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Modern Engineering Thermodynamics

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8.3 Systems Undergoing Irreversible Processes 259<br />

Exercises<br />

9. If the surface temperature of the bulb in Example 8.6 were 40.0°C (which is typical of a fluorescent light), determine the<br />

entropy production rate of the bulb. Answer: _S p = 0:319 W=K:<br />

10. Take _U = 100: watts, T 0 = T b = 110:°C, and for a glass bulb take m = 0.050 kg and c = 0.80 kJ/kg · K. Then, using the<br />

last expression in Example 8.6 for the decay in entropy production rate for an insulated lightbulb, determine the entropy<br />

production rate at t = 0, 300., 600., and 1000. s. Answers: _S p = 0:26, 0:088, 0:053, and 0:035 W=K:<br />

EXAMPLE 8.7 A CONTINUATION OF EXAMPLE 5.3, WITH<br />

THE ADDITION SHOWN IN ITALIC TYPE<br />

A basic vapor cycle power plant consists of the following four parts:<br />

a. The boiler, where high-pressure vapor is produced.<br />

b. The turbine, where energy is removed from the high-pressure vapor as shaft work.<br />

c. The condenser, where the low-pressure vapor leaving the turbine is condensed into a liquid.<br />

d. The boiler feed pump, which pumps the condensed liquid back into the high-pressure boiler for reheating.<br />

In such a power plant, the boiler receives 950. × 10 5 kJ/h from the burning fuel, and the condenser rejects 600. × 10 5 kJ/h<br />

to the environment. The boiler feed pump requires 23.0 kW input, which it receives directly from the turbine. Assuming<br />

that the turbine, pump, and connecting pipes are all insulated, determine the net power of the turbine and the rate of entropy<br />

production of the plant if the boiler temperature is 500.°C and the condenser temperature is 10.0°C.<br />

Solution<br />

First, draw a sketch of the system (Figure 8.7).<br />

Q B = 950. × 10 5 kJ/h<br />

T B = 500.°C<br />

S P = ?<br />

Boiler<br />

Boiler<br />

feed<br />

pump<br />

W p =−23.0 kW<br />

Turbine<br />

(W T )net = ?<br />

Condenser<br />

Q c =−600. × 10 5 kJ/h<br />

T c = 10.0°C<br />

System<br />

boundary<br />

FIGURE 8.7<br />

Example 8.7.<br />

The unknowns here are _W T<br />

net and _S P for the entire power plant. Therefore, the system is the entire power plant. Since we<br />

have few specific details on the internal operation of the plant, the thermodynamic properties within the power plant are<br />

apparently not needed in the solution.<br />

The net turbine work output is determined in Example 5.3 to be<br />

_W T<br />

net<br />

= 9720 kW<br />

The answer to the second part of this problem can be obtained by the indirect method from Eq. (8.2) as<br />

_S P = _S − d Z <br />

dQ<br />

dt T b<br />

Σ<br />

act<br />

(Continued )

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