Fundamentals of Heat Engines. Jamil Ghojel
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The entropy change of a gas on molar basis is
The entropy change for process 1–2 is then
(1.94)
If the specific heat Cp is assumed constant, Eq. (1.94) becomes
(1.95)
More accurate results can be obtained if the variability of specific heat with temperature is accounted for. Taking the absolute zero as the reference temperature,
(1.96)
The values of
(1.97)
Substituting Eq. (1.97) in Eq. (1.94), we obtain
(1.98)
As Eq. (1.98) shows, entropy changes with both temperature and pressure. When using Eq. (1.98) in chemical reactions, the pressure ratio in the last term is replaced by the mole concentration of each substance.
The
(1.99)
The coefficients of correlation Eq. (1.99) for six gases are given in Table 1.3.
Table 1.3 Coefficients of Eq. (1.99) for the calculation of
of combustion products, pref = 0.1 MPa Tref = 0 K.
|
||||||
Coefficient | CO2 | CO | H2O | H2 | O2 | N2 |
a | 269.772 6 | 234.929 1 | 233.305 3 | 166.044 4 | 243.729 9 | 228.592 9 |
b | 53.720 45 | 33.106 85 | 42.087 92 | 30.813 48 | 34.405 98 | 32.655 06 |
c | 4.955 586 | 1.661 032 | 4.707 912 | 2.022 13 | 2.175 759 | 1.661 282 |
d | −0.617 24 | 9.19E‐02 | 0.667 926 | 0.447 018 | 0.197 82 | 0.150 999 |
As for air, the following modified function (Rivkin 1987) can be used for the temperature range −50 to 1500 °C with the constant coefficients shown in Table 1.4:
(1.100)
Table 1.4 Coefficients of Eq. (1.100) for the calculation of
of air.B n | ||||||||
A | B 1 | B 2 | B 3 | B 4 | B 5 | B 6 | B 7 | B 8 |
29.44 | 230.18 | −1.61 | −5.99 | 22.94 | −24.56 | 12.98 | −3.48 |
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