problems on gas cycles in thermo
TRANSCRIPT
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Problems on Gas Cycles:
1. An automobile engine consumes fuel at a rate of 28 L/h and delivers 60kW of po er to the heels. !f the fuel has a heating value of ""#000 k$/kgand a densit% of 0.8 g/cm determine the efficienc% of this engine.
Solution:
2. 'onsider an ideal (ricsson c%cle ith air as the orking fluid e)ecuted in
kg22."L/h*kg/L*+28+0.8*,+m fuelfuel === 2-&.-8k$/h8 #600k$/kg*00kg/h*+""#0+22."um coalcoalA ====
A
net
QW
e = 21.or0.21
2-&.-8kW
60kW ==
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a stead% flo s%stem.Air is at 2-3' and 120
k4a at the beginning of the isothermal compression process# during hich1 0 k$/kg of heat is re5ected. eat transfer to air occurs at 1200 7.
etermine + a* the ma)imum pressure in the c%cle# + b* the net ork output per unit mass of air# and + c* the thermal efficienc% of the c%cle.
9olution:
a*
;hus#
kPa
kP P
K kg kJ K kg kJ
T
T
RT
T
c s
Kkg kJ K
kg kJ T
q s
p
2.68
120ln*/28-.0+/.0
lnln
/.0&00
/1 0
"
"
&
"
&
"
&"
1
"&&"
=
==
=== kJ kg kJ K K
QT T
QT T
QQ
R A A
R /600*/1 0+&00
1200*
&
1
1
& ====
kkJ QQw R Anet /" 01 0600 ===
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&.
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V pp
V pV p
Then
mRT V p
mRT V pT T
V mRT W
vv
mRdV V
mRT pdV W
QW
kJ Q
h
h
11.-2&60
@ *&.0*+6.+
#
A
.02&81.0n
"0
1
221
2211
22
1121
121
1
2
2
1
2
121
2121
21
====
===
====
===
==
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'.* =or process 2 &
=or process & "
=or process " 1
0&2 =
Q
*+ &2&2 uumW =
kkg W -.2 6*0.16--."2&+1&2 ==
"&"& = QW
W kkJ QkJ kJ QT
QT
Q
hc
1#1616*"0+".0BBBBB
"&"&"&21"& ======
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b.*
. 'onsidera simple ideal ?ra%ton c%cle ith air as the orking fluid. ;he pressure ratioof the c%cle is 6# and the minimum and ma)imum temperatures are &00 and
1&00 7# respectivel%. Do the pressure ratio is doubled ithout changingthe minimum and ma)imum temperatures in the c%cle. etermine thechange in + a* the net ork output per unit mass and + b* the thermalefficienc% of the c%cle as a result of this modification. Assume variablespecific heats for air.
9olution:
=or > 6
kg kJ kg kJ K K
qT T
eqw A Anet /-2*/00+1800& 0
111
& =
===
kkJ h K T /1.&00&00 11 ==
&86.11 =r P kkJ h K T /-.1&1&00 && ==
.&&0& =r P pr
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=or > 12
;hus#
6. An oldgas turbinehas anefficienc% of21 percentanddevelops a
po eroutput of6000 kW.eterminethe fuel
.&--.8 ""6.&&
/"6.&&11.-.8 "
/11.1.&00&.8
/-.8 ""0.01-.1&
/&.81.*.&&0+
6
1
/"0.01&16.8*&86.1*+6+
1"
2&
"
&
"
21
22
&"
1
===
======
===
==
==
====
A
net
R Anet
R
A
r r
r r
Qw
kg kJ qq
kg kJ hh
kg kJ hh
kJ h P
P
P
kJ h P P P
pr ."8
/&-.-8/6.&80
/6.&80"1."0"&-.-8
/"1."0"1.&006.-0"
/&-.-860.610-.1&
/6.-0"8.2-*.&&0+
12
1
/6.6106&.16*&86.1*+12+
1"
2&
"
&
"
21
22
&"
1
===
======
===
====
====
kg kJ kg kJ
qw
kg kJ qqw
kg kJ hh
kg kJ hh
kkJ h P
P
P
kJ h P P P
A
net
R Anet
R
A
r r
r r
*+6.10.&-."8
+/."1"6.&&6.&80
increasee
increasekg kJ wnet ==
==
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consumption rate of this gas turbine# in L/min# if the fuel has a heating valueof "2#000 k$/kg and a densit% of 0.8 g/cm&.
9olution:
-. 'onsider t o 'arnot heat engines operating in series. ;he first engine
receives heat from the reservoir at 1800 7 and re5ects the aste heat toanother reservoir at temperature T . ;he second engine receives this energ%re5ected b% the first one# converts some of it to ork# and re5ects the rest to areservoir at &00 7. !f the thermal efficiencies of both engines are the same#determine the temperature T .
9olution:
s L Lkg
skg mV
skg kg kJ skJ m
kJ skJ
eW
Q net A
/8 0.0/8.0
/680&.0
/680&.0/000#"2/-0#28
/-0#2821.0
/6000
===
==
===
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T T T
ThT T T
T
Th
T T
T e
Th
T e
h
*&00*+1800+
11
1
1
2
2
1
==
=
=
=
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E
8. Air is used as the orking fluid in a simple ideal ?ra%ton c%cle that has a pressure ratio of 12# a compressor inlet temperature of &00 7# and a turbineinlet temperature of 1000 7. etermine the reFuired mass flo rate of air fora net po er output of -0 GW# assuming both the compressor and the turbinehave an isentropic efficienc% of + a* 100 percent and + b* 8 percent. Assumeconstant specific heats at room temperature.
9olution:
. An air standard c%cle ith variable specific heats is e)ecuted in a closeds%stem and is composed of the follo ing four processes:
1 2 v c!nstant heat addition from 1".- psia and803= in the amount of &00 ?tu/lbm2 & P c!nstant heat addition to &200 H & " !sentropic e)pansion to 1".- psia" 1 P c!nstant heat re5ection to initial state+a* 9ho the c%cle on P"v and T s diagrams.+b* 'alculate the total heat input per unit mass.
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+c* etermine the thermal efficienc%
9olution:
10. ;he compression ratio of an ideal dual c%cle is 1". Air is at 100 k4a and&00 7 at the beginning of the compression process and at 2200 7 at the endof the heat addition process. eat transfer to air takes place partl% atconstant volume and partl% at constant pressure# and it amounts to 1 20."k$/kg. Assuming variable specific heats for air# determine + a* the fraction ofheat transferred at constant volume and + b* the thermal efficienc% of thec%cle.
9olution:
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