Consider a heat engine operating between a high temperature of 127◦C and a low temperature of 27◦C. 1a. What is the maximum thermal efficiency (ηmax) that could theoretically be achieved with this engine?  1b. What is the actual thermal efficiency η of this engine if it produces 500 J of work for every 4000 J of heat supplied from the hot side?  1c. Wha

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Consider a heat engine operating between a high temperature of 127◦C and a low temperature of 27◦C.

1a. What is the maximum thermal efficiency (ηmax) that could theoretically be achieved with this engine? 

1b. What is the actual thermal efficiency η of this engine if it produces 500 J of work for every 4000 J of heat supplied from the hot side? 

1c. What is the entropy change of the hot side, the cold side, and the total entropy change in part b? 

Useful info
NA = 6.022x103 mol
g =9.807 m/s?
P[H>O] =1.00 g/mL
1 bar = 10° Pa
1 atm =1.013bar
R = 8.314 J/K-mol
= 8.206x10? L-atm/K-mol
= 8.206x10° m-atm/K-mol
= 62.36 L-Tor/K-mol
1J = 10 L-bar = 9.870×10³ L-atm= 0.2390 cal
1m = 10° cm = 10° mm = 10° um = 10° nm = 101º A
= 760 Torr
1 mbar = 10 bar
RT = 2.478 kJ/mol for T = 298 K. (= 24.46 L-atm/mol)
1 L-atm = 101.3J
1 m = 10° L = 10° cm
1 kg = 1000 g
1 Watt (W) = 1 J/s
Physical Properties of Selected Substances
Cp.m
J/(mol-K) J/(mol-K) kJ/mol
24.3
AH melting temp AHap boiling temp
kJ/mol
mol. wt.
fas
g/mol
kJ/mol
K
K
Al(s)
CH,OH(I)
CH;OH(g)
H,(g)
H;O(1)
H,O(g)
H,O(s)
1,(s)
L(g)
I(g)
N2(g)
Na(s)
NaN,(s)
0:(g)
Properties of pure phases are for standard conditions of 298 K and 1 atm.
Phase transition enthalpies are valid at the indicated phase transition temperature, at 1 atm.
27.0
28.3
32.04
-238.66
81.6
3.16
175.2
35.29
337.2
32.04
-200.66
43.9
2.0
131.7
28.8
18.0
-285.8
69.9
75.3
6.0
273
40.6
373
18.0
-241.8
188.8
33.6
18.0
38.0
37.0
253.8
116.14
54.44
15.5
386.8
41.8
458.4
253.8
+62.44
260.69
36.90
126.9
+106.84
180.79
20.79
28.0
191.61
29.1
23.0
51.2
28.2
2.6
371
97.4
1156
65.0
+21.76
70.5
76.6
32.0
205.1
29.4
Integrals
Maxwell relations
n# -1
n+1
av
as
In z
as
P
rp-
1
- In(az – b)
as
av
T
T
Properties of Some Materials
Density (293 K)
g/cm
KT
10-4 K-1
10-" bar
C, graphite
C, diamond
Cu, solid
Water, liquid
2.26
3
Euler chain rule
3.5
0.030
0.187
az
8.9
0.501
0.735
= -1
az
0.997
2.1
49.6
Transcribed Image Text:Useful info NA = 6.022x103 mol g =9.807 m/s? P[H>O] =1.00 g/mL 1 bar = 10° Pa 1 atm =1.013bar R = 8.314 J/K-mol = 8.206x10? L-atm/K-mol = 8.206x10° m-atm/K-mol = 62.36 L-Tor/K-mol 1J = 10 L-bar = 9.870×10³ L-atm= 0.2390 cal 1m = 10° cm = 10° mm = 10° um = 10° nm = 101º A = 760 Torr 1 mbar = 10 bar RT = 2.478 kJ/mol for T = 298 K. (= 24.46 L-atm/mol) 1 L-atm = 101.3J 1 m = 10° L = 10° cm 1 kg = 1000 g 1 Watt (W) = 1 J/s Physical Properties of Selected Substances Cp.m J/(mol-K) J/(mol-K) kJ/mol 24.3 AH melting temp AHap boiling temp kJ/mol mol. wt. fas g/mol kJ/mol K K Al(s) CH,OH(I) CH;OH(g) H,(g) H;O(1) H,O(g) H,O(s) 1,(s) L(g) I(g) N2(g) Na(s) NaN,(s) 0:(g) Properties of pure phases are for standard conditions of 298 K and 1 atm. Phase transition enthalpies are valid at the indicated phase transition temperature, at 1 atm. 27.0 28.3 32.04 -238.66 81.6 3.16 175.2 35.29 337.2 32.04 -200.66 43.9 2.0 131.7 28.8 18.0 -285.8 69.9 75.3 6.0 273 40.6 373 18.0 -241.8 188.8 33.6 18.0 38.0 37.0 253.8 116.14 54.44 15.5 386.8 41.8 458.4 253.8 +62.44 260.69 36.90 126.9 +106.84 180.79 20.79 28.0 191.61 29.1 23.0 51.2 28.2 2.6 371 97.4 1156 65.0 +21.76 70.5 76.6 32.0 205.1 29.4 Integrals Maxwell relations n# -1 n+1 av as In z as P rp- 1 - In(az – b) as av T T Properties of Some Materials Density (293 K) g/cm KT 10-4 K-1 10-" bar C, graphite C, diamond Cu, solid Water, liquid 2.26 3 Euler chain rule 3.5 0.030 0.187 az 8.9 0.501 0.735 = -1 az 0.997 2.1 49.6
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