Date post: | 24-Oct-2014 |
Category: |
Documents |
Upload: | karina-alexandra-bolanos-moreno |
View: | 253 times |
Download: | 12 times |
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
1
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field.
Pathlines and streamlines. Newton’s Viscosity Law.
Problem 1. The Principle of Dimensional Homogeneity
A valid physical relation for the change in thermal/internal energy of a substance ( 12 UUU −=Δ ) and the specific heat (at constant volume, c ) can be expressed as
TmcU Δ=Δ where m is the mass of the substance and 12 TTT −=Δ is the change in temperature. 1.1. What are the dimensions of the specific heat c in terms of the primary dimensions
• EAtT (E = Energy, M = Mass, t = time, T = Temperature), and • MLtT (M = Mass, L = Length, t = time, T = Temperature)?
1.2. What should be the physical interpretation of the specific heat c ? Problem 2. Field Concept. Classification of Velocity Field. 2.1. Steadiness and Uniformity of the Property Field φ
Let φ be a property whose field representation is ),( txEvφφ = .
We are interested in • the uniformity of the field φ over a region of interest (it can be line, area, or volume) at any one instant, • the steadiness of the field φ over a period of time of interest (and over the region of interest).
Let the shading represent the value of the property φ , say light = high value of φ , dark = low value of φ . Answer the following questions.
(b) Sketch a similar diagram for a uniform but unsteady field.
(a)
t t+dt
Over the region of interest, is the property field φ steady over the period of time of interest? At the instant t, is the property field φ uniform over the region of interest? At the instant t+dt, is the property field φ uniform over the region of interest?
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
2
2.2. Classification of Velocity Field
(a) Fill in the table below. ba, , and c are non-zero, finite constants.
tV ∂∂ /v
Unsteady or Steady ..)(...,...,.VV
vv=
1-, 2-, or 3-dim.
Vvv
×∇=:ω Rotational
or Irrotational
Vv
⋅∇ [a] [b] [c] [d]
A kctjbyiaxV ˆ)(ˆ)(ˆ)( ++=v
kctV ˆ/ =∂∂v
Unsteady ),,( tyxVVvv
= 2 0vv
=×∇ V Irrotational baV +=⋅∇v
1/t 1/t L/t2 -
B ieayV bt ˆ)( 2 −=v
C kcjbyiaxyV ˆ)(ˆ)(ˆ)( +−=v
D ( ) jdicybtaV ˆ)(ˆsin +−=v
(b) Can you initially guess physically what the quantity b in Problem B should be related to? If so, what?
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
3
2.3. Dimensionality and Functionality of A Velocity Field Assuming that the following velocity fields are steady. State the dimensionality of the fields and write down
its functional relation (e.g., ),,,( tzyxVv
, ),,( tyxVv
, ),( zxVv
, or etc.)
(d) Similar to above, sketch an example of the velocity field in which iyVV x
ˆ)(=v
Problem 3. Velocity Field and Its Boundary Conditions. Shear deformation and shear stress.
1. Qualitatively sketch the velocity profile along the transverse AB. Be mindful about physical constraints at the solid and free boundaries. Assume for simplicity first that there is only one dominant velocity component.
2. For the marked surface (marked by solid dot) of the fluid element C (and D):
a. state whether the shear deformation (or velocity gradient) dydu / at the point on that surface is positive or negative,
b. state whether yxτ at the point on that surface is positive or negative, and
c. sketch the correct direction of the shear stress yxτ on that surface at that point. d. Also, state whether the fluid element C is being dragged forward (in x+ direction) or dragged
backward (in x− direction) by the fluid element adjacent to it at that surface.
x
y
z
1-, 2-, or 3-D?
.)..........(.........Vv
(a)
x
y
z
1-, 2-, or 3-D?
.)..........(.........Vv
(b)
x
y
z
1-, 2-, or 3-D?
.)..........(.........Vv
x
y
z
(c)
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
4
3.1. Flow in a channel with a moving plate in the middle. Assume linear velocity distribution across the gaps.
3.2. Wall jet. Assume smooth velocity profile.
C is a fluid element in the region where u is
increasing with increasing y
Marked surface on fluid element C
dydu / :
yxτ :
Forward/Backward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
D is a fluid element in the region where u is
decreasing with increasing y
dydu / :
yxτ :
Forward/Backward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
y
xA
B
D
Flow
Stationary wall
Stationary surrounding fluid far away above the wall
C
Marked surface on fluid element C
dydu / :
yxτ :
Forward/Backward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
Marked surface on fluid element D
dydu / :
yxτ :
Forward/Backward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
y
x
Flow
A
B
C
D
Flow
Stationary plate
Stationary plate
Moving plate, oV
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
5
Problem 4. Velocity Field and Flow Lines [Adapted from Fox et al., 2010, Problem 2.17, p. 45; and from 2145-213 – 2010 HW#1]
Consider the flow described by the velocity field jCyiAtBxV ˆ)(ˆ)1( ++=
v
where A , B , and C are constants and all numerical values in the above expression are dimensionless. 4.1. Is the velocity field steady? 4.2. What are the dimensions of A , B , and C in the system of primary dimensions MLtT? Pathline 4.3. Find the pathline of the particle that is located at the point (xo , yo ) at time to . 4.4. Find the velocity of the above particle at any time t . 4.5. Find the acceleration of the above particle at any time t . Streamline 4.6. Find the streamline that passes through the point (xo , yo ) at time to .
Problem 5. Newton’s Viscosity Law and Shear Stress [Çengel and Cimbala, 2010, Problem 2-75, p. 66.] A 50-cm× 30-cm× 20-cm block weighing 150 N is to be moved at a constant velocity of 0.8 m/s on an inclined
surface with a friction coefficient of 0.27. a) Determine the force F that needs to be applied in the horizontal direction. b) If a 0.4-mm thick oil film with a dynamic viscosity of 0.012 Pa-s is applied between the block and inclined
surface, determine the percent reduction in the required force.
50 cm
30 cm
W = 150 N
F
V = 0.8 m/s
θ = 20o
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
6
Solution
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
7
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field.
Pathlines and streamlines. Newton’s Viscosity Law.
Problem 1. The Principle of Dimensional Homogeneity
A valid physical relation for the change in thermal/internal energy of a substance ( 12 UUU −=Δ ) and the specific heat (at constant volume, c ) can be expressed as
TmcU Δ=Δ where m is the mass of the substance and 12 TTT −=Δ is the change in temperature. 1.1. What are the dimensions of the specific heat c in terms of the primary dimensions
• EAtT (E = Energy, M = Mass, t = time, T = Temperature), and • MLtT (M = Mass, L = Length, t = time, T = Temperature)?
1.2. What should be the physical interpretation of the specific heat c ? Solution
1.1. Tm
UcΔ
Δ= → [ ]
eTemperaturMassEnergy
MTE
TmUc
−==⎥⎦
⎤⎢⎣⎡
ΔΔ
= ANS
→ [ ] 12222
−−−
===⎥⎦⎤
⎢⎣⎡
ΔΔ
= TtLMT
tMLMTE
TmUc ANS
1.2. From [ ]eTemperaturMass
EnergyMTE
TmUc
−==⎥⎦
⎤⎢⎣⎡
ΔΔ
= , c can be interpreted as the quantity that is related to
energy per unit mass per unit change in temperature. ANS
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
8
Problem 2. Field Concept. Classification of Velocity Field. 2.1. Steadiness and Uniformity of the Property Field φ
Let φ be a property whose field representation is ),( txEvφφ = .
We are interested in • the uniformity of the field φ over a region of interest (it can be line, area, or volume) at any one instant, • the steadiness of the field φ over a period of time of interest (and over the region of interest).
Let the shading represent the value of the property φ , say light = high value of φ , dark = low value of φ . Answer the following questions.
(b) Sketch a similar diagram for a uniform but unsteady field. Solution
ANS
ANS
(b)
t t+dt
Uniform but unsteady field
(a)
t t+dt
Over the region of interest, is the property field φ steady over the period of time of interest? Yes At the instant t, is the property field φ uniform over the region of interest? No At the instant t+dt, is the property field φ uniform over the region of interest? No
(a)
t t+dt
Over the region of interest, is the property field φ steady over the period of time of interest? At the instant t, is the property field φ uniform over the region of interest? At the instant t+dt, is the property field φ uniform over the region of interest?
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
9
2.2. Classification of Velocity Field
(a) Fill in the table below. ba, , and c are non-zero, finite constants.
tV ∂∂ /v
Unsteady or Steady ..)(...,...,.VV
vv=
1-, 2-, or 3-dim.
Vvv
×∇=:ω Rotational
or Irrotational
Vv
⋅∇ [a] [b] [c] [d]
A kctjbyiaxV ˆ)(ˆ)(ˆ)( ++=v
kctV ˆ/ =∂∂v
Unsteady ),,( tyxVVvv
= 2 0vv
=×∇ V Irrotational baV +=⋅∇v
1/t 1/t L/t2 -
B ieayV bt ˆ)( 2 −=v
ieaby bt ˆ)( 2 −− Unsteady ),( tyVVvv
= 1 kaye bt ˆ)2( −− Irrotational 0 1/(Lt) 1/t - -
C kcjbyiaxyV ˆ)(ˆ)(ˆ)( +−=v
0v
Steady
),( yxVVvv
= 2 kax ˆ)(− Irrotational bay − 1/(Lt) 1/t L/t -
D ( ) jdicybtaV ˆ)(ˆsin +−=v
( )icybtabV ˆcos −=v
Unsteady
),( tyVV
vv= 1 kcybtac ˆ)cos( − Irrotational 0 L/t 1/t 1/L L/t
(c) Can you initially guess physically what the quantity b in Problem B should be related to? If so, what?
Because of its dimension ( [ b ] = 1/t = frequency), we can guess that b should be related to some kind of frequency. ANS
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
10
2.3. Dimensionality and Functionality of A Velocity Field Assuming that the following velocity fields are steady. State the dimensionality of the fields and write down its
functional relation (e.g., ),,,( tzyxVv
, ),,( tyxVv
, ),( zxVv
, or etc.)
(d) Similar to above, sketch an example of the velocity field in which iyVV x
ˆ)(=v
ANS
x
y
z
1-, 2-, or 3-D? 2-D
),( yxVv
(a)
x
y
z
1-, 2-, or 3-D? 2-D
),( zyVv
(b)
x
y
z
1-, 2-, or 3-D? 3-D
),,( zyxVv
x
y
z
(c)
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
11
Problem 3. Velocity Field and Its Boundary Conditions. Shear deformation and shear stress.
1. Qualitatively sketch the velocity profile along the transverse AB. Be mindful about physical constraints at the solid and free boundaries. Assume for simplicity first that there is only one dominant velocity component.
2. For the marked surface (marked by solid dot) of the fluid element C (and D):
a. state whether the shear deformation (or velocity gradient) dydu / at the point on that surface is positive or negative,
b. state whether yxτ at the point on that surface is positive or negative, and
c. sketch the correct direction of the shear stress yxτ on that surface at that point. d. Also, state whether the fluid element C is being dragged forward (in x+ direction) or dragged backward
(in x− direction) by the fluid element adjacent to it at that surface. 3.1. Flow in a channel with a moving plate in the middle. Assume linear velocity distribution across the gaps.
ANS
Marked surface on fluid element C
dydu / : negative
yxτ : negative
Forward/Backward backward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
Marked surface on fluid element D
dydu / : negative
yxτ : negative
Forward/Backward forward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
y
x
Flow
A
B
C
D
Flow
Stationary plate
Stationary plate
Moving plate, oV oV
C
D
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
12
3.2. Wall jet. Assume smooth velocity profile.
ANS
C is a fluid element in the region where u is
increasing with increasing y
Marked surface on fluid element C
dydu / : positive
yxτ : positive
Forward/Backward backward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
D is a fluid element in the region where u is
decreasing with increasing y
dydu / : negative
yxτ : negative
Forward/Backward forward (Being dragged forward or backward by the fluid element
adjacent to it at that surface?)
y
xA
B
D
Flow
Stationary wall
Stationary surrounding fluid far away above the wall
C
C
D
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
13
Problem 4. Velocity Field and Flow Lines [Adapted from Fox et al., 2010, Problem 2.17, p. 45; and from 2145-213 – 2010 HW#1]
Consider the flow described by the velocity field jCyiAtBxV ˆ)(ˆ)1( ++=
v
where A , B , and C are constants and all numerical values in the above expression are dimensionless. 4.1. Is the velocity field steady? 4.2. What are the dimensions of A , B , and C in the system of primary dimensions MLtT? Pathline 4.3. Find the pathline of the particle that is located at the point (xo , yo ) at time to . 4.4. Find the velocity of the above particle at any time t . 4.5. Find the acceleration of the above particle at any time t . Streamline 4.6. Find the streamline that passes through the point (xo , yo ) at time to . Solution 4.1. Since ),,( tyxVV
vv= [ 0/
vv≠∂∂ tV ], the velocity field is not steady. ANS
4.2. ][A = 1/t, [ B ] = 1/t, and [ C ] = 1/t. ANS Pathline 4.3. Find the pathline of the particle that is located at the point (xo , yo ) at time to.
⎥⎦⎤
⎢⎣⎡ −+−
=
⎥⎦⎤
⎢⎣⎡ −+−=
+=
+=
+==
∫∫
)(2
)(
22
2
)(
22
)(
)(2
)(
2)(ln
)1(
)1(
oo
o
oo
ttAttB
o
oo
t
to
t
t
tx
x
x
extx
ttAttB
tAtBx
tx
dtAtBx
dx
dtAtBxdtVdx
)(
)(
)(
)(
)(ln
o
o
oo
ttCo
o
tt
o
t
t
ty
y
y
eyty
ttC
tCy
ty
Cdty
dy
Cydt
dtVdy
−=
−=
=
=
=
=
∫∫
Thus, the path line is given by
( ) LDimensionjeyiexjtyitxtr ooo ttC
o
ttAttB
o =+⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛=+= −⎥⎦
⎤⎢⎣⎡ −+−
,ˆˆˆ)(ˆ)()( )()(
2)( 22
v . ANS
4.4. Find the velocity of the above particle at any time t . The velocity of the particle in 4.3 can be found as follows. Approach 1: Directly time differentiate the position vector to the pathline.
( ) ( )
( ) ( )jeCyiexAtB
jCeyiAtBexjdt
tdyidt
tdxdt
trdtV
ooo
ooo
ttCo
ttAttB
o
ttCo
ttAttB
o
ˆˆ1
ˆˆ1ˆ)(ˆ)()()(
)()(
2)(
)()(
2)(
22
22
−⎥⎦⎤
⎢⎣⎡ −+−
−⎥⎦⎤
⎢⎣⎡ −+−
+⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛+=
+⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛+=+==
vv
Approach 2: Recognize that 1. the velocity field ),( txV vv
gives the velocity at any point in space at any time t , and 2. the point/location of the particle at any time t is given by the pathline.
Hence, the velocity of the particle )(tVv
is the velocity at the point at which the particle
currently occupies, i.e., )(trx vv= . Thus,
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
14
( ) ( )[ ]
( )jeCyiAteBx
jtyitxtrxjCyiAtBx
txVtV
ooo ttC
o
ttAttB
o
trx
trx
ˆˆ)1(
pathlineˆ)(ˆ)()(,ˆˆ)1(
),()(
)()(
2)(
)(
)(
22
−⎥⎦⎤
⎢⎣⎡ −+−
=
=
+⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛+=
−+==++=
=
vv
vvv
vv
vv
Thus, ( ) VelocityDimensionjeCyiexAtBtV ooo ttC
o
ttAttB
o =+⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛+= −⎥⎦
⎤⎢⎣⎡ −+−
,ˆˆ)1()( )()(
2)( 22v
ANS
4.5. Find the acceleration of the above particle at any time t .
The acceleration of the particle in 2.3 can be found as follows.
( ) [ ]
( ) [ ] onAcceleratiDimensionjeyCiexAtBAB
jeyCieAtBAtAeBx
dttVdta
ooo
ooooo
ttCo
ttAttB
o
ttCo
ttAttBttAttB
o
=+⎥⎥
⎦
⎤
⎢⎢
⎣
⎡++=
+⎥⎥⎥
⎦
⎤
⎢⎢⎢
⎣
⎡
⎟⎟⎟
⎠
⎞
⎜⎜⎜
⎝
⎛+++=
=
−⎥⎦⎤
⎢⎣⎡ −+−
−⎥⎦⎤
⎢⎣⎡ −+−⎥⎦
⎤⎢⎣⎡ −+−
,ˆˆ)1(
ˆˆ1)1()(
)()(
)(2)(
2)(
2
)(2)(
2)()(
2)(
22
2222
vv
ANS Streamline 4.6. Find the streamline that passes through the point (xo , yo ) at time to .
The streamline can be found as follows.
essDimensionlxx
yy
yy
Cxx
AtB
tCydy
AtBxdx
Vdy
Vdx
AtBC
oo
oo
y
y
x
x
yx
oo
)1(
ln1ln)1(
1
timefix,)1(
+
⎟⎟⎠
⎞⎜⎜⎝
⎛=
=+
=+
=
∫∫
ANS Example of a pathline and streamlines that pass through point (1, 1) for this velocity field is shown below.
0
1
2
3
4
5
6
7
8
9
10
0 1 2 3 4 5 6 7 8 9 10
x (m)
y (m
)
Series1Series2Series3
Pathline
Streamline at t = 0 sStreamline at t = 1 s
Pathline
Streamline at t = 0 s
Streamline at t = 1 s
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
15
Problem 5. Newton’s Viscosity Law and Shear Stress [Çengel and Cimbala, 2010, Problem 2-75, p. 66.] A 50-cm× 30-cm× 20-cm block weighing 150 N is to be moved at a constant velocity of 0.8 m/s on an inclined
surface with a friction coefficient of 0.27. a) Determine the force F that needs to be applied in the horizontal direction. b) If a 0.4-mm thick oil film with a dynamic viscosity of 0.012 Pa-s is applied between the block and inclined
surface, determine the percent reduction in the required force.
Solution a)
System: Closed system (material volume MV). We define our system as the solid block only. The system is
shown by the free-body-diagram (FBD) above. Motion: Block moves with constant velocity, no acceleration. Governing Equation: 0
vv=∑F , Nf kμ=
∑ = 0xF : 0sincos =−− θθ WfF (A)
∑ = 0yF : 0cossin =+−− NWF θθ (B)
Nf kμ= (C) Equations (A)-(C) constitute a system of 3 equations in 3 unknonws: F , f , and N .
(B): θθ cossin WFN += (1) (C) → (A): 0sincos =−− θμθ WNF k (2)
(1) → (2):
NN
WF
WFWWFF
oo
ook
k
kk
k
5.105150)20sin27.020(cos)20cos27.020(sin
)sin(cos)cos(sin
)cos(sin)sin(cos0sin)cossin(cos
=××−
×+=
−+
=
+=−=−+−
θμθθμθ
θμθθμθθθθμθ
ANS
Body force W = 150 N
Surface (concentrated point) force F
V = 0.8 m/s
Surface force f , 27.0=kμ
Surface force N
x
y
θ
L = 50 cm
H = 30 cm
W = 150 N
F
V = 0.8 m/s
θ = 20o
2141-365 Fluid Mechanics for International Engineers HW #1: Fundamental concepts: dimensions, field concepts, velocity field. Pathlines and streamlines. Newton’s Viscosity Law Due: Mon, Aug 30, 2010. Drop the homework in the ISE’s course box.
16
(b)
Assumptions 1. Newtonian fluid 2. Velocity filed is steady. 3. Linear velocity distribution over the small gap. 4. μ = constant
System: Oil film
Newton’s viscosity law: (Below, we take Eq. (D) as a tensor equation, taking the signs of components into account.)
Pam
smsPa
hV
hV
dydu
erfaceoilblockyx
24104.0
/8.0012.0
(D)0
3
int
+=×
×⋅=
=−
==
−
−μμμτ
Fluid frictional force (Below, we take Eq. (E) as a tensor equation, taking the signs of components into account.)
NPamWL
Af
yx
yxy
4.2)24)(2.05.0()(
(E)2 +=+×+=+=
=′
τ
τ
Hence, on the oil film f ′ acts in the positive x direction. System: Solid Block
Due to Newton’s third law, f ′ acts on the block in the negative x direction. Since Eq. (A) – with f replaced by f ′ , and F by F ′ - is still applicable, we have
(A): 0sincos =−′−′ θθ WfF
→ NNNWfF o
o2.57
20cos20sin1504.2
cossin
=×+
=+′
=′θ
θ
Thus, the percent reduction in the required force is
%8.45%1005.105
2.575.105%100 =×−
=×′−
=N
NNF
FF ANS
NOTE: The required force is reduced considerably by using oil film.
Body force W = 150 N
Surface (concentrated point) force F ′
V = 0.8 m/s
Surface force f ′
Surface force N ′
x
y
θ
System is solid block
V
Oil film of thickness h
h Adv
System is oil film
yxτ
Surface force f ′