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Page1
M.Bahrami ENSC 283 Assignment # 1
ENSC-283
Assignment #1
Assignment date: Monday Jan. 12, 2009
Due date: Monday Jan. 19, 2009
Problem: (Newtonian fluid shear stress)
The velocity distribution for the flow of a Newtonian fluid between two wide,
parallel plates (see Figure) is given by the equation
𝑢 =
3𝑈 𝑚
2
[1 − (
𝑦
ℎ
)
2
]
where 𝑈 𝑚 is the mean velocity. The fluid has the viscosity of 0.04 𝑙𝑏. 𝑠/𝑓𝑡2
. If
𝑈 𝑚 = 2 𝑓𝑡/𝑠 and ℎ = 0.2 in, determine:
(a) The shearing stress acting on the bottom wall.
(b)The shearing stress acting on a plane parallel to the walls and passing
through the centerline (midplane).
𝑦ℎ
ℎ
𝑢
Page2
M.Bahrami ENSC 283 Assignment # 1
Solution
For this type of parallel flow the shearing stress is obtained from
𝜏 = 𝜇
𝑑𝑢
𝑑𝑦
(1)
Thus, if the velocity distribution 𝑢 = 𝑢(𝑦) is known, the shearing stress can be
determined at all points by evaluating the velocity gradient, 𝑑𝑢/𝑑𝑦. For the
distribution given
𝑑𝑢
𝑑𝑦
= −
3𝑈𝑦
ℎ2
(2)
(a)The bottom wall𝑦 = −ℎ so that
𝑑𝑢
𝑑𝑦
=
3𝑈
ℎ
(3)
And therefore the shearing stress is
𝜏 𝑏𝑜𝑡𝑡𝑜𝑚 𝑤𝑎𝑙𝑙 = 𝜇 (
3𝑈
ℎ
) =
(0.04 𝑙𝑏.
𝑠
𝑓𝑡2)(3)(2
𝑓𝑡
𝑠
)
(0.2 𝑖𝑛.)(1
𝑓𝑡
12𝑖𝑛.
)
= 14.4 𝑙𝑏/𝑓𝑡2
(𝑖𝑛 𝑑𝑖𝑟𝑒𝑐𝑡𝑖𝑜𝑛 𝑜𝑓 𝑓𝑙𝑜𝑤)
This stress creates a drag on the wall. Since the velocity distribution is
symmetrical, the shearing stress along the upper wall would have the same
magnitude and direction.
(b)Along the midplane where 𝑦 = 0 it follows from Eq. (2) that
𝑑𝑢
𝑑𝑦
= 0 (4)
Always use units in your calculations
Page3
M.Bahrami ENSC 283 Assignment # 1
And thus the shearing stress is
𝜏 𝑚𝑖𝑑𝑝𝑙𝑎𝑛𝑒 = 0
Note (1):
In this problem, we calculated the shearing stress acting on the walls. Same
shearing stress but in the opposite direction is acting on the fluid. Why?
Note (2):
From Eq. (2) we see that the velocity gradient is a linear function of y i.e. 𝜏 = 𝛼𝑦
with 𝛼 = −3𝑈/ℎ2
. Hence, the shearing stress (see Eq. (1)) varies linearly with y
and in this particular problem varies from 0 at the center of the channel to
14.4 𝑙𝑏/𝑓𝑡2
at the walls. For the more general case, the actual variation will
depend on the nature of the velocity distribution.
𝜏,𝑙𝑏/𝑓𝑡2
15
10
5
0
-0.2 -0.1 0 0.1 0.2
y, in
𝜏 𝑤𝑎𝑙𝑙 = 14.4 𝑙𝑏. 𝑓𝑡2
𝜏 𝑚𝑖𝑑𝑝𝑙𝑎𝑛𝑒 = 0

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Assignment1 solution

  • 1. Page1 M.Bahrami ENSC 283 Assignment # 1 ENSC-283 Assignment #1 Assignment date: Monday Jan. 12, 2009 Due date: Monday Jan. 19, 2009 Problem: (Newtonian fluid shear stress) The velocity distribution for the flow of a Newtonian fluid between two wide, parallel plates (see Figure) is given by the equation 𝑢 = 3𝑈 𝑚 2 [1 − ( 𝑦 ℎ ) 2 ] where 𝑈 𝑚 is the mean velocity. The fluid has the viscosity of 0.04 𝑙𝑏. 𝑠/𝑓𝑡2 . If 𝑈 𝑚 = 2 𝑓𝑡/𝑠 and ℎ = 0.2 in, determine: (a) The shearing stress acting on the bottom wall. (b)The shearing stress acting on a plane parallel to the walls and passing through the centerline (midplane). 𝑦ℎ ℎ 𝑢
  • 2. Page2 M.Bahrami ENSC 283 Assignment # 1 Solution For this type of parallel flow the shearing stress is obtained from 𝜏 = 𝜇 𝑑𝑢 𝑑𝑦 (1) Thus, if the velocity distribution 𝑢 = 𝑢(𝑦) is known, the shearing stress can be determined at all points by evaluating the velocity gradient, 𝑑𝑢/𝑑𝑦. For the distribution given 𝑑𝑢 𝑑𝑦 = − 3𝑈𝑦 ℎ2 (2) (a)The bottom wall𝑦 = −ℎ so that 𝑑𝑢 𝑑𝑦 = 3𝑈 ℎ (3) And therefore the shearing stress is 𝜏 𝑏𝑜𝑡𝑡𝑜𝑚 𝑤𝑎𝑙𝑙 = 𝜇 ( 3𝑈 ℎ ) = (0.04 𝑙𝑏. 𝑠 𝑓𝑡2)(3)(2 𝑓𝑡 𝑠 ) (0.2 𝑖𝑛.)(1 𝑓𝑡 12𝑖𝑛. ) = 14.4 𝑙𝑏/𝑓𝑡2 (𝑖𝑛 𝑑𝑖𝑟𝑒𝑐𝑡𝑖𝑜𝑛 𝑜𝑓 𝑓𝑙𝑜𝑤) This stress creates a drag on the wall. Since the velocity distribution is symmetrical, the shearing stress along the upper wall would have the same magnitude and direction. (b)Along the midplane where 𝑦 = 0 it follows from Eq. (2) that 𝑑𝑢 𝑑𝑦 = 0 (4) Always use units in your calculations
  • 3. Page3 M.Bahrami ENSC 283 Assignment # 1 And thus the shearing stress is 𝜏 𝑚𝑖𝑑𝑝𝑙𝑎𝑛𝑒 = 0 Note (1): In this problem, we calculated the shearing stress acting on the walls. Same shearing stress but in the opposite direction is acting on the fluid. Why? Note (2): From Eq. (2) we see that the velocity gradient is a linear function of y i.e. 𝜏 = 𝛼𝑦 with 𝛼 = −3𝑈/ℎ2 . Hence, the shearing stress (see Eq. (1)) varies linearly with y and in this particular problem varies from 0 at the center of the channel to 14.4 𝑙𝑏/𝑓𝑡2 at the walls. For the more general case, the actual variation will depend on the nature of the velocity distribution. 𝜏,𝑙𝑏/𝑓𝑡2 15 10 5 0 -0.2 -0.1 0 0.1 0.2 y, in 𝜏 𝑤𝑎𝑙𝑙 = 14.4 𝑙𝑏. 𝑓𝑡2 𝜏 𝑚𝑖𝑑𝑝𝑙𝑎𝑛𝑒 = 0