fluid_mechanics
438 Chapter 8 ■ Viscous Flow in Pipes standard electrical engineering methods can be carried over to help solve fluid mechanics problems, others cannot. One of the simplest multiple pipe systems is that containing pipes in series, as is shown in Fig. 8.35a. Every fluid particle that passes through the system passes through each of the pipes. Thus, the flowrate 1but not the velocity2 is the same in each pipe, and the head loss from point A to point B is the sum of the head losses in each of the pipes. The governing equations can be written as follows: and Q 1 Q 2 Q 3 Series and parallel pipe systems are often encountered. where the subscripts refer to each of the pipes. In general, the friction factors will be different for each pipe because the Reynolds numbers 1Re i rV i D im2 and the relative roughnesses 1e iD i 2 will be different. If the flowrate is given, it is a straightforward calculation to determine the head loss or pressure drop 1Type I problem2. If the pressure drop is given and the flowrate is to be calculated 1Type II problem2, an iteration scheme is needed. In this situation none of the friction factors, are known, so the calculations may involve more trial-and-error attempts than for corresponding single pipe systems. The same is true for problems in which the pipe diameter 1or diameters2 is to be determined 1Type III problems2. Another common multiple pipe system contains pipes in parallel, as is shown in Fig. 8.35b. In this system a fluid particle traveling from A to B may take any of the paths available, with the total flowrate equal to the sum of the flowrates in each pipe. However, by writing the energy equation between points A and B it is found that the head loss experienced by any fluid particle traveling between these locations is the same, independent of the path taken. Thus, the governing equations for parallel pipes are and h LA – B h L1 h L2 h L3 Q Q 1 Q 2 Q 3 f i , h L1 h L2 h L3 Again, the method of solution of these equations depends on what information is given and what is to be calculated. Another type of multiple pipe system called a loop is shown in Fig. 8.36. In this case the flowrate through pipe 112 equals the sum of the flowrates through pipes 122 and 132, or Q 1 Q 2 Q 3 . As can be seen by writing the energy equation between the surfaces of each reservoir, the head loss for pipe 122 must equal that for pipe 132, even though the pipe sizes and flowrates may be different for each. That is, p A g V 2 A 2g z A p B g V 2 B 2g z B h L1 h L2 for a fluid particle traveling through pipes 112 and 122, while p A g V 2 A 2g z A p B g V 2 B 2g z B h L1 h L3 A B Node, N (2) Q 2 (1) V 2 V 1 V 3 (3) Q 3 Q 1 D 1 D 2 D 3 F I G U R E 8.36 Multiple pipe loop system.
8.5 Pipe Flow Examples 439 A B D 1 , 1 D 2 , 2 D 3 , 3 (1) (2) C (3) F I G U R E 8.37 A three-reservoir system. For some pipe systems, the direction of flow is not known a priori. for fluid that travels through pipes 112 and 132. These can be combined to give h L2 h L3 . This is a statement of the fact that fluid particles that travel through pipe 122 and particles that travel through pipe 132 all originate from common conditions at the junction 1or node, N2 of the pipes and all end up at the same final conditions. The flow in a relatively simple looking multiple pipe system may be more complex than it appears initially. The branching system termed the three-reservoir problem shown in Fig. 8.37 is such a system. Three reservoirs at known elevations are connected together with three pipes of known properties 1lengths, diameters, and roughnesses2. The problem is to determine the flowrates into or out of the reservoirs. If valve 112 were closed, the fluid would flow from reservoir B to C, and the flowrate could be easily calculated. Similar calculations could be carried out if valves 122 or 132 were closed with the others open. With all valves open, however, it is not necessarily obvious which direction the fluid flows. For the conditions indicated in Fig. 8.37, it is clear that fluid flows from reservoir A because the other two reservoir levels are lower. Whether the fluid flows into or out of reservoir B depends on the elevation of reservoirs B and C and the properties 1length, diameter, roughness2 of the three pipes. In general, the flow direction is not obvious, and the solution process must include the determination of this direction. This is illustrated in Example 8.14. E XAMPLE 8.14 Three-Reservoir, Multiple-Pipe System GIVEN Three reservoirs are connected by three pipes as are shown in Fig. E8.14. For simplicity we assume that the diameter of each pipe is 1 ft, the friction factor for each is 0.02, and because of the large length-to-diameter ratio, minor losses are negligible. A Elevation = 100 ft D 1 = 1 ft (1) 1 = 1000 ft FIND SOLUTION Determine the flowrate into or out of each reservoir. It is not obvious which direction the fluid flows in pipe 122. However, we assume that it flows out of reservoir B, write the governing equations for this case, and check our assumption. The continuity equation requires that which, since the diameters are the same for each pipe, becomes simply V 1 V 2 V 3 Q 1 Q 2 Q 3 , The energy equation for the fluid that flows from A to C in pipes 112 and 132 can be written as p A g V 2 A 2g z A p C g V 2 C 2g z C f / 1 V 2 1 1 D 1 2g f / 3 V 2 3 3 D 3 2g (1) F I G U R E E8.14 By using the fact that p A p C V A V C z C 0, this becomes For the given conditions of this problem we obtain 100 ft D 3 = 1 ft 3 = 400 ft z A f / 1 V 2 1 1 D 1 2g f / 3 V 2 3 3 D 3 2g 0.02 2132.2 fts 2 2 D 2 = 1 ft 2 = 500 ft (3) (2) Elevation = 20 ft Elevation = 0 ft 1 11 ft2 311000 ft2V 2 1 1400 ft2V 2 34 C B
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8.5 Pipe Flow Examples 439<br />
A<br />
B<br />
D 1 , 1<br />
D 2 , 2<br />
D 3 , 3<br />
(1)<br />
(2)<br />
C<br />
(3)<br />
F I G U R E 8.37<br />
A three-reservoir system.<br />
For some pipe systems,<br />
the direction<br />
of flow is not<br />
known a priori.<br />
for <strong>fluid</strong> that travels through pipes 112 and 132. These can be combined to give h L2<br />
h L3<br />
. This is a<br />
statement of the fact that <strong>fluid</strong> particles that travel through pipe 122 and particles that travel through<br />
pipe 132 all originate from common conditions at the junction 1or node, N2 of the pipes and all end<br />
up at the same final conditions.<br />
The flow in a relatively simple looking multiple pipe system may be more complex than<br />
it appears initially. The branching system termed the three-reservoir problem shown in Fig. 8.37<br />
is such a system. Three reservoirs at known elevations are connected together with three pipes<br />
of known properties 1lengths, diameters, and roughnesses2. The problem is to determine the<br />
flowrates into or out of the reservoirs. If valve 112 were closed, the <strong>fluid</strong> would flow from<br />
reservoir B to C, and the flowrate could be easily calculated. Similar calculations could be<br />
carried out if valves 122 or 132 were closed with the others open.<br />
With all valves open, however, it is not necessarily obvious which direction the <strong>fluid</strong> flows.<br />
For the conditions indicated in Fig. 8.37, it is clear that <strong>fluid</strong> flows from reservoir A because the<br />
other two reservoir levels are lower. Whether the <strong>fluid</strong> flows into or out of reservoir B depends<br />
on the elevation of reservoirs B and C and the properties 1length, diameter, roughness2 of the<br />
three pipes. In general, the flow direction is not obvious, and the solution process must include<br />
the determination of this direction. This is illustrated in Example 8.14.<br />
E XAMPLE 8.14<br />
Three-Reservoir, Multiple-Pipe System<br />
GIVEN Three reservoirs are connected by three pipes as are<br />
shown in Fig. E8.14. For simplicity we assume that the diameter<br />
of each pipe is 1 ft, the friction factor for each is 0.02, and<br />
because of the large length-to-diameter ratio, minor losses are<br />
negligible.<br />
A<br />
Elevation = 100 ft<br />
D 1 = 1 ft<br />
(1) 1 = 1000 ft<br />
FIND<br />
SOLUTION<br />
Determine the flowrate into or out of each reservoir.<br />
It is not obvious which direction the <strong>fluid</strong> flows in pipe 122.<br />
However, we assume that it flows out of reservoir B, write the<br />
governing equations for this case, and check our assumption.<br />
The continuity equation requires that<br />
which,<br />
since the diameters are the same for each pipe, becomes simply<br />
V 1 V 2 V 3<br />
Q 1 Q 2 Q 3 ,<br />
The energy equation for the <strong>fluid</strong> that flows from A to C in pipes<br />
112 and 132 can be written as<br />
p A<br />
g V 2 A<br />
2g z A p C<br />
g V 2 C<br />
2g z C f / 1 V 2 1<br />
1<br />
D 1 2g f / 3 V 2 3<br />
3<br />
D 3 2g<br />
(1)<br />
F I G U R E E8.14<br />
By using the fact that p A p C V A V C z C 0, this becomes<br />
For the given conditions of this problem we obtain<br />
100 ft <br />
D 3 = 1 ft<br />
3 = 400 ft<br />
z A f / 1 V 2 1<br />
1<br />
D 1 2g f / 3 V 2 3<br />
3<br />
D 3 2g<br />
0.02<br />
2132.2 fts 2 2<br />
D 2 = 1 ft<br />
2 = 500 ft<br />
(3)<br />
(2)<br />
Elevation =<br />
20 ft<br />
Elevation =<br />
0 ft<br />
1<br />
11 ft2 311000 ft2V 2 1 1400 ft2V 2 34<br />
C<br />
B