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Modern Engineering Thermodynamics

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312 CHAPTER 9: Second Law Open System Applications<br />

heat exchanger while it absorbs heat from the environment. At<br />

the outlet, the pressure is 1.00 MPa. Determine (a) the heat<br />

transfer rate, and (b) the entropy production rate. (c) Show<br />

whether this device violates the second law of thermodynamics.<br />

Assume that the system boundary temperature is isothermal<br />

at 200.°C.<br />

27. A contact feedwater heat exchanger for heating the water going<br />

into a boiler operates on the principle of mixing steam with<br />

liquid water. For the steady flow adiabatic process shown in<br />

Figure 9.25, calculate<br />

a. The rate of change of entropy of the entire heater.<br />

b. The rate of entropy production inside the heater.<br />

p = 100. psia<br />

x = 0.98<br />

p = 100 psia<br />

T = 80.0°F<br />

FIGURE 9.25<br />

Problem 27.<br />

Steam<br />

Water<br />

Feedwater<br />

heater<br />

Water<br />

m = 25.0 × 10 3 lbm/h<br />

p = 100. psia<br />

T = 80.0°F<br />

28. As an engineering consultant, you are asked to review a design<br />

proposal in which an electric resistance heater is to be used in<br />

conjunction with a precision air bearing (Figure 9.26). The<br />

heater uses 100 W of electrical power and the air bearing has a<br />

constant surface temperature of 160.°F. The heater is well<br />

insulated on the outside and air enters the bearing at 40.0°F,<br />

35.0 psia and exits at 80.0°F , 40.0 psia. The bearing is a steady<br />

flow, steady state device with an air flow rate of 35.55 lbm/h.<br />

Determine<br />

a. Whether this device violates the first law of thermodynamics.<br />

b. Whether this device violates the second law of<br />

thermodynamics.<br />

Air inlet<br />

40.0°F<br />

35.0 psia<br />

FIGURE 9.26<br />

Problem 28.<br />

160.°F<br />

Air outlet<br />

80.0°F<br />

40.0 psia<br />

100. watt<br />

Resistance heater<br />

29.* A slide projector contains a 500. W lightbulb cooled by an<br />

internal fan that blows room air across the bulb at a rate of<br />

1.00 kg/min. If the equilibrium surface temperature of the<br />

bulb is 350.°C and the inlet temperature (the room air) is at<br />

20.0°C, then determine (a) the outlet temperature of the<br />

cooling air and (b) the rate of entropy production in the air<br />

passing through the projector. Assume the air is an ideal gas<br />

with constant specific heats and that it undergoes an aergonic<br />

process.<br />

30. Determine the total entropy production rate for the heat<br />

exchanger shown in Figure 9.27. In addition to the air-water<br />

heat transfer within the heat exchanger, the air also loses an<br />

unknown amount of heat to the surroundings while the water<br />

receives an additional 10.0 Btu/s from the surroundings. Assume<br />

the internal air-water interface is isothermal at 100.°F and the<br />

outer surface of the heat exchanger is isothermal at 70.0°F.<br />

Neglect all flow stream pressure losses.<br />

140.°F<br />

Air<br />

35.0°F<br />

Water<br />

FIGURE 9.27<br />

Problem 30.<br />

100. °F<br />

T b = 70.0°F<br />

Q air = ?<br />

Air−water<br />

interface<br />

Q water = 10.0 Btu/s<br />

110.°F<br />

78.5°F<br />

m air = 100. lbm/s<br />

m water = 16.3 lbm/s<br />

31.* A new Yo Yo Dyne propulsion system has three flow streams,<br />

as shown in Figure 9.28. It mixes 0.500 kg/s of saturated water<br />

vapor at 100.°F with 0.200 kg/s of saturated liquid water at<br />

100.°C in a steady flow, steady state, isobaric process. This<br />

system is cheaply made and uninsulated; consequently, it loses<br />

heat at the rate of 75.0 kJ/s to the surroundings. Assuming the<br />

system boundary temperature is isothermal at 100.°C, determine<br />

a. The quality of the outlet mixture.<br />

b. The entropy production rate of the system.<br />

Sat. liq.<br />

0.200 kg/s<br />

at 100.°C<br />

Sat. vap.<br />

0.500 kg/s<br />

at 100.°C)<br />

FIGURE 9.28<br />

Problem 31.<br />

Vapor−mixer<br />

incorporated<br />

W = 1.00 hp<br />

(power to the mixing blades)<br />

Q = 75.0 kJ/s<br />

Mixture<br />

x =?<br />

32.* In a steady flow, adiabatic, aergonic desuperheater (a kind of<br />

mixing heat exchanger), water is sprayed into superheated steam<br />

in the proper amount to cause the superheated steam to become<br />

saturated.<br />

a. Calculate the mass flow rate of water necessary for<br />

desuperheating.<br />

b. What is the entropy production rate of this system?<br />

c. Show whether this process violates the second law of<br />

thermodynamics.<br />

Given that<br />

■ Steam mass flow rate = 200. kg/h.<br />

■ Steam entering state = 10.0 MPa, 600.°C.<br />

■ Water entering state = 10.0 MPa, 100.°C.<br />

■ Steam outlet state = 10.0 MPa, saturated vapor.<br />

33. A steady state, steady flow steam mixer consists of a box with<br />

two inlet pipes and one outlet pipe. One inlet pipe carries<br />

saturated water vapor at 50.0 lbm/s and 20.0 psia. The other<br />

inlet pipe carries saturated liquid water at 10.0 lbm/s and 20.0<br />

psia. The mixing process is isobaric. In addition, 9602 Btu/s of

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