iðhal flow, Nondimensionalize the continuity and Navier-Stokes equations (for tw momentum only). Review section 7.10 in the text. Start from Eqs. (7.28) and (7.29). Consider the reference scales for velocity, length, time, and pressure to be: U, L, L/U, pƯ², respectively. Show all work. . Comment on the significance of the result in terms of the concept of Similarity. Why is the Reynolds number so prevalent in characterizing the behavior of flows? c. Review sections 7.1-7.3, which considers as an example, pressure drop (per unit length) for flow through a smooth pipe. 1. Consider SAE 10W oil at 77°F flowing through a l-in. diameter horizontal pipe, at an average speed of 3 ft/s, produces a pressure drop of 7 psi over a 500-ft length. Water at 60°F flows through the same pipe under dynamically similar conditions. Using the text results reviewed in

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a. Nondimensionalize the continuity and Navier-Stokes equations (for two-dimensional flow, x-
momentum only). Review section 7.10 in the text. Start from Eqs. (7.28) and (7.29). Consider
the reference scales for velocity, length, time, and pressure to be: U, L, L/U, pU², respectively.
Show all work.
b. Comment on the significance of the result in terms of the concept of Similarity. Why is the
Reynolds number so prevalent in characterizing the behavior of flows?
c. Review sections 7.1-7.3, which considers as an example, pressure drop (per unit length) for flow
through a smooth pipe.
d. Consider SAE 10W oil at 77°F flowing through a 1-in. diameter horizontal pipe, at an average
speed of 3 ft/s, produces a pressure drop of 7 psi over a 500-ft length. Water at 60°F flows
through the same pipe under dynamically similar conditions. Using the text results reviewed in
c., determine the average speed of the water flow [ft/s] and the corresponding pressure drop [psi].
Transcribed Image Text:a. Nondimensionalize the continuity and Navier-Stokes equations (for two-dimensional flow, x- momentum only). Review section 7.10 in the text. Start from Eqs. (7.28) and (7.29). Consider the reference scales for velocity, length, time, and pressure to be: U, L, L/U, pU², respectively. Show all work. b. Comment on the significance of the result in terms of the concept of Similarity. Why is the Reynolds number so prevalent in characterizing the behavior of flows? c. Review sections 7.1-7.3, which considers as an example, pressure drop (per unit length) for flow through a smooth pipe. d. Consider SAE 10W oil at 77°F flowing through a 1-in. diameter horizontal pipe, at an average speed of 3 ft/s, produces a pressure drop of 7 psi over a 500-ft length. Water at 60°F flows through the same pipe under dynamically similar conditions. Using the text results reviewed in c., determine the average speed of the water flow [ft/s] and the corresponding pressure drop [psi].
distorted model flows and the real thing.
7.10
Similitude Based on Governing Differential Equations
Similarity laws
can be directly
developed from
the equations
governing the
phenomenon of
In the preceding sections of this chapter, dimensional analysis has been used to obtain similarity
laws. This is a simple, straightforward approach to modeling, which is widely used. The use of
dimensional analysis requires only a knowledge of the variables that influence the phenomenon of
interest. Although the simplicity of this approach is attractive, it must be recognized that omission
of one or more important variables may lead to serious errors in the model design. An alternative
approach is available if the equations (usually differential equations) governing the phenomenon are
known. In this situation similarity laws can be developed from the governing equations, even though
it may not be possible to obtain analytic solutions to the equations.
To illustrate the procedure, consider the flow of an incompressible Newtonian fluid. For
simplicity we will restrict our attention to two-dimensional flow, although the results are applicable
to the general three-dimensional case. From Chapter 6 we know that the governing equations are
the continuity equation
interest.
ди
do
+
= 0
ду
(7.28)
dx
and the Navier-Stokes equations
ди
ди
др
ди
+ u
dt
(7.29)
--
dx
dx
do
др
Pg + u
ду
dv
dv
+ u
+ v
+
(7.30)
д
ду
dx² ™ dy²,
дх
where the y axis is vertical, so that the gravitational body force, pg, only appears in the “y equation."
To continue the mathematical description of the problem, boundary conditions are required. For
example, velocities on all boundaries may be specified; that is, u = ug and v = vg at all boundary
points x = xg and y = yg. In some types of problems it may be necessary to specify the pressure
over some part of the boundary. For time-dependent problems, initial conditions would also have to
be provided, which means that the values of all dependent variables would be given at some time
(usually taken at t = 0).
Transcribed Image Text:distorted model flows and the real thing. 7.10 Similitude Based on Governing Differential Equations Similarity laws can be directly developed from the equations governing the phenomenon of In the preceding sections of this chapter, dimensional analysis has been used to obtain similarity laws. This is a simple, straightforward approach to modeling, which is widely used. The use of dimensional analysis requires only a knowledge of the variables that influence the phenomenon of interest. Although the simplicity of this approach is attractive, it must be recognized that omission of one or more important variables may lead to serious errors in the model design. An alternative approach is available if the equations (usually differential equations) governing the phenomenon are known. In this situation similarity laws can be developed from the governing equations, even though it may not be possible to obtain analytic solutions to the equations. To illustrate the procedure, consider the flow of an incompressible Newtonian fluid. For simplicity we will restrict our attention to two-dimensional flow, although the results are applicable to the general three-dimensional case. From Chapter 6 we know that the governing equations are the continuity equation interest. ди do + = 0 ду (7.28) dx and the Navier-Stokes equations ди ди др ди + u dt (7.29) -- dx dx do др Pg + u ду dv dv + u + v + (7.30) д ду dx² ™ dy², дх where the y axis is vertical, so that the gravitational body force, pg, only appears in the “y equation." To continue the mathematical description of the problem, boundary conditions are required. For example, velocities on all boundaries may be specified; that is, u = ug and v = vg at all boundary points x = xg and y = yg. In some types of problems it may be necessary to specify the pressure over some part of the boundary. For time-dependent problems, initial conditions would also have to be provided, which means that the values of all dependent variables would be given at some time (usually taken at t = 0).
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