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Modern Engineering Thermodynamics

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

7. The coefficient of performance (COP) of a Carnot engine operating in reverse as a heat pump, refrigerator,<br />

or air conditioner is<br />

and<br />

COP Carnot<br />

=<br />

heat pump<br />

COP Carnot<br />

=<br />

refrig: or<br />

air cond:<br />

T H<br />

T H − T L<br />

(7.18)<br />

T L<br />

T H − T L<br />

(7.20)<br />

8. The change in specific entropy of an incompressible material (solid or liquid) with constant specific heat c is<br />

and, for an ideal gas with constant specific heats c p and c v ,itis<br />

ðs 2 − s 1 Þ incompressible material = c lnðT 2 /T 1 Þ (7.33)<br />

with a constant c<br />

ðs 2 − s 1 Þ ideal gas<br />

= c v ln T 2<br />

+ R ln v 2<br />

(7.36)<br />

T 1 v 1<br />

constant<br />

c p and c v<br />

= c p ln T 2<br />

T 1<br />

− R ln p 2<br />

p 1<br />

(7.37)<br />

9. When an ideal gas is used in an isentropic process between states 1 and 2, the following is valid:<br />

<br />

T 2<br />

= v 1−k <br />

2<br />

= p ðk−1Þ/k<br />

2<br />

(7.38)<br />

T 1 v 1 p 1<br />

10. The heat transport of entropy (S T ) Q and the heat transport rate of entropy<br />

a constant temperature T b are<br />

_S T across a system boundary at<br />

Q<br />

<br />

ðS T Þ Q<br />

=<br />

_q <br />

ðτAÞ = 1 Q 2<br />

T b act<br />

T b act<br />

(7.60a)<br />

and<br />

<br />

_S T<br />

Q = Q _ <br />

T b act<br />

(7.61a)<br />

11. The work transport of entropy (S T ) W and the work transport rate of entropy _S T across a system boundary<br />

W<br />

are both zero:<br />

and<br />

ðS T Þ W = constant = 0 (7.62)<br />

_S T<br />

W = 0 (7.63)<br />

12. The entropy production (S P ) Q due to an actual heat transfer inside a system of volume V during the time<br />

interval 0 − τ is<br />

Z Z<br />

ðS P Þ Q<br />

= −<br />

V τ<br />

<br />

_q<br />

<br />

dT<br />

T 2 dx<br />

<br />

dt dV =<br />

act<br />

Z<br />

V<br />

Z<br />

τ<br />

σ Q dt dV (7.65)<br />

and the entropy production rate (_S P ) Q due to an actual heat transfer inside a system of volume V is<br />

Z <br />

<br />

<br />

Z<br />

_S P Q = −<br />

V<br />

_q<br />

T 2<br />

<br />

dT<br />

dx<br />

dV =<br />

act<br />

σ Q dV (7.66)<br />

V<br />

13. The equations for the entropy production (S P ) W due to the presence of work modes by a system depends on<br />

the type of work mode present. For example, if the system is isothermal throughout at temperature T and an

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