Exercise
4 :
a)
W =
-nRTln(Vf/Vi) = -16.9 kJ
b)
ΔS = Q/T = (ΔEint-W)/T = -W/T = -16.9 kJ / 410 K = 41.2 J/K
c)
ΔS
= 0 for any reversible process
Exercise 6:
ΔS = Q/T =
mL/T = -0.001kg*333kJ*kg-1/268K = -1.24 J/K
Exercise
22 :
a)
Wcycle
= Wbc-Wda = -p1(V1-V0) +
p0(V0-V1) = -2.28 kJ
b)
Qab
= ΔEintab = 3/2 n R (Tb-Ta) =
3/2 n R [(p1V0-p0V0)*n-1*R-1]
= 3/2 (p1V0-p0V0) = 3/2 p0V0
Qbc = ΔEintbc
– Wbc = 3/2 n R (Tc-Tb) + p1(V1-V0)
= 3/2 p1V0 + p1(V1-V0) =
11.4 kJ
Qabc = Qab
+ Qbc = 14.8 kJ
c)
e =
|Wcycle|/|Qabc| = 2.28 kJ / 14.8 kJ = 0.15
d) e
= 1 – TL/TH = 1 – Ta/Tc
= 1 – p0 * V0 * p1-1 * V1-1
= 0.75
Exercise 29:
a) e = 1 – TL/TH
= 1 - |QL|/|QH| è |QL| = |QH|*TL/TH
W = |QH|
- |QL| = |QH| (1 - |QL|/|QH|) = |QH|
(1 – TL/TH) = 568 J (1 – 258K/322K) = 113 J
b) W = |QL|
(TH-TL)/TL = 1230 J (322K-258K)/258K = 305 J
Problem 8:
Va=Vb=1.22
m3; Vc=9.13 m3
pb=10.4
atm = 10.4*1.01*105 Pa=1.05*106 Pa
Calculate pc=pa=(Vb/Vc)γ pb = 3.64*104 Pa with γ = 1.67
Then calculate T from the equation of state of an ideal gas
T = (pV)/(nR):
Ta=2670K, Tb=77100K, Tc=20000K
Calculate changes in internal energy for each segment:
ΔEintab = n cv ΔTab = 2 mol * 3/2 * 8.31 J*K-1*mol-1 * (77100-2670)K = 1.86*106 J
ΔEintbc = n cv ΔTbc = 2 mol * 3/2 * 8.31 J*K-1*mol-1 * (20000-77100)K = -1.42*106 J
ΔEintca = - ΔEintab - ΔEintbc = -1.86*106 J +1.42*106 J = -4.40*105 J, since ΔEintcycle = 0
a) ΔEintab = Qab + Wab = Qab = 1.86*106 J, which is the heat added to the gas
b) ΔEintca = Qca + Wac è Qca = ΔEintca – Wca = ΔEintca – pa(Va-Vc) = -7.28*105 J, which is the heat leaving the gas
c) Wcycle = Wab + Wbc + Wca = Wbc + Wca = ΔEintbc + pa(Va-Vc) = -1.13*106 J
d) e
= |Wcycle|/|Qab| = 1.13*106J
/ 1.86*106J = 0.61