ρ µ µ ρ ∂ ∂∂ ∂ ∂
− + + =+ + ∇ ⋅ ∂ ∂∂ ∂ ∂
( )2 2 2
2 2 2
13y y
p v v vg aqy yx y z
ρ µ µ ρ ∂ ∂∂ ∂ ∂
− + + =+ + ∇ ⋅ ∂ ∂∂ ∂ ∂
( )2 2 2
2 2 2
13z z
p w w wg aqz zx y z
ρ µ µ ρ ∂ ∂∂ ∂ ∂
− + + =+ + ∇ ⋅ ∂ ∂∂ ∂ ∂
( ) ( ) ( ) 0u v wt x y zρ ρ ρ ρ∂ ∂ ∂ ∂+ + + =
∂ ∂ ∂ ∂
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1.2 Historical Perspective
• New problems in modern times
- dispersion of man's wastes in lakes, rivers, and oceans
→ Environmental Fluid Mechanics (Hydraulics)
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• state: solid
liquid increasing spacing increasing inter
fluid gaseous and latitude of molecular cohesive
plasma particle motion force
• fluid – continuum (연속체) → no voids or holes
1.3 Physical Characteristics of the Fluid State
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1.3 Physical Characteristics of the Fluid State
stressstrain
solid fluid
tension
elastic deformation
→ permanent distortion
unable to support tension
(surface tension)
compressionelastic deformation
(compressible fluid)
shear (tangential forces)
permanent distortion or flow
(change shape) to infinitesimal
shear stress
(연속적 변형 또는 흐르는 물질)
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1.3 Physical Characteristics of the Fluid State
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1.3 Physical Characteristics of the Fluid State
stress
real fluid (viscous fluid; 실제유체)
ideal fluid
(non-viscous
Fluid; 이상유체)
in motion at restat rest and
in motion
compression
(pressure)○ ○ ○
shear ○ × ×
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1.3 Physical Characteristics of the Fluid State
incompressible fluid (비압축성 유체) compressible fluid (압축성 유체)
① Compressibility is of small important. ① Compressibility is predominant.
② Liquids and gases may be treated
similarly.
② Behavior of liquids and gases is quite
dissimilar.
③ Fluid problems may be solved with
the principles of mechanics.
③ Thermodynamics and heat transfer
concepts must be used as well as
principles of mechanics.
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17/961.4 Units and Density
물리량 SI unit English Unit (FSS) Korean Unit
Length (L) metre (m) feet (ft) 자=0.3m, 리=392m
Mass (M) kilogram (kg) slug (-) 근=600g
Time (t) second (s) second (s) 경=2시간, 나절=6시간
Temp. (T) kelvin (K)degree Rankine (°
R)도
Basic units (기본단위)
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1.4 Units and Density
■ International System of Units; SI system – metric system (국제표준단위계)
[Cf] English Unit System (영국계 단위계)
f• Frequency ( ): hertz (HZ = s-1) F
F ma=
2/ /a v t L t= = 2Lt− /v L t= 1Lt−
21kg m/s 1N( )F Newton∴ → ⋅ =
• Force,
→ introduce Newton's 2nd law of motion
Force = mass × acceleration
(m/s2)
(m/s)
■ 기본단위 vs 유도단위
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1.4 Units and Density
E2 2kg m /s ( )E FL J Joule= → ⋅ =
P2 3/ / kg m sP E t J s= → = ⋅
p ,σ τ2 2/ N/m Pa (pascal) kg/m sp F A= → = = ⋅
T
• Energy, (work)
• Power,
• Pressure, ; Stress,
• Temperature, : degree Celsius (°C)
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1.4 Units and Density
ρ
3kg/mMV
ρ = →
• Density (밀도),
= mass per unit volume → heaviness
~ depends on the number of molecules per unit of volume
~ decreases with increasing temperature
γ
3 2 2N/m kg/m sWV
γ = → = ⋅
• Specific weight (weight density; 단위중량),
= weight (force) per unit volume
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1.4 Units and Density
(1.1)
W Mg=g
gγ ρ∴ =
[Re](Newton’s 2nd law of motion)
= acceleration due to gravity
1/ ρ• Specific volume=volume per unit mass=
• Specific gravity, s.g. , ~ r. d. (relative density; 비중)
= ratio of density of a substance to the density of water at a specified
temperature and pressure
. . f fw w
s gρ γρ γ
= =
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1.4 Units and Density
[Re] s.g. of sea water = 1.03
s.g. of soil = 2.65
s.g. of mercury = 13.6
SI unit English unit
1,000 kg/m3 1.94 slugs/ft3
9,806 N/m3 62.4 lb/ft3
9.81 m/s2 32.2 ft/s2
ρ
γ
g
Water at 5 °C
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Density measurement
Pycnometer (specific gravity bottle; 비중병)– Equipment to weigh accurately a known volu
me of liquid.– The specific weight of the liquid,
– W2 is total weight of the pycnometer,– W1 is the weight of empty pycnometer– γt is specific weight of the liquid
2 1t
W WV
γ−
=
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Density measurement
Hydrometer (비중계)– Float with different immersions
in liquids of different densities
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1.4 Units and Density
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1.4 Units and Density
α
β,γ Γ
,δ ∆εζη
,θ Θ
ι
• Greek Alphabet
Alpha angle
Beta [beitə] angle
Gamma specific weight, circulation
Delta thickness of boundary layer
Epsilon eddy viscosity, height of surface roughness
Zeta
Eta
Theta
Iota [aioutə]
Kappa [kæpə]κ
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1.4 Units and Density
,λ Λ
µ
νξοπ
ρ
,σ ∑
τ
Lambda
Mu [mju:] dynamic viscosity
Nu kinematic viscosity
Xi [gzai, ksai] vorticity
Omicron
Pi [pai]
Rho mass density
Sigma Sigma Xi, Scientific Research Society, 1886
honor society for scientists & engineers
Tau shear
Upsilon,υ ϒ
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1.4 Units and Density
,ϕ Φ
χ
,ψ Ψ
,ω Ω
Phi [fai] Phi Beta Kappa
Chi [kai]
Psi [psai, sai] stream function
Omega angular velocity
• Prefixes
E exa 1018
P peta 1015
T tera 1012
G giga 109
M mega 106
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1.4 Units and Density
µ
M mega 106
k kilo 103
h hecto 102
da deca 101
d deci 10-1
c centi 10-2
m milli 10-3
micro 10-6
n nano 10-9
p pico 10-12
f femto 10-15
a atto 10-18
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1.4 Units and Density
유체역학 계산 (문제풀이)• 동차성의 원리
- 모든 항은 동일한 차원을 가져야 함. 또한 동일한 단위계로 계산하여야 함
• 정확도
- 계산과정에서 유효숫자가 4자리 이상으로 표시되더라도,해답은 3자리로 반올림함.
이유는 유체의 물성데이터나 실험 결과의 정확도가 유효숫자 3자리를 넘지 않기 때문임
• 문제풀이
- 주어진 데이터를 나열하고, 문제 풀이에 필요한 그림(개념도, 그래프)을 그림
- 유체 원리에 해당하는 수학적 식을 쓴다.
- 식에 대입하는 수치들의 단위를 포함하고 동차성의 원리를 따르는지 점검
- 식을 풀고 해답은 유효숫자 3자리로 표기함
- 구한 답이 공학적인 상식에 부합하는 지 판단함. 또한 의미를 찾아서 자신만의 토론
을 붙임
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1.5 Compressibility, Elasticity
• Elastic behavior to compression
• Compressibility (압축성) ≡ change in volume due to change in pressure
solid - modulus of elasticity, E (N/m2)fluid - bulk modulus
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1.5 Compressibility, Elasticity
1
dVdpV
∝1
dVdp EV
→ = −
1
1
( , )dp dpE V const fn p TdV dVV
= − = − ≠ = → p E↑ → ↑
1
1 1dVCE V dp
= = −
• Stress-strain curve (E↑, difficult to compress)
= modulus of compressibility (m2/N)
Minus means that increase in
pressure causes decrease in
volume
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1.5 Compressibility, Elasticity
, 1E C= ∞ ρ
[Re] large E or small C → less compressible• incompressible fluid (inelastic):
→ constant density =const.
~ water is incompressible fluid.
• compressible fluid
→ changes in density → variable density
~ gas
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1.5 Compressibility, Elasticity
Pressure
106 N/m2
Temperature, °C
0° 20° 50° 100° 150°
0.1 1950 2130 2210 2050
10.0 2000 2200 2280 2130 1650
30.0 2110 2320 2410 2250 1800
100.0 2530 2730 2840 2700 2330
Bulk modulus of water, E (106 N/m2)
1.5 Compressibility, Elasticity
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1.5 Compressibility, Elasticity
Compressibility Modulus of Elasticity, E (kPa)
steel 1/80 of water water 2,170,500
mercury 1/12.5 of water sea water 2,300,000
nitric acid 6 of water mercury 26,201,000
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1.5 Compressibility, Elasticity
E
E
- increases as pressure increases.
- is maximum at about 50 °C.
→ The water has minimum compressibility at about 50 °C.
1dpE VdV
= −
1
V pV E∆ ∆
≈ −
2 1 2 1
1
V V p pV E− −
≈ −
• For the case of a fixed mass of liquid at constant temperature
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1.5 Compressibility, Elasticity
62,200 10 PaE = ×6
2 1 7 10 Pap p= + ×
2 1 2 1
1
0.0032V V p pV E− −
∴ ≈ − = −
2 1(1 0.0032)V V∴ = −
0.3%V∆ ≈
[Ex] For water; @ 20˚C
decrease
→ water is incompressible
63
7 10 Pa 70101.3 10 Pap×∆ = ≈
×기압
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1.6 Viscosity
[Re] From Wikipedia
Viscosity is a measure of the resistance of a fluid which is being
deformed by either shear stress or tensile stress. (상대적인 운동에 저항
하는 성질)
Viscosity ~ "thickness" or "internal friction"
▪ water ~ "thin (묽다)", having a lower viscosity
▪ honey ~ "thick (진하다)", having a higher viscosity
The less viscous the fluid is, the greater its ease of movement (fluidity).
Viscosity describes a fluid's internal resistance to flow and may be
thought of as a measure of fluid friction.
dvdy
τ µ=
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1.6 Viscosity
For example, high-viscosity felsic (규장질) magma will create a tall, steep
stratovolcano, because it cannot flow far before it cools, while low-viscosity
mafic (철질암) lava will create a wide, shallow-sloped shield volcano.
All real fluids (except superfluids) have some resistance to stress and
therefore are viscous, but a fluid which has no resistance to shear stress is
known as an ideal fluid or inviscid fluid.
[Re] super fluid – a fluid having frictionless
flow, and other unusual properties
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1.6 Viscosity
• Two types of fluid motion (real fluid)
1) laminar flow:
- viscosity plays a dominant role
- fluid elements or particles slide over each other in layers (laminar)
- molecular diffusion
[Ex] flow in a very small tube, a very thin flow over the pavement, flow in
the laminar flow table
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1.6 Viscosity
Re Vdν
=
where V = flow velocity; d = characteristic length; ν = kinematic viscosity
diameter of pipe,depth of stream
2) turbulent flow:
- random or chaotic motion, eddies of various sizes are seen
- common in nature (streams, rivers, pipes)
- large scale mixing between the layers
• Reynolds number
[Ex] flows in the water supply pipe, flows in the storm sewer pipe, flows in
the canals and streams
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1.6 Viscosity
• Reynolds experiments
laminar flow: Re < 2,100
transition: 2,100 4,000
The same fluid withdifferent velocity
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1.6 Viscosity
cubestreamline
source
sink
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1.6 Viscosity
Smoothsurface
Eddyingmotion
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1.6 Viscosity
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1.6 Viscosity
Symmetric shape,No separation
Re < 1
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1.6 Viscosity
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1.6 Viscosity
Separation, eddyformation
Growthof eddy
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1.6 Viscosity
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1.6 Viscosity
후방난류
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1.6 Viscosity
Spiralsecondaryflow
Secondaryflow
대규모와류
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1.6 Viscosity
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1.6 Viscosity
• Deformation of solid between two plates
Shear stress total angular displacement
yxdGdyζτ =
∝
yxddyζτ ∝
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1.6 Viscosity
• Laminar flow between two plates
2 1d d dvdt dv dtdy dy dy−
= = =
2 2 1 1
2 1 2 1
;( )
d v dt d v dtd d v v dt
= =− = −
strain = angular displacement (전단변형도)
[Re]
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1.6 Viscosity
τ• Experiment has shown that, in many fluids, shearing (frictional) stress
per unit of contact area, is proportional to the time rate of relative
strain (Newton).
/dv dvdt dtdy dy
τ∴ ∝ =
dvdy
τ µ= →
(velocity gradient)
Newton’s equation of viscosity (1.2)
µwhere = coefficient of viscosity
= dynamic (absolute) viscosity (점성계수)
• Viscosity ~ measure of fluid's resistance to shear or angular deformation
~ internal resistance of a fluid to motion (fluidity)
Large → sticky, difficult to flowµ
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1.6 Viscosity
du duu y t u t y tdy dy
= + ∆ ∆ − ∆ = ∆ ∆
/du duy t y tdy dy
= ∆ ∆ ∆ = ∆
[Re] rate of angular deformation (전단변형도의 시간변화율)
(i) displacement of AB relative to CD
(ii) angular displacement of AC
(iii) time rate of angular deformation
/du dut tdy dy
= ∆ ∆ =
dvdy
τ µ=
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1.6 Viscosity
µ• dynamic viscosity,
/F Aτ =
[ ] 2 2 1 2 2/ kg/(m s ) PaMLt L ML tτ − − − = = ⋅ = 1
1dv Lt tdy L
−− = =
[ ]1 2
1 1 21/ kg/m s N s / m Pa s
dv ML t ML tdy t
µ τ− −
− −−
∴ = = = = ⋅ = ⋅ = ⋅
11 ( ) 10 Pa spoises Poiseuille −⇒ = ⋅
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1.6 Viscosity
ν• kinematic viscosity (동점성계수),µνρ
=
[ ]1 1
2 1 23 m /s
ML t L tML
ν− −
−−
= = =
(1.3)
1 m2/s = 104 stokes =106 centistokes
,τ µ
τ τ
• Remarks on Eq. (1.2)
① are independent of pressure.
[Cf] friction between two moving solids
② Shear stress (even smallest ) will cause flow (velocity gradient).
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1.6 Viscosity
0 0dvdy
τ= → = µregardless of
③ Shearing stress in viscous fluids at rest will be zero.
dvdy
≠ ∞ τ→ ≠ ∞④ At solid boundary, ( (no infinite shear))→ Infinite shearing stress between fluid and solid is not possible.
⑤ Eq. 1.2 is limited to laminar (non-turbulent) fluid motion in which
viscous action is predominant.
[Cf] For turbulent flow
ε µ( )dvdy
τ µ ε= +
where ε = eddy viscosity
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1.6 Viscosity
⑥ Velocity at a solid boundary is zero.
→ No-slip condition (continuum assumption; 점착조건, 비활조건)
• Newtonian and non-Newtonian fluids
i) Newtonian fluid ~ water
ii) Non-Newtonian fluid ~
plastic, blood, suspensions, paints,
polymer solutions → rheology
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1.6 Viscosity
1dvdy
τ τ µ− =
ndvKdy
τ
=
1τ
1n >
1n <
• Non-Newtonian fluid
1) plastic, = threshold
2) Shear-thickening fluid
Shear-thinning fluid
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1.6 Viscosity
• Couette flow: laminar flow in which the shear stress is constant
- thin fluid film between two large flat plates
- thin fluid film between the surfaces of coaxial cylinders
dv Vdy h
=
Vh
τ µ∴ =
~ linear velocity gradient
~ constant
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1.6 Viscosity
[IP 1.1] Couette flow
Upper plate is moving on the oil (µ = 0.0652 N·s/m2) with the constant velocity
0.2 m/s. Find force F. The thickness of oil is 0.1 mm, and the contact area of the upper plate is 75 cm2.
[Solution]
2 23
2 2 2
(0.2 / )(0.0652 / ) 130.4 /(0.1 10 )
(130.4 / )(75 10 ) 97.8 ~10
F Adv Vdy h
m sN s m N mm
F N m m N kg
τ
τ µ µ
τ −
−
=
= =
= ⋅ =×
= × = 중
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64/961.6 Viscosity
gas liquid
main cause of
viscosity
exchange of molecule's momentum →
interchange of molecules between
the fluid layers of different velocities
intermolecular cohesion
effect of
temperature
variation
temp↑ → molecular activity↑
→ viscosity↑ → shearing stress↑
temp↑ → cohesion↓
→ viscosity↓ → shear stress↓
[Re] Viscosities of gas and liquid
Friction forces result from
- cohesion for liquid
- momentum interchange between molecules for gas
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1.6 Viscosity
Two layers tendto stick togetheras if there issome viscositybetween two.
[Re] Exchange of momentum
fast-speed layer (FSL)
molecules from FSL speed up molecules in LSL
molecules from LSL slow down molecules in FSL
low-speed layer (LSL)
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1.6 Viscosity
[Re]
- Exchange of momentum (운동량 교환): exchange momentum in either
direction from high to low or from low to high momentum due to random
motion of molecules ~ molecular scale
- Transport of momentum (온동량 전달): transport of momentum from
layers of high momentum (high velocity) to layers of low momentum ~
continuum scale
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Viscosity measurement
Rotational Viscometers
Outer cylinder is rotating at constant angular velocity (각속도), ωMeasure torque (회전모멘트) on the inner cylinder
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Rotational Viscometers- Measure torque, T on the inner tank
2 322
R h V R VTR h
π µ π µ= +
∆ ∆
T F r Ardvdy
τ
τ µ
= =
=
1
1
1
2
1
2
2
2
2
3
2
2
2
2
2
i
i
i
i
i
i
T Fr Ar
dV V
dy R
A R h
r R
R hVT
RV
h
A R
Rr
R VT
h
τ
τ µ µ
π
πµ
τ µ
π
πµ
= =
= =∆
=
=
=∆
=∆
=
=
=∆
10
Viscosity measurement
V Rω=
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1.7 Surface Tension, Capillarity
• Surface tension
- occur when the liquid surfaces are in contact with another fluid (air) or
solid
- Forces develop in the liquid surface that cause the surface to behave as
if it were a “skin” or “membrane” stretched over the liquid mass
• Engineering problems related to surface tension
- capillary rise of liquids in narrow spaces
- formation of liquid drops
- small models of larger prototype
→ dam, river model
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1.7 Surface Tension, Capillarity
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1.7 Surface Tension, Capillarity
σ /F L• surface tension, ( , N/m)- force per unit length
- force attracting molecules away from liquid
- function of (relative sizes of intermolecular cohesive and adhesive
forces to another body)
- as temp↑ → cohesion↓ → σ↓ ☞ Table A2.4b, p. 694
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72/961.7 Surface Tension, Capillarity
Consider the small element dx dy of a surface of double curvature with radii R1and R2
0F∑ =
0( ) 2 sin 2 sinip p dxdy dy dxσ α σ β− = +
where pi = pressure inside the curvature; po = pressure inside the
curvature
1
sin ,2dxR
α ≈2
sin ,2dyR
β ≈ 12( sin )dx R α=
01 2
1 1ip p R R
σ
∴ − = +
(1.4)
→ for the force components normal to the element
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1.7 Surface Tension, Capillarity
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1.7 Surface Tension, Capillarity
• Cylindrical capillary tube
- due to both cohesion (응집력) and adhesion (부착력)
cohesion < adhesion → rise (water)
cohesion > adhesion → depression (mercury)
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1.7 Surface Tension, Capillarity
1 2R R R= = ≈
0p hγ= −
0ip =
For a small tube, given conditions are as follows
(liquid surface section of sphere)
(hydrostatic pressure)
(atmospheric)
01 2
1 1ip p R R
σ
− = + 2h
Rγ σ∴ =
Substitute above conditions into Eq. 1.4: (1.5)
cosr R θ=2 2 cos
/ cosh
r rσ θγ σ
θ∴ = =
2 coshr
σ θγ
=
By the way,
(1.6)
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1.7 Surface Tension, Capillarity
h r hθr ≤
in which = capillary rise → ↑ → ↓
= angle of contact
= radius of tube 2.5 mm for spherical form
12r > h
[Ex] water and mercury
If mm, is negligible for water.
• Pressure measurement using tubes in hydraulic experiments
→ Ch.2 manometer
~ capillarity problems can be avoided entirely by providing
tubes large enough to render the capillarity correction negligible.
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1.7 Surface Tension, Capillarity
• Formation of curved surface, droplet
- At free liquid surface contacting the air, cohesive forces
at the outer layer are not balanced by a layer above.
→ The surface molecules are pulled tightly to the lower layer.
→ Free surface is curved.
[Ex] Surface tension force supports small loads (water strider).
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1.7 Surface Tension, Capillarity
0 1.0ip p− =
0.0728σ =At 20°C, N/m ← App. 2
[IP 1.10] For a droplet of water (20 °C), find diameter of droplet
Given: kPa
01 2
1 1 2ip p R R R
σσ
− = + =
∴1R⋅
0.000146m 0.146mmR∴ = = 0.292d→ =
[Sol]
(1.4)
1×103 N/m2 = 2(0.0728)
mm
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1.7 Surface Tension, Capillarity
[IP 1.11] Find height of capillary rise in a clean glass tube of 1 mm
diameter if the water temperature is 10°C or 90°C.
[Sol]
From App. 2 Table A 2.4b;
σ γ
σ γ@ 10°C =0.0742 N/m, = 9.804 kN/m3
@ 90°C =0.0608 N/m, = 9.466 kN/m3
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1.7 Surface Tension, Capillarity
Use Eq. 1.16
For water, 0θ =
2 coshr
σ θγ
=
1̀02(0.0742)(1) 0.030m=30mm
9804(0.0005)h = =
902(0.0608)(1) 0.026m=26mm
9466(0.0005)h = =
(1.5)
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1.8 Vapor Pressure
• Vapor pressure is the partial pressure exerted by ejected
molecules of liquid.
• 증기압 – 분자의 운동에너지에 기인
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1.8 Vapor Pressure
• Liquids tend to vaporize or evaporate due to molecular thermal
vibrations (molecular activity).
- Evaporation takes place because some liquid molecules at the
surface have sufficient momentum to overcome the intermolecular
cohesive forces and escape into the atmosphere.
- If the container is closed with a small air space left above the surface,
a pressure will develop in the space as a result of the vapor that is
formed by the escaping molecules.
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1.8 Vapor Pressure
55.2 kPavp =2.34 kPavp =
0.00017 kPavp =
• volatile liquids (휘발성 액체):
~ easy to vaporize → high vapor pressure
gasoline: at 20 °C
water: at 20 °C
mercury: at 15.6 °C
• mercury: low vapor pressure and high density → difficult to vaporize
→ suitable for pressure-measuring devices
• Vapor pressure → Table A2.1 and A2.4b
temperature↑ → molecular activity↑ → vaporization↑ → vapor pressure↑
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1.8 Vapor Pressure
In the interior and/or boundariesof a liquid system
• Cavitation (공동현상): App. 7 (p. 672)
In a flow fluid wherever the local pressure falls to the vapor pressure of
the liquid, local vaporization occurs.
→ Cavities (공동) are formed in the low pressure regions.
→ The cavity contains a swirling mass of droplets and vapor.
→ Cavities are swept downstream into a region of high pressure.
→ Then, cavities are collapses suddenly.
→ it causes erosion (pitting) of solid boundary surfaces in machines, and
vibration
→ boundary wall receives a blow as from a tiny hammer
[Cf] 지하동공 (싱크홀) -> 지반함몰
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1.8 Vapor Pressure
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1.8 Vapor Pressure
• Prevention of cavitation
~ cavitation is of great importance in the design
of high-speed hydraulic machinery such as
turbines, pumps, in the overflow and underflow
structures of high dams, and in high-speed
motion of underwater bodies (submarines,
hydrofoils).
→ design improved forms of boundary surfaces
→ predict and control the exact nature of
cavitation → set limits
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1.8 Vapor Pressure
atm vp p≤
• Boiling:
= rapid rate of vaporization caused by an increase in temperature
= formation of vapor bubbles throughout the fluid mass
~ occur (whatever the temperature) when the external absolute pressure
imposed on the liquid is equal to or less than the vapor pressure of the
liquid
~ boiling point = fn (imposed pressure, temp.)→ boiling occurs
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1.8 Vapor Pressure
altitude
(El. m)
(kPa),
absolute
(kPa),
absolute
boiling point
(°C)remark
m.s.l. 101.3 101.3 at 100°C 100 well cooked
12,000 19.4 19.9 at 60°C 60 undercooked
vpatmp
• Boiling point of water at high altitude
- 해발이 낮은 곳에서 대기압은 101.3 kPa 이나,- 높은 산에 올라가면 공기가 희박하여 기압이 낮아짐- 해발 12,000 m에서는 대기압이 19.4 kPa로 떨어짐 (Table A2.5b)- 한편 물의 증기압은 온도의 함수로서 기온이 60 °C 일 때 19.9 kPa 임 (Table A2.4b)- 따라서 해발 12,000 m에서는 물이 60 °C 에서 끓기 시작함.
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1.8 Vapor Pressure
• Evaporation (증발): When the space surrounding the liquid is too large,
the liquid continues to vaporize until the liquid is gone and only vapor
remains at a pressure less than or equal to pv.
[IP 1.12] For a vertical cylinder of diameter 300
mm, find minimum force that will cause the water
boil. (patm = 100 kPa)
patm
F
-
90/96
1.8 Vapor Pressure
'vp p≤
' 100 31.16FpA
∴ = − =
2(0.3)(100 31.16) 4.87 kN4
F π∴ = − =
[Sol] From Table A2.4b: At 70 °C, Pv = 31.16 kPa; patm = 100 kPa
For water to boil;
-
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Homework Assignment # 1
Due: 1 week from today
1. (Prob. 1.10)
A rocket payload with a weight on earth of 8,900 N is landed on the moon
where the acceleration due to the moon’s gravity gm ≈ gn /6. Find the mass of
the payload on the earth and the moon and the payload’s moon weight.
2. (Prob. 1.27)
The flux of momentum F of a flow through a pipe is F = QγV / gn . Given
that Q is the flowrate with dimensions of ( L3 / t ), what are the dimensions of
F ?
Homework Assignment # 1
-
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3. (Prob. 1.46)
Calculate velocity gradients for y = 0, 0.2, 0.4, and 0.6 m from the
boundary, if the velocity profile is a quarter-circle having its center 0.6 m
from the boundary.
Homework Assignment # 1
-
93/96
4. (Prob. 1.49)
The velocity profile for laminar flow in a pipe is
where r is measured from the centerline where υ = υcand R is the pipe radius. Find τ(r) and dυ / dr . Plot both versus r.
( ) 2 2 1 /( )– c rr Rυ υ=
Homework Assignment # 1
-
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5. (Prob. 1.60)
Crude oil at 20°C fills the space between two concentric cylinders 250
mm high and with diameters of 150 mm and 156 mm. What torque is
required to rotate the inner cylinder at 12 rpm, with the outer cylinder
remaining stationary? Ignore end effects.
Homework Assignment # 1
-
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6. (Prob. 1.69)
The weight falls at a constant velocity of 50 mm/s in the cylinder.
Calculate the approximate viscosity of the oil.
Homework Assignment # 1
-
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7. (Prob. 1.72)
Calculate and plot the maximum capillary rise of water (20℃) to be
expected in a vertical glass tube as a function of tube diameter (for
diameters from 0.5 to 2.5 mm).
8. (Prob. 1.82)
At what temperature will water boil at an altitude of 6,100 m? See
Appendix 2.
Homework Assignment # 1
Chapter 1Chapter 1 Fundamentals1.1 Scope of Fluid Mechanics��슬라이드 번호 4슬라이드 번호 5슬라이드 번호 6슬라이드 번호 71.2 Historical Perspective��1.2 Historical Perspective��1.2 Historical Perspective��1.2 Historical Perspective��1.3 Physical Characteristics of the Fluid State��1.3 Physical Characteristics of the Fluid State��1.3 Physical Characteristics of the Fluid State��1.3 Physical Characteristics of the Fluid State��1.3 Physical Characteristics of the Fluid State��1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��Density measurementDensity measurement 1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��1.4 Units and Density��1.5 Compressibility, Elasticity��1.5 Compressibility, Elasticity��1.5 Compressibility, Elasticity��1.5 Compressibility, Elasticity��1.5 Compressibility, Elasticity��1.5 Compressibility, Elasticity��1.5 Compressibility, Elasticity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity��1.6 Viscosity���1.6 Viscosity��1.6 Viscosity��Viscosity measurement슬라이드 번호 681.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��Consider the small element dx dy of a surface of double curvature with radii R1 and R21.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.7 Surface Tension, Capillarity��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��1.8 Vapor Pressure��슬라이드 번호 91Homework Assignment # 1��Homework Assignment # 1��Homework Assignment # 1��Homework Assignment # 1��Homework Assignment # 1��