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208 Chapter 5 ■ Finite Control Volume Analysis Note that the y component of velocity is positive at section 112 but is negative at section 122. Also, the mass flowrate term is negative at section 1121flow in2 and is positive at section 1221flow out2. From the continuity equation 1Eq. 5.122, we get and thus Eq. 3 can be written as Solving Eq. 5 for m # 1v 1 v 2 2 F Ay p 1 A 1 p 2 A 2 F Ay m # m # 1 m # 2 we obtain F Ay m # 1v 1 v 2 2 p 1 A 1 p 2 A 2 From the given data we can calculate the mass flowrate, m # , from Eq. 5.6 as m # r 1 A 1 v 1 11.94 slugsft 3 210.1 ft 2 2150 fts2 9.70 slugss For determining the anchoring force, F Ay , the effects of atmospheric pressure cancel and thus gage pressures for p 1 and p 2 are appropriate. By substituting numerical values of variables into Eq. 6, and using the fact that 1 lb 1 slug fts 2 we get F Ay 19.70 slugss2150 fts 50 fts2 130 psia 14.7 psia21144 in. 2 ft 2 210.1 ft 2 2 124 psia 14.7 psia21144 in. 2 ft 2 210.1 ft 2 2 F Ay 970 lb 220 lb 134 lb 1324 lb (Ans) F Ay The negative sign for is interpreted as meaning that the y component of the anchoring force is actually in the negative y direction, not the positive y direction as originally indicated in Fig. E5.12b. COMMENT As with Example 5.11, the anchoring force for the pipe bend is independent of the atmospheric pressure. However, the force that the bend puts on the fluid inside of it, R y , (4) (5) (6) depends on the atmospheric pressure. We can see this by using a control volume which surrounds only the fluid within the bend as shown in Fig. E5.12c. Application of the momentum equation to this situation gives R y m # 1v 1 v 2 2 p 1 A 1 p 2 A 2 where p 1 and p 2 must be in terms of absolute pressure because the force between the fluid and the pipe wall, R y , is the complete pressure effect 1i.e., absolute pressure2. We see that forces exerted on the flowing fluid result in a change in its velocity direction 1a change in linear momentum2. Thus, we obtain R y 19.70 slugss2150 fts 50 fts2 130 psia21144 in. 2 ft 2 210.1 ft 2 2 124 psia21144 in. 2 ft 2 210.1 ft 2 2 1748 lb We can use the control volume that includes just the pipe bend 1without the fluid inside it2 as shown in Fig. E5.12d to determine F Ay , the anchoring force component in the y direction necessary to hold the bend stationary. The y component of the momentum equation applied to this control volume gives F Ay R y p atm 1A 1 A 2 2 (8) where R y is given by Eq. 7. The p atm 1A 1 A 2 2 term represents the net pressure force on the outside portion of the control volume. Recall that the pressure force on the inside of the bend is accounted for by R y . By combining Eqs. 7 and 8 and using the fact that p atm 14.7 lbin. 2 1144 in. 2 ft 2 2 2117 lbft 2 , we obtain F Ay 1748 lb 2117 lbft 2 10.1 ft 2 0.1 ft 2 2 1324 lb in agreement with the original answer obtained using the control volume of Fig. E5.12b. (7) z Water in 180° bend R z w p 1 A 1 u v y x p 2 A 2 R y Pipe bend only F Ay R y p atm (A 1 + A 2 ) v 2 v 1 (c) Control volume R x Control volume F I G U R E E5.12 cont. (d) V5.8 Fire hose In Examples 5.10 and 5.12 the force exerted on a flowing fluid resulted in a change in flow direction only. This force was associated with constraining the flow, with a vane in Example 5.10, and with a pipe bend in Example 5.12. In Example 5.11 the force exerted on a flowing fluid resulted in a change in velocity magnitude only. This force was associated with a converging nozzle. Anchoring forces are required to hold a vane or conduit stationary. They are most easily estimated with a control volume that contains the vane or conduit and the flowing fluid involved. Alternately, two separate control volumes can be used, one containing the vane or conduit only and one containing the flowing fluid only.

5.2 Newton’s Second Law—The Linear Momentum and Moment-of-Momentum Equations 209 E XAMPLE 5.13 GIVEN Air flows steadily between two cross sections in a long, straight portion of 4-in. inside diameter pipe as indicated in Fig. E5.13, where the uniformly distributed temperature and pressure at each cross section are given. If the average air velocity at section 122 is 1000 fts, we found in Example 5.2 that the average air velocity at section 112 must be 219 fts. Assume uniform velocity distributions at sections 112 and 122. SOLUTION The control volume of Example 5.2 is appropriate for this problem. The forces acting on the air between sections 112 and 122 are identified in Fig. E5.13. The weight of air is considered negligibly small. The reaction force between the wetted wall of the pipe and the flowing air, R x , is the frictional force sought. Application of the axial component of Eq. 5.22 to this control volume yields The positive x direction is set as being to the right. Furthermore, for uniform velocity distributions 1one-dimensional flow2, Eq. 1 becomes 1u 1 21m # 12 1u 2 21m # 22 R x p 1 A 1 p 2 A 2 (2) From conservation of mass 1Eq. 5.122 we get so that Eq. 2 becomes cs urV nˆ dA R x p 1 A 1 p 2 A 2 Solving Eq. 4 for R x , we get The equation of state gives r 2 p 2 RT 2 and the equation for area A 2 is Thus, from Eqs. 3, 6, and 7 m # m # 1 m # 2 m # 1u 2 u 1 2 R x A 2 1 p 1 p 2 2 R x A 2 1 p 1 p 2 2 m # 1u 2 u 1 2 A 2 pD2 2 4 m # a p 2 RT 2 b a pD2 2 4 b u 2 Linear Momentum—Pressure, Change in Speed, and Friction (1) (3) (4) (5) (6) (7) FIND Determine the frictional force exerted by the pipe wall on the air flow between sections 112 and 122. p 1 A 1 F I G U R E E5.13 English Engineering 1EE2 units are often used for this kind of flow. The gas constant, R, for air in EE units is Thus, from Eqs. 5 and 8 or V Control volume V 2 = 1 1000 ft/s Section (1) p 1 = 100 psia T 1 = 540 °R Pipe R x R 17161ft # lb21slug # °R2 53.31ft # lb21lbm # °R2 32.1741lbmslug2 Hence, m # 118.4 psia21144 in. 2 ft 2 2 353.31ft # lb21lbm # °R24 1453 °R2 p14 in.22 41144 in. 2 ft 2 2 11000 ft s2 9.57 lbms p14 in.22 R x 1100 psia 18.4 psia2 4 19.57 lbm211000 fts 219 fts2 32.1741lbm ft21lb s 2 2 1025 lb 232 lb R x 793 lb p 2 A 2 Section (2) p 2 = 18.4 psia T 2 = 453 °R Flow (8) (Ans) COMMENT For this compressible flow, the pressure difference drives the motion which results in a frictional force, R x , and an acceleration of the fluid (i.e., a velocity magnitude increase). For a similar incompressible pipe flow, a pressure difference results in fluid motion with a frictional force only (i.e., no change in velocity magnitude). y x E XAMPLE 5.14 Linear Momentum—Weight, Pressure, Friction, and Nonuniform Velocity Profile GIVEN upward. Consider the flow of Example 5.4 to be vertically FIND Develop an expression for the fluid pressure drop that occurs between sections 112 and 122.

208 Chapter 5 ■ Finite Control Volume Analysis<br />

Note that the y component of velocity is positive at section 112 but<br />

is negative at section 122. Also, the mass flowrate term is negative<br />

at section 1121flow in2 and is positive at section 1221flow out2. From<br />

the continuity equation 1Eq. 5.122, we get<br />

and thus Eq. 3 can be written as<br />

Solving Eq. 5 for<br />

m # 1v 1 v 2 2 F Ay p 1 A 1 p 2 A 2<br />

F Ay<br />

m # m # 1 m # 2<br />

we obtain<br />

F Ay m # 1v 1 v 2 2 p 1 A 1 p 2 A 2<br />

From the given data we can calculate the mass flowrate, m # , from<br />

Eq. 5.6 as<br />

m # r 1 A 1 v 1 11.94 slugsft 3 210.1 ft 2 2150 fts2<br />

9.70 slugss<br />

For determining the anchoring force, F Ay , the effects of atmospheric<br />

pressure cancel and thus gage pressures for p 1 and p 2 are<br />

appropriate. By substituting numerical values of variables into<br />

Eq. 6, and using the fact that 1 lb 1 slug fts 2 we get<br />

F Ay 19.70 slugss2150 fts 50 fts2<br />

130 psia 14.7 psia21144 in. 2 ft 2 210.1 ft 2 2<br />

124 psia 14.7 psia21144 in. 2 ft 2 210.1 ft 2 2<br />

F Ay 970 lb 220 lb 134 lb 1324 lb (Ans)<br />

F Ay<br />

The negative sign for is interpreted as meaning that the y<br />

component of the anchoring force is actually in the negative y<br />

direction, not the positive y direction as originally indicated in<br />

Fig. E5.12b.<br />

COMMENT As with Example 5.11, the anchoring force for<br />

the pipe bend is independent of the atmospheric pressure. However,<br />

the force that the bend puts on the <strong>fluid</strong> inside of it, R y ,<br />

(4)<br />

(5)<br />

(6)<br />

depends on the atmospheric pressure. We can see this by using a<br />

control volume which surrounds only the <strong>fluid</strong> within the bend as<br />

shown in Fig. E5.12c. Application of the momentum equation to<br />

this situation gives<br />

R y m # 1v 1 v 2 2 p 1 A 1 p 2 A 2<br />

where p 1 and p 2 must be in terms of absolute pressure because<br />

the force between the <strong>fluid</strong> and the pipe wall, R y , is the complete<br />

pressure effect 1i.e., absolute pressure2. We see that forces exerted<br />

on the flowing <strong>fluid</strong> result in a change in its velocity direction 1a<br />

change in linear momentum2.<br />

Thus, we obtain<br />

R y 19.70 slugss2150 fts 50 fts2<br />

130 psia21144 in. 2 ft 2 210.1 ft 2 2<br />

124 psia21144 in. 2 ft 2 210.1 ft 2 2<br />

1748 lb<br />

We can use the control volume that includes just the pipe<br />

bend 1without the <strong>fluid</strong> inside it2 as shown in Fig. E5.12d to<br />

determine F Ay , the anchoring force component in the y direction<br />

necessary to hold the bend stationary. The y component of the<br />

momentum equation applied to this control volume gives<br />

F Ay R y p atm 1A 1 A 2 2<br />

(8)<br />

where R y is given by Eq. 7. The p atm 1A 1 A 2 2 term represents the<br />

net pressure force on the outside portion of the control volume.<br />

Recall that the pressure force on the inside of the bend is accounted<br />

for by R y . By combining Eqs. 7 and 8 and using the fact that<br />

p atm 14.7 lbin. 2 1144 in. 2 ft 2 2 2117 lbft 2 , we obtain<br />

F Ay 1748 lb 2117 lbft 2 10.1 ft 2 0.1 ft 2 2<br />

1324 lb<br />

in agreement with the original answer obtained using the control<br />

volume of Fig. E5.12b.<br />

(7)<br />

z<br />

Water in 180° bend<br />

R z<br />

w p 1<br />

A 1<br />

u v y<br />

x<br />

p 2<br />

A 2<br />

R y<br />

Pipe bend only<br />

F Ay<br />

R y p atm<br />

(A 1 + A 2 )<br />

v 2<br />

v 1<br />

(c)<br />

Control volume<br />

R x<br />

<br />

Control volume<br />

F I G U R E E5.12 cont.<br />

(d)<br />

V5.8 Fire hose<br />

In Examples 5.10 and 5.12 the force exerted on a flowing <strong>fluid</strong> resulted in a change in flow<br />

direction only. This force was associated with constraining the flow, with a vane in Example 5.10,<br />

and with a pipe bend in Example 5.12. In Example 5.11 the force exerted on a flowing <strong>fluid</strong><br />

resulted in a change in velocity magnitude only. This force was associated with a converging<br />

nozzle. Anchoring forces are required to hold a vane or conduit stationary. They are most easily<br />

estimated with a control volume that contains the vane or conduit and the flowing <strong>fluid</strong> involved.<br />

Alternately, two separate control volumes can be used, one containing the vane or conduit only<br />

and one containing the flowing <strong>fluid</strong> only.

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