Microsoft Word - Cengel and Boles TOC _2-03-05_.doc

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Both the Stirling and Ericsson cycles are totally reversible, as is the Carnot
cycle, and thus according to the Carnot principle, all three cycles must have
the same thermal efficiency when operating between the same temperature
limits:

(9–14)

This is proved for the Carnot cycle in Example 9–1 and can be proved in a
similar manner for both the Stirling and Ericsson cycles.

hth,Stirlinghth,Ericssonhth,Carnot 1 

TL
TH

506 | Thermodynamics


EXAMPLE 9–4 Thermal Efficiency of the Ericsson Cycle

Using an ideal gas as the working fluid, show that the thermal efficiency of
an Ericsson cycle is identical to the efficiency of a Carnot cycle operating
between the same temperature limits.

Solution It is to be shown that the thermal efficiencies of Carnot and
Ericsson cycles are identical.
Analysis Heat is transferred to the working fluid isothermally from an external
source at temperature THduring process 1-2, and it is rejected again isother-
mally to an external sink at temperature TL during process 3-4. For a
reversible isothermal process, heat transfer is related to the entropy change by

The entropy change of an ideal gas during an isothermal process is

The heat input and heat output can be expressed as

and

Then the thermal efficiency of the Ericsson cycle becomes

since P 1 P 4 and P 3  P 2. Notice that this result is independent of
whether the cycle is executed in a closed or steady-flow system.

hth,Ericsson 1 

qout
qin

 1 

RTL ln 1 P 4 >P 32
RTH ln 1 P 1 >P 22

 1 

TL
TH

qoutTL 1 s 4 s 32 TLaR ln

P 4
P 3

bRTL ln

P 4
P 3

qinTH 1 s 2 s 12 THaR ln

P 2
P 1

bRTH ln

P 1
P 2

¢scp ln

Te
Ti

R ln

Pe
Pi

R ln

Pe
Pi

qT ¢s

Stirling and Ericsson cycles are difficult to achieve in practice because
they involve heat transfer through a differential temperature difference in all
components including the regenerator. This would require providing infi-
nitely large surface areas for heat transfer or allowing an infinitely long time
for the process. Neither is practical. In reality, all heat transfer processes take
place through a finite temperature difference, the regenerator does not have
an efficiency of 100 percent, and the pressure losses in the regenerator are
considerable. Because of these limitations, both Stirling and Ericsson cycles

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