EXAMPLE 6-1 Momentum-Flux Correction Factor for Laminar Pipe Flow Vavg Consider laminar flow through a very long straight section of round pipe. It is shown in Chap. 8 that the velocity profile through a cross-sectional area of the pipe is parabolic (Fig. 6-15), with the axial velocity component given by V = 2V 1 - R2 (1) where R is the radius of the inner wall of the pipe and Vvg is the average velocity. Calculate the momentum-flux correction factor through a cross sec- tion of the pipe for the case in which the pipe flow represents an outlet of the control volume, as sketched in Fig. 6-15. Assumptions 1 The flow is incompressible and steady. 2 The control volume slices through the pipe normal to the pipe axis, as sketched in Fig. 6-15. Analysis We substitute the given velocity profile for V in Eq. 6-24 and inte- grate, noting that dA, = 2mr dr, FIGURE Velocity profile over a cross se of a pipe in which the flow is- developed and lam •R 4 dA 2mr dr R2 (2) TR2 avg Defining a new integration variable y = 1 - r2/R and thus dy = -2r drlR2 (also, y = 1 at r 0, and y = 0 at r = R) and performing the integra- For turbulent flow Bmay h- tion, the momentum-flux correction factor for fully developed laminar flow an insignificant effect at in and outlets, but for laminar flow Bmay be important an (3) should not be neglected. It wise to include Bin all becomes Laminar flow: B = -4 y² dy = -4 Discussion We have calculated B for an outlet, but the same result would have been obtained if we had considered the cross section of the pipe as an inlet to the control volume. momentum control volume problems.
EXAMPLE 6-1 Momentum-Flux Correction Factor for Laminar Pipe Flow Vavg Consider laminar flow through a very long straight section of round pipe. It is shown in Chap. 8 that the velocity profile through a cross-sectional area of the pipe is parabolic (Fig. 6-15), with the axial velocity component given by V = 2V 1 - R2 (1) where R is the radius of the inner wall of the pipe and Vvg is the average velocity. Calculate the momentum-flux correction factor through a cross sec- tion of the pipe for the case in which the pipe flow represents an outlet of the control volume, as sketched in Fig. 6-15. Assumptions 1 The flow is incompressible and steady. 2 The control volume slices through the pipe normal to the pipe axis, as sketched in Fig. 6-15. Analysis We substitute the given velocity profile for V in Eq. 6-24 and inte- grate, noting that dA, = 2mr dr, FIGURE Velocity profile over a cross se of a pipe in which the flow is- developed and lam •R 4 dA 2mr dr R2 (2) TR2 avg Defining a new integration variable y = 1 - r2/R and thus dy = -2r drlR2 (also, y = 1 at r 0, and y = 0 at r = R) and performing the integra- For turbulent flow Bmay h- tion, the momentum-flux correction factor for fully developed laminar flow an insignificant effect at in and outlets, but for laminar flow Bmay be important an (3) should not be neglected. It wise to include Bin all becomes Laminar flow: B = -4 y² dy = -4 Discussion We have calculated B for an outlet, but the same result would have been obtained if we had considered the cross section of the pipe as an inlet to the control volume. momentum control volume problems.
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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Transcribed Image Text:Hello sir, can you solve in detail? How did the
output of 4/3 come out without words, just solve
the question?
EXAMPLE 6-1
Momentum-Flux Correction Factor
for Laminar Pipe Flow
CV
Vavg
Consider laminar flow through a very long straight section of round pipe. It
is shown in Chap. 8 that the velocity profile through a cross-sectional area of
the pipe is parabolic (Fig. 6-15), with the axial velocity component given by
V
R
V = 2Vavg
(1)
R
where R is the radius of the inner wall of the pipe and Vavg is the average
velocity. Calculate the momentum-flux correction factor through a cross sec-
tion of the pipe for the case in which the pipe flow represents an outlet of
the control volume, as sketched in Fig. 6-15.
Assumptions 1 The flow is incompressible and steady. 2 The control volume
slices through the pipe normal to the pipe axis, as sketched in Fig. 6-15.
Analysis We substitute the given velocity profile for V in Eq. 6-24 and inte-
grate, noting that dA. = 2nr dr,
FIGURE 6-
Velocity profile over a cross secti
(2) of a pipe in which the flow is fu
developed and lamin
2
CR
4
dA.
1 -
2mr dr
TR
R2
avg
Defining a new integration variable y = 1 - r2/R2 and thus dy = -2r dr/R2
%3D
(also, y = 1 at r = 0, and y = 0 at r = R) and performing the integra- For turbulent flow Bmay hav
tion, the momentum-flux correction factor for fully developed laminar flow an insignificant effect at inlet
and outlets, but for laminar
flow B may be important and
(3) should not be neglected. It is
wise to include Bin all
%3D
becomes
4.
Laminar flow:
B = -4
dy = -4
3.
Discussion We have calculated B for an outlet, but the same result would momentum control volume
have been obtained if we had considered the cross section of the pipe as an
inlet to the control volume.
problems.
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