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Modern Engineering Thermodynamics

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492 CHAPTER 13: Vapor and Gas Power Cycles<br />

Figure 13.40b shows that T 2 = T 3 = T L , T 1 = T 4 = T H ,andp 1 /p 4 = p 2 /p 3 , so that the previous equations yields<br />

s 1 – s 4 = s 2 – s 3 and the thermal efficiency becomes<br />

ðη T Þ Ericsson<br />

= 1 − T L /T H = 1 − T 2 /T 1 = 1 − T 3 /T 4 (13.20)<br />

cold ASC<br />

Thus, like the Stirling cold ASC, the Ericsson cold ASC has the same thermal efficiency as the Carnot cold ASC<br />

operating between the same two temperature limits. The Stirling and Ericsson cycle engines of the 19th century<br />

were large and costly, and their actual operating thermal efficiencies were quite poor. They were ultimately<br />

replaced by a newer, more efficient engine technology introduced in the second half of the 19th century, the<br />

internal combustion Otto and Diesel cycles, discussed later in this chapter. However, the high thermal efficiency<br />

potential of the Stirling and Ericsson cycles produces periodically renewed interest in utilizing these cycles within<br />

the framework of modern technology.<br />

EXAMPLE 13.10<br />

A new Ericsson cycle engine is being designed with a pressure ratio of PR = p 4 /p 1 = 2.85, a power piston outlet pressure of<br />

p 1 = 0.500 MPa, a maximum volume of V 1 = 0.0110 m 3 , and a minimum volume of V 3 = 3.00 × 10 –3 m 3 . The engine will<br />

contain 0.0500 kg of air. Use the Ericsson cold ASC analysis shown in Figure 13.40 to complete this design, determining<br />

a. The compressor inlet pressure and volume (p 2 and V 2 ).<br />

b. The power piston outlet pressure and inlet volume (p 4 and V 4 ).<br />

c. The compressor outlet pressure (p 3 ).<br />

d. The temperatures at the inlet and outlet of the power and displacer pistons (T 1 , T 2 , T 3 , and T 4 ).<br />

e. The Ericsson cold ASC thermal efficiency of this engine.<br />

Solution<br />

Using the Ericsson cycle diagram shown in Figure 13.40 we can carry out the following analysis.<br />

a. For this cycle, the compressor inlet pressure is the same as the power piston outlet pressure (see Figure 13.40), or<br />

p 2 = p 1 = 0.500 MPa. The compressor inlet volume is V 2 = V 3 × (CR), where the isentropic compression ratio<br />

CR = V 1 /V 4 and V 4 = mRT 4 /p 4 . Now, from Figure 13.40,<br />

T 4 = T 1 = p 1V 1<br />

mR<br />

= ð0:500 MPaÞð1000 kPa/MPaÞð0:0110 m3 Þ<br />

ð0:0500 kgÞð0:286 kJ/kg . KÞ<br />

= 385 K<br />

and<br />

p 4 = p 3 = p 2 ðPRÞ = p 1 ðPRÞ = ð0:500 MPaÞð2:85Þ = 1:43 MPa<br />

so<br />

V 4 = mRT 4<br />

p 4<br />

= ð0:0500 kgÞð0:286 kJ/kg . KÞð385 KÞ<br />

ð1:43 MPaÞð1000 kPa/MPaÞ<br />

= 0:00385 m 3<br />

and the isentropic compression ratio is<br />

CR = V 1 0:0110 m3<br />

=<br />

V 4 0:00385 m = 2:86<br />

3<br />

Then, the compressor inlet volume is V 2 = V 3 × (CR) = (3.00 × 10 –3 )(2.86) = 0.00858 m 3 .<br />

b. For this cycle, the power piston outlet pressure is the same as the compressor inlet pressure (see Figure 13.40):<br />

p 4 = p 3 = 1.43 MPa, and from part a, V 4 = 0.00385 m 3 .<br />

c. Since p 4 /p 1 = p 3 /p 2 = PR, the compressor outlet pressure is p 3 = p 2 (PR), where the isentropic pressure ratio is given as<br />

PR = 2.86. Then, p 3 = 0.500(2.86) = 1.43 MPa.<br />

d. Using the ideal gas equation of state, we have<br />

T 3 = T 2 = p 2V 2<br />

mR<br />

= ð0:500 MPaÞð1000 kPa/MPaÞð0:00858 m3 Þ<br />

ð0:0500 kgÞð0:286 kJ/kg . KÞ<br />

e. The Ericsson cold ASC thermal efficiency for this engine is given by Eq. (13.20) as<br />

= 300: K<br />

ðη T Þ Ericsson<br />

= 1 − T L<br />

= 1 − T 2<br />

= 1 − 300: K = 0:221 = 22:1%<br />

T H T 1 385 K<br />

cold ASC

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