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Typology: Exercises
Uploaded on 05/30/2020
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3 /kg and v g = 0.08609 m 3 /kg (Table A-4).
Analysis ( a ) Two phases coexist in equilibrium, thus we have a saturated liquid-vapor mixture. The pressure of the steam is the
saturation pressure at the given temperature. Then the pressure in the tank must be the saturation pressure at the specified temperature,
P T sat@220C 2320 kPa
( b ) The total mass and the quality are determined as
1 3.94kg 0.08609m/kg
2/3 (1.8m)
504 .2kg 0.001190m/kg
1/3 (1.8m)
3
3
3
3
t
g
t f g
g
g g
f
f f
m
m x
m m m
m
m
v
V
v
V
( c ) The density is determined from
3 287.8kg/ m
( ) 0. 001190 ( 0. 0269 )( 0. 08609 ) 0. 003474 m/kg 3
f x g f
on the boiling pressure and temperature is negligible. 3 No air has leaked into the pan during cooling.
Properties The saturation pressure of water at 20C is 2.3392 kPa (Table A-4).
Analysis Noting that the weight of the lid is negligible, the reaction force F on the lid after cooling at the pan-lid interface can be
determined from a force balance on the lid in the vertical direction to be
PA +F = PatmA
or,
= 6997 mPa= (since 1 Pa= 1 N/m )
( 101 , 325 2339. 2 )Pa 4
( 0. 3 m)
2 2
2
2
The weight of the pan and its contents is
( 8 kg)(9.81m/s)= 78.5N
2 W mg
which is much less than the reaction force of 6997 N at the pan-lid interface. Therefore, the pan will move up together with the lid
when the person attempts to open the pan by lifting the lid up. In fact, it looks like the lid will not open even if the mass of the pan and
its contents is several hundred kg.
Properties The density of liquid water is approximately = 1000 kg/m 3 .
Analysis The pressure at the bottom of the 5-cm pan is the saturation pressure corresponding to
the boiling temperature of 98C:
94.39kPa sat@98 C P P (Table A-4)
The pressure difference between the bottoms of two pans is
3.43kPa 1000 kg/ms
1 kPa (1000 kg/m)(9.807m/s)(0.35m) 2
3 2
Then the pressure at the bottom of the 40-cm deep pan is
P = 94.39 + 3.43 = 97.82 kPa
Then the boiling temperature becomes
T boiling T [email protected] 99.0 C (Table A-5)
3
P
Patm = 1 atm mmHg
2.3392 kPa
40 cm
5 cm
( c ) The quality at the final state is specified to be x 2 = 0.5. The specific volumes at the
initial and the final states are
0.25799m/kg 300 C
1.0 MPa 3 1 1
1
^ v T
(Table A-6)
0 .09775m/kg
1.0MPa
3
2 2 2
2
f x fg x
Thus,
3 Δ ( )(0.8kg)(0.0977 5 0.25799)m/kg 0.128 2 m
3
3 /kg and uf = 850.46 kJ/kg (Table A-4).
Analysis ( a ) The tank initially contains saturated liquid water and air. The volume occupied by water is
3 3
which is the 25 percent of total volume. Then, the total volume is determined from
3 ( 0. 001619 ) 0.006476 m
( b ) Properties after the heat addition process are
0.006476 m 3
3
2 ^ m
2
2
2
2
3 2
u
x
21,367kPa
v (Table A-4 or A-5)
( c ) The total internal energy change is determined from
U m ( u 2 u 1 )( 1. 4 kg)(2201.5-850.46)kJ/kg 1892 kJ
T [email protected] MPa = 242.6C (Table A-5)
Then, the initial temperature becomes
T 1 = 242.6+5 = 247.6 C
Also, 2821. 1 kJ/kg
6 C
5 MPa 1 1
1
h T
(Table A-6)
( b ) The properties of steam when the piston first hits the stops are
001235 m/kg
7 kJ/kg
0
2
2
2 1
h
x
(Table A-5)
T
2
1
Then, the enthalpy change of steam becomes
h h 2 h 1 1049. 7 2821.1 -1771kJ/kg
( c ) At the final state
1555 kPa
3
3
3
3 3 2
200 C
x
(Table A-4)
The cylinder contains saturated liquid-vapor mixture with a small mass of vapor at the final state.