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Modern Engineering Thermodynamics

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260 CHAPTER 8: Second Law Closed System Applications<br />

EXAMPLE 8.7 (Continued )<br />

The surface area of our system can be divided into three major parts: the boiler’s surface area, the condenser’s surfacearea,<br />

and all the remaining surface areas. Therefore, the surface area Σ system of the system is composed of the boiler, the condenser,<br />

and everything else, or<br />

∑ system<br />

= ∑ boiler<br />

+∑ condenser<br />

+∑ everything else<br />

Now, both the boiling and the condensing processes are isothermal phase changes; and since no heat transfer occurs at any<br />

other point in the system, we can write<br />

Z<br />

d dQ<br />

= d dt Σ T b dt<br />

Z<br />

Σ boiler<br />

dQ<br />

T b<br />

+<br />

Z<br />

Σ condenser<br />

dQ<br />

T b<br />

+<br />

Z<br />

!<br />

dQ<br />

Σ T b remainder<br />

where<br />

and<br />

Z<br />

d dQ<br />

=<br />

dt Σ T b boiler<br />

Z<br />

d dQ<br />

=<br />

dt Σ T b condenser<br />

_Q boiler<br />

T boiler<br />

_Q condenser<br />

T condenser<br />

Z<br />

d<br />

dQ<br />

= 0 ðno heat transfer across the remaining surface areaÞ<br />

dt Σ T b remainder<br />

Then, we have<br />

_S P = _S −<br />

and, for steady state operation ð _S = 0Þ, this reduces to<br />

_Q boiler<br />

T boiler<br />

−<br />

_Q condenser<br />

T condenser<br />

!<br />

_Q<br />

_S p = − boiler<br />

_Q<br />

+ condenser<br />

T boiler<br />

T condenser<br />

<br />

<br />

950: × 10<br />

= −<br />

5 − 600: × 105 kJ/h<br />

+<br />

500: + 273:15 10:0 + 273:15 K<br />

Note that the actual thermal efficiency of this power plant is given by Eq. (7.9) as<br />

= 89:0 × 10 3 kJ/ ðh⋅KÞ<br />

ðη T Þ act<br />

= 1 − j _Q out j<br />

= 1 −<br />

600: × 105<br />

= 0:368 = 36:8%<br />

5 _Q in 950: × 10<br />

whereas its theoretical reversible (Carnot) efficiency is given by Eq. (7.16) as<br />

ðη T Þ rev<br />

= 1 − T condenser<br />

= 1 −<br />

10:0 + 273:15<br />

= 0:634 = 63:4%<br />

T boiler 500: + 273:15<br />

Therefore, the actual efficiency is less than the theoretical maximum (reversible) efficiency, as it should be.<br />

Exercises<br />

11. Determine the condenser temperature that would cause the entropy production rate of the power plant in Example 8.7<br />

to be 500. kJ/h·K. Answer: T condenser = 486 K = 213°C.<br />

12. Determine the condenser temperature that would cause the entropy production rate of the power plant in Example 8.7<br />

to equal zero. Why can’t this occur? Answer: T condenser = 488 K = 215°C. This cannot occur because it would require the<br />

plant to be reversible throughout (i.e., it could have no internal friction, heat transfer, chemical reactions, or anything<br />

else that would naturally be irreversible).<br />

13. If the heat transfer rate into the boiler is doubled in Example 8.7 and all the other parameters remain constant,<br />

determine the new entropy production rate of the power plant. Is this possible? Answer: _S P = −33,900 kJ=h⋅K: This is<br />

not possible because it violates the second law of thermodynamics _S P must be > 0 .

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