Chapter 1:
1
Chapter 2:
2
3
4
5
Chapter 3:
6
Chapter 4:
For a closed system
For a constant pressure process
For an ideal gas
Specific heat ratio
For incompressible substances (liquids and solids)
The Δu and Δh of incompressible substances
7
Chapter 5
General Steady State Energy Equation:
Q cv Wcv
(V 2  V22 )

 (h1  h2 )  1
 g ( z1  z2 )
m
m
2
General Nozzle Eq: Wcv  m (h1  h2 )
0
 V12  V22 


)

=
(h
h
General Turbine Eq: Wout 1 2 
2


m

General Compressor and Pump Eq: Wcv  m (h1  h2 )
General Heat Exchanger Eq.:
0   m i hi   m e he
i
e
General Throttling and Valves Eq.: h1=h2
8
Chapter 6
9
Chapter 7
For an ideal gas
10
For an ideal gas assuming constant heat capacities
For an ideal gas with variable heat capacities
Isentropic process of ideal gases
Reversible steady flow work
11
Compressor work
Isentropic
Polytropic
Isothermal
Isentropic efficiency of turbines
Isentropic efficiency of compressors and pumps
Isentropic efficiency of nozzle
12
13
Chapter 9
Carnot cycle
14
Otto cycle
Assuming constant heat capacities
15
Diesel cycle
Assuming constant heat capacities
16
Stirling and Ericsson cycles
17
Brayton cycle
Assuming constant heat capacities
18
Brayton cycle with regeneration
Ideal jet-propulsion cycle
19
Chapter 10
Carnot vapor cycle
Rankine cycle
20
21
The ideal reheat Rankine cycle
The ideal regenerative Rankine cycle with an open feedwater heater
22
The ideal regenerative Rankine cycle with a closed feedwater heater
23
Cogeneration
Combined gas-vapor power cycle
24
Chapter 11
Reversed Carnot cycle
The ideal vapor-compression refrigeration cycle
25
Cascade refrigeration cycles
Gas refrigeration cycles
26
Absorption refrigeration cycles
27