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Modern Engineering Thermodynamics

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13.14 Ericsson Cycle 491<br />

Q H<br />

4<br />

1<br />

3<br />

4<br />

T<br />

T H<br />

p H = c p L = c<br />

p<br />

p H<br />

T L = c T H = c<br />

T L<br />

3<br />

Q<br />

2<br />

L<br />

p L<br />

2<br />

1<br />

s<br />

(a) T–s diagram<br />

V<br />

(b) p–V diagram<br />

Q regen<br />

Isobaric regenerator<br />

Isobaric regenerator<br />

2 Q regen<br />

1<br />

3 2<br />

4 1<br />

3<br />

4<br />

Q L<br />

Q H Q L Q H<br />

W comp.<br />

W out<br />

W comp.<br />

W out<br />

Isothermal<br />

compressor (T L )<br />

(c) Closed loop Ericson cycle<br />

reciprocating equipment<br />

Isothermal power<br />

piston (T L )<br />

Isothermal<br />

compressor (T L )<br />

Isothermal<br />

turbine (T L )<br />

(d) Closed loop Ericson cycle<br />

turbomachinery equipment<br />

FIGURE 13.40<br />

The Ericsson cycle.<br />

To atmosphere<br />

From atmosphere<br />

Isobaric regenerator<br />

Q regen<br />

Q H<br />

W out<br />

p L = constant<br />

T H<br />

T L<br />

T<br />

p H = constant<br />

s<br />

Q L<br />

Compressor stage<br />

intercoolers<br />

Turbine stage<br />

reheaters<br />

FIGURE 13.41<br />

An open loop gas turbine power plant as an approximation to the Ericsson cycle.<br />

and<br />

j _Q L j = _mT L ðs 2 − s 3 Þ<br />

Equation (7.37) of Chapter 7 gives these entropy changes for the cold ASC as<br />

and<br />

s 1 − s 4 = c p ln ðT 1 /T 4 Þ+ R ln ðp 1 /p 4 Þ = R ln ðp 1 /p 4 Þ<br />

s 2 − s 3 = c p ln ðT 2 /T 3 Þ+ R ln ðp 2 /p 3 Þ = R ln ðp 2 /p 3 Þ

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