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Modern Engineering Thermodynamics

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352 CHAPTER 10: Availability Analysis<br />

Some of the more important equations introduced in this chapter are (recall that the thermodynamic properties<br />

of the local environment or ground state are written as T 0 , p 0 , V 0, v 0 , U 0 , u 0 , H 0 , h 0 , S 0 and s 0 ) follow.<br />

1. The maximum reversible work that a closed system can perform is given by Eq. (10.1) as<br />

ðWÞ maximum<br />

reversible<br />

= E − E 0 − T 0 ðS − S 0 Þ<br />

and the maximum reversible useful work that a closed system can perform is given by Eq. (10.2) as<br />

ðWÞmaximum<br />

reversible<br />

useful<br />

= ðWÞ maximum<br />

reversible<br />

− ðWÞreversible = E − E 0 + p 0 ðV − V 0Þ − T 0 ðS − S 0 Þ<br />

moving<br />

boundary<br />

2. The total availability A of a closed system is given by Eq. (10.3) as<br />

A = ðWÞmaximum<br />

= E − E<br />

reversible<br />

0 + p 0 ðV − V 0Þ − T 0 ðS − S 0 Þ<br />

useful<br />

<br />

<br />

= mu− u 0 + p 0 ðv − v 0 Þ − T 0 ðs − s 0 Þ + V 2 /2g c + gZ/g c<br />

and the specific availability, a, of a closed system is given by Eq. (10.4) as<br />

a = A/m = u − u 0 + p 0 ðv − v 0 Þ − T 0 ðs − s 0 Þ + V 2 /2g c + gZ/g c<br />

3. The change in total and specific availability of a closed system as it passes from state 1 to state 2 is given by<br />

Eqs. (10.5) and (10.6) as<br />

and<br />

A 2 − A 1 = E 2 − E 1 + p 0 ðV 2 − V 1Þ − T 0 ðS 2 − S 1 Þ<br />

= m½u 2 − u 1 + p 0 ðv 2 − v 1 Þ − T 0 ðs 2 − s 1 Þ + ðV 2 2 − V2 1 Þ/2g c + gðZ 2 − Z 1 Þ/g c Š<br />

a 2 − a 1 = u 2 − u 1 + p 0 ðv 2 − v 1 Þ − T 0 ðs 2 − s 1 Þ + ðV 2 2 − V 2 1 Þ/2g c + gðZ 2 − Z 1 Þ/g c<br />

4. The irreversibility I and the irreversibility rate _ I that occur inside a system are given by Eqs. (10.14) and<br />

(10.15) as<br />

and<br />

1I 2 = T 01 ðS P Þ 2<br />

≥ 0<br />

_I = T 0<br />

_S P ≥ 0<br />

5. The availability balance (AB) and availability rate balance (ARB) for a closed system with a single heat<br />

transfer mode occurring at a constant system boundary temperature T b is given by Eqs. (10.18) and<br />

(10.19) as<br />

<br />

1 − T <br />

0<br />

ð 1 Q 2 Þ − 1W 2 + p 0 ðV 2 − V 1Þ − 1 I 2 = ðA 2 − A 1 Þ<br />

T system = ½mða 2 − a 1 ÞŠ system<br />

bi<br />

and<br />

<br />

1 − T <br />

<br />

0<br />

dV<br />

_Q − _W + p 0<br />

T b<br />

dt − _I =<br />

dA <br />

dt<br />

system<br />

6. The specific flow availability of mass crossing a system boundary is defined by Eq. (10.20) as<br />

a f = h − h 0 − T 0 ðs − s 0 Þ + V2<br />

2g c<br />

+ gZ<br />

g c

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