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Modern Engineering Thermodynamics

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228 CHAPTER 7: Second Law of <strong>Thermodynamics</strong> and Entropy Transport and Production Mechanisms<br />

then<br />

<br />

ðdS T Þ rev = d Q <br />

Q T<br />

rev<br />

(7.45)<br />

which, when integrated, produces Eq. (7.43) again.<br />

In an irreversible process, the total production of entropy is always positive, by virtue of the second law of thermodynamics.<br />

Therefore, Eq. (7.25) can be viewed as an entropy balance equation for a closed system undergoing<br />

irreversible heat and work transports of energy. Then,<br />

dS = dS T + dS P<br />

<br />

= dQ <br />

+ dW rev − dW act<br />

T<br />

act<br />

T<br />

where dS P > 0 by the second law of thermodynamics. To reconcile the difference between the actual work and the<br />

reversible work terms in this equation, we use the conceptofaworktransportenergyefficiency,η W ,whichwas<br />

introduced in Chapter 4. For a work-absorbing system such as a pump, we have<br />

Work-absorbing system<br />

and, for a work-producing system such as an engine, we have<br />

W act = W rev /η W (4.71)<br />

Work-producing system<br />

W act = η W W rev (4.72)<br />

Let us define an irreversible work component, W irr , which is always a positive number, as<br />

and<br />

W irr = ð1 − 1/η W ÞW rev , for a work-absorbing system<br />

W irr = ð1 − η W ÞW rev , for a work-producing system (7.46)<br />

Note that η W is a positive number between zero and unity (0 < η W < 1) and that W rev is negative for a workabsorbing<br />

system and positive for a work-producing system. Consequently, Eq. (7.46) produces positive values<br />

for W irr for both work-absorbing and work-producing systems. Then, we can write for either a work-absorbing or<br />

a work-producing system that<br />

and the entropy balance equation becomes 9<br />

dS = dS T + dS P =<br />

W rev − W act = W irr<br />

<br />

dQ T<br />

<br />

<br />

act<br />

+ dW T<br />

<br />

irr<br />

(7.47)<br />

We now wish to identify the individual heat and work components of the entropy transport and production<br />

terms. For a closed system, we may decompose the transport and production terms as follows:<br />

and<br />

so that<br />

dS = ðdS T<br />

dS T = ðdS T<br />

dS P = ðdS P<br />

Þ Q<br />

+ ðdS T<br />

Þ Q + ðdS T Þ W<br />

Þ Q + ðdS P Þ W<br />

Þ W<br />

+ ðdS P Þ Q<br />

+ ðdS P Þ W<br />

(7.48)<br />

Substituting Eq. (7.44) into (7.47) gives<br />

<br />

dS = d Q <br />

+ Q <br />

T<br />

act<br />

T 2 dT + dW<br />

act<br />

T<br />

<br />

irr<br />

(7.49)<br />

9 Note that W irr is always positive for both work-absorbing and work-producing systems, so its sign is correct here.

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