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Modern Engineering Thermodynamics

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

EXAMPLE 8.2 (Continued )<br />

Therefore,<br />

Q _ <br />

T<br />

condenser = _Q river<br />

solar<br />

T collector<br />

and the ERB becomes<br />

<br />

_W electrical<br />

rev = _Q solar 1 − T river<br />

T collector<br />

= ð24,300 Btu/hÞ<br />

<br />

<br />

<br />

<br />

= ð100: × 10 3 40:0 + 459:67<br />

Btu/hÞ 1 −<br />

200: + 459:67<br />

1kW<br />

3412 Btu/h<br />

<br />

= 7:11 kW<br />

The positive sign indicates that the electrical power is out of the system.<br />

This example could also have been solved by using the Carnot heat engine efficiency (which is defined only for<br />

a reversible system) and the definition of the absolute temperature scale given in Eq. (7.15).<br />

EXAMPLE 8.3<br />

Determine an expression for the minimum isothermal system boundary temperature required by the second law of thermodynamics<br />

as an incompressible material is heated or cooled from a temperature T 1 to a temperature T 2 in a closed system<br />

with a constant heat flux.<br />

Solution<br />

First, draw a sketch of the system (Figure 8.3).<br />

Here, we are asked to derive a formula (the unknown) for the minimum<br />

value of an isothermal boundary temperature, (T b ) min =?Thesystemis<br />

(T b ) min = ?<br />

closed and made up exclusively of an incompressible material (solid or<br />

T 1 T 2<br />

liquid). The energy balance equation for this system is<br />

Q<br />

1Q 2 − 1 W 2 = mu ð 2 − u 1 Þ+ KE 2 − KE 1 + PE 2 − PE A = Constant<br />

1<br />

Incompressible<br />

State 1<br />

State 2<br />

0 ðassume the system is stationaryÞ<br />

material<br />

For an incompressible Z substance, V = constant, so dV = 0, and<br />

2<br />

FIGURE 8.3<br />

1W 2 = − pdV = 0: Since no other work modes are mentioned in Example 8.3.<br />

1<br />

the problem statement, we assume that there are none. The resulting<br />

energy balance is then<br />

1Q 2 = mu ð 2 − u 1 Þ<br />

The entropy balance equation for this system is<br />

Z Z <br />

_q<br />

ms ð 2 − s 1 Þ = dA dt + 1 ðS P Þ<br />

τ Σ T 2<br />

b<br />

which, for a constant heat flux ð _q Þ and isothermal boundaries, reduces to<br />

ms ð 2 − s 1 Þ = 1 Q 2<br />

+ 1 ðS P Þ<br />

T 2<br />

b<br />

Combining the energy balance and the entropy balance, we get<br />

mu ð 2 − u 1 Þ<br />

T b =<br />

ms ð 2 − s 1 Þ− 1 ðS P Þ 2<br />

Now, since 1 (S P ) 2 ≥ 0, clearly T b is at a minimum when 1 (S P ) 2 = 0 (a reversible process). Therefore,<br />

ðT b Þ min<br />

= u 2 − u 1<br />

s 2 − s 1

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