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Modern Engineering Thermodynamics

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8.2 Systems Undergoing Reversible Processes 255<br />

For an incompressible material, u 2 – u 1 = c(T 2 – T 1 ) and s 2 – s 1 = c ln(T 2 /T 1 ). Then,<br />

This is the required final formula.<br />

ðT b Þ min = T 2 − T 1<br />

ln ðT 2 /T 1 Þ<br />

If you look closely at the last equation in Example 8.3, you see that (T b ) min always falls between T 1 and T 2 . This<br />

means that, to change the temperature of an incompressible substance by a heat transfer process from an external<br />

source without producing entropy (i.e., reversibly), the system must be constructed with a well-defined<br />

boundary that is somehow maintained isothermal at the temperature given by this equation. This causes all the<br />

entropy generated by the heat transfer process to be produced outside the system.<br />

EXAMPLE 8.4<br />

Show that a reversible and adiabatic process carried out in a closed system results in the system having a constant entropy;<br />

that is, that a closed system reversible adiabatic process is also isentropic.<br />

Solution<br />

First, draw a sketch of the system (Figure 8.4).<br />

Here, we are to show that a reversible and adiabatic process carried out in a closed<br />

system results in the system having a constant entropy. We begin with just the<br />

entropy balance equation and note that<br />

Z Z <br />

ms ð 2 − s 1 Þ =<br />

τ Σ<br />

<br />

_q<br />

dA dt<br />

T b<br />

0 ðadiabaticÞ<br />

+ 1 ðS P Þ 2<br />

= 0<br />

0 ðreversibileÞ<br />

and therefore s 2 = s 1 and we have a constant entropy or isentropic process. Similarly, the entropy rate balance equation<br />

gives<br />

Z <br />

_q<br />

_S = dA + _S P = 0<br />

and therefore S (and, of course, s) is again constant.<br />

Σ<br />

T b<br />

0 ðadiabaticÞ<br />

0 ðreversibileÞ<br />

Exercises<br />

4. If the size of the solar collectors in Example 8.2 is doubled and the collectors capture 200. × 10 3 Btu/h of solar energy,<br />

determine the new maximum steady state electrical power output of the power plant. Answer: _W electrical<br />

rev = 14:2kW:<br />

5. Using the result of Example 8.3, determine the minimum isothermal boundary temperature as liquid water is heated<br />

from 50.0°F to 70.0°F at atmospheric pressure. Answer: (T b ) min = 520°F.<br />

6. Example 8.4 shows that a reversible and adiabatic process carried out in a closed system is also an isentropic process.<br />

Use a similar argument to show that an isentropic Z process in a closed system is not necessarily reversible and adiabatic.<br />

Answer: s 2 – s 1 = 0 simply implies that _S P = − ð _q /T b ÞdA, not that _S P = 0 and _q = 0:<br />

Σ<br />

S 1<br />

1 Q 2 = 0<br />

S 2 = ?<br />

1 (S P ) 2 = 0<br />

State 1<br />

Reversible and<br />

adiabatic process<br />

State 2<br />

FIGURE 8.4<br />

Example 8.4.<br />

Isentropic processes are an important new category that we add to our list of constant property processes<br />

(isothermal, isobaric, isochoric, and isenthalpic).<br />

ARE ALL ISENTROPIC PROCESSES REVERSIBLE AND ADIABATIC?<br />

Example 8.4 shows that all reversible and adiabatic processes are isentropic but not all isentropic processes are necessarily<br />

reversible and adiabatic. It does not automatically go both ways. For example, heat loss from a system results in an entropy<br />

loss for that system; and if this entropy loss exactly balances the entropy production for the process the system is<br />

undergoing, then the process also is isentropic without being either reversible or adiabatic.

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