Air Standard Cycle
Air Standard Cycle
Air Standard Cycle
MEC 451
5 Thermodynamics
Lecture Notes:
MOHD HAFIZ MOHD NOH
HAZRAN HUSAIN & MOHD
SUHAIRIL
Faculty of Mechanical Engineering
Universiti Teknologi MARA, 40450
Air Standard
Shah Alam, Selangor Cycle
TL
η th , Carnot = 1−
TH
Wnet
η th =
Qin
2
Review – Ideal Gas Law
Pv = RT or PV = mRT
3 3
The Δu and Δh of ideal gases can be expressed as
∆u = u 2 − u1 = C v (T2 − T1 )
∆h = h2 − h1 = C P (T2 − T1 )
4
Review – Thermodynamics Processes
P1 P2
isochoric constant volume (V1 = V2) =
T1 T2
constant pressure (P1 = V1 V2
isobaric
P 2)
=
T1 T2
constant temperature
isothermal
(T1 = T2) P1V1 = P2V2
n
polytropic -none- n
P1 V2 T1 n −1
= =
isentropic constant entropy (S1 = S2) P2 V1 T2
5
Review – Properties of Air
R = 0.2871 kJ/kg.K
Cp = 1.005 kJ/kg.K
Cv = 0.718 kJ/kg.K
k = 1.4
7
Air-Standard Assumptions
8
Air-Standard Assumptions
9
Terminology for Reciprocating Devices
10
The compression ratio r of an
engine is defined as
V max VBDC
r= =
V min VTDC
12
The processes in the Otto cycle are as per following:
Process Description
1-2 Isentropic compression
2-3 Constant volume heat addition
3-4 Isentropic expansion
4-1 Constant volume heat rejection
13
Related formula based on basic thermodynamics:
n
n
P1 V2 T n −1
= = 1
P2 V1 T2
Qin = mCv ( T3 − T2 )
n
n
P1 V2 T1 n −1
= =
P2 V1 T2
Qout = mCv ( T4 − T1 )
14
Thermal efficiency of the Otto cycle:
Qnet , 23 = ∆U 23
Qnet , 23 = Qin = mCv (T3 − T2 )
15
Apply first law closed system to process 4-1, V = constant.
Qnet ,41 − Wnet ,41 = ∆U 41
1
Wnet ,41 = Wother ,41 + Wb ,41 = 0 + ∫ PdV = 0
4
Thus, for constant specific heats,
Qnet , 41 = ∆U 41
Qnet , 41 = −Qout = mCv (T1 − T4 )
Qout = −mCv (T1 − T4 ) = mCv (T4 − T1 )
T2 T3 T4 T3
= or =
T1 T4 T1 T2
17
The Otto cycle efficiency becomes
T1
η th , Otto = 1 −
T2
1
η th , Otto = 1 −
r k −1 18
Example 5.1
Q23 = mCv ( T3 − T2 )
0.2871( 290 )
1 1 = RT1 ⇒ v1 = = 0.875 mkg
3
IGL : Pv
95
Q23 v1
q23 = = Q23 = 1727 kJ
kg
m V1 20
Example 5.1
P3 V4
21
Example 5.1
Then:
Wnet = qin − qout
= q23 − q41
= 1009.6 kJ
kg
Wnet
ηth,Otto = = 0.585 ( 58.5% )
qin
22
Example 5.1
What else?
Wnet wnet
MEP = =
Vmax − Vmin vmax − vmin
wnet wnet
= =
v1 − v2 v1 ( 1 − v2 / v1 )
wnet 1009.6
= = = 1298 kPa
v1 ( 1 − r ) 0.875 ( 1 − 1/ 9 )
1
wcompr ∆u12 Cv ( T2 − T1 )
rbw = = =
wexp ans −∆u34 Cv ( T3 − T4 )
= 0.225 ( 22.5% )
23
Supplementary Problems 5.1
24
Diesel Cycle
25
Diesel Cycle
v1 v3
= Compression ratio, rv and = Cut − off ratio, rc
v2 v2
26
Related formula based on basic thermodynamics:
n
n
P1 V2 T n −1
= = 1
P2 V1 T2
Qin = mCP ( T3 − T2 )
n
n
P1 V2 T n −1
= = 1
P2 V1 T2
Qout = mCv ( T4 − T1 )
27
Thermal efficiency of the Diesel cycle
Wnet Q
η th , Diesel = = 1 − out
Qin Qin
Apply the first law closed system to process 2-3, P = constant.
Qnet ,23 − Wnet ,23 = ∆U 23
3
Wnet ,23 = Wother ,23 + Wb ,23 = 0 + ∫ PdV = 0
2
= P2 ( V3 − V2 )
Thus, for constant specific heats
Qnet , 23 = ∆U 23 + P2 (V3 − V2 )
Qnet , 23 = Qin = mCv (T3 − T2 ) + mR (T3 − T2 )
Qin = mC p (T3 − T2 )
28
Apply the first law closed system to process 4-1, V = constant
Qnet ,41 − Wnet ,41 = ∆U 41
1
Wnet ,41 = Wother ,41 + Wb ,41 = 0 + ∫ PdV = 0
4
1 1 = PV 4 4 = PV
k k k k
PV 2 2 and PV 3 3
Solution:
Data given:
V1
= 18
V2
V3
= 2.5
V2
31
Example 5.2
V2 V3 V3
P2 = P3 ⇒ = ⇒ T3 = T2 ÷ = 2383.3 K
T2 T3 V2
Pr ocess 3 − 4 ( isentropic exp ansion )
V4 V1 V2
= . = 18 ( 1/ 2.5 ) = 7.2
V3 V2 V3
k −1
T4 V3
⇒ T4 = 2383.3 ( 1/ 7.2 )
0.4
= ÷ = 1082 K
T3 V4
32
Example 5.2
What we need?
wnet
( i ) ηth,diesel = = 0.6093 ( 60.93% )
qin
( ii ) Pmax = P2 = P3
k −1
P2 T2 k
÷ = ÷ ⇒ P2 = 5148 kPa ( Pmax )
P1 T1
wnet 875.67
( iii ) MEP = = = 969.1 kPa
V1 ( 1 − 1/ r ) 0.9566 ( 1 − 1/ 18 )
33
Supplementary Problems 5.2
34
Dual Cycle
rp rck − 1
η th = 1 −
[( r p ]
− 1) + k c p ( rc − 1) rvk −1
36
Example 5.3
V1 P1
= 18 = 1.5
V2 P2
V4
T1 = 300 K = 1.2
V3
P1 = 1bar
37
Pr ocess 1 − 2 ( isentropic compression )
k −1
T2 V1
⇒ T2 = 300 ( 18 )
0.4
= ÷ = 953.3K
T1 V2
Pr ocess 2 − 3 ( Const. pressure heat addition )
V2 V3 V3
P2 = P3 ⇒ = ⇒ T3 = T2 ÷ = 2383.3 K
T2 T3 V2
Pr ocess 3 − 4 ( isentropic exp ansion )
V4 V1 V2
= . = 18 ( 1/ 2.5 ) = 7.2
V3 V2 V3
k −1
T4 V3
⇒ T4 = 2383.3 ( 1/ 7.2 )
0.4
= ÷ = 1082 K
T3 V4
38
Pr ocess 4 − 5 ( isentropic exp ansion )
k −1 k −1 k −1
T5 V4 V4 V4 V3
= ÷ ⇒ T5 = T4 ÷ = T4 ÷ ÷
T4 V5 V5 V3 V5
= 1715.94 ( 1.2 ) ( )
0.4
1
18
= 584.85 K
Information needed?
39
Answer the questions ?
40
Criteria of Performance
41
Indicated Power
Defined as the rate of work done by the gas on the
piston as evaluated from an indicator diagram obtained
from the engine using the electronic engine indicator.
pi LANn
IP =
2
And for two-stroke engine, n is the number of cylinders.
IP = pi LANn
42
Indicated Power
τ = Wr
44
Therefore
bp = 2πNτ
Brake power is also can be expressed as
η m pi LANn Pb LANn
bp = η m IP = =
2 2
Then the brake mean effective pressure (Pb) is
Pb = η m Pi
45
Friction Power
brake power
η mech =
indicated power
47
ηm
Brake Mean Effective Pressure
48
ηm
Brake Thermal Efficiency
The power output of the engine is obtained from the chemical energy of
the fuel supplied. The overall engine efficiency is given by the brake
thermal efficiency,
brake power brake power bp bp
ηbp = = = =
power given fuel equivalent power Pfe m f Qnet ,v
49
Specific Fuel Consumption
sfc is the mass flow rate of fuel consumed per unit power
output and is a criterion of economical power production.
m f
sfc =
bp
50
Volumetric Efficiency
V
ηV =
Vs
51
Example 5.4
Solution:
52
Example 5.4
53
Real Case
pi LANn
IP =
2
bp = 2πNτ
54