여재익, [email protected], (02) 880-9334 - 2006 Spring - 11
Next, we consider unsteady state Next, we consider unsteady state
• Unsteady Process
• filling closed tanks with a gas or liquid.
• discharge from closed vessels.
Basic assumptions are as follows:
• The control volume remains constant in relation to the coordinate frame.
• The state of the mass within the control volume may change with time,
• The state of the mass crossing each of the areas of flow on the control surface is constant with time, although the mass flow rate may vary with time.
=0
− +
∑
e∑
icv m m
dt
dm or
( m
2− m
1)
cv+ ∑ m
e− ∑ m
i= 0
(*)여재익, [email protected], (02) 880-9334 - 2006 Spring - 12
The first law becomes
Or
cv e e e e cv
i i i i
cv
V gz W
h dt m
gz dE h V
m
Q + ∑ ( + 2
2+ ) = + ∑ ( + 2
2+ ) +
cv cv e
e e e
i i i i cv
W V gz
u m V gz
u m V gz
h m
V gz h m Q
+ +
+
− + + +
+ +
= + + +
∑
∑
2 )]
( 2 )
( [ 2 )
(
2 ) (
1 2 1 1 1 2 2 2 2 2 2
---(**) To make any sense to these equations, consider example.
여재익, [email protected], (02) 880-9334 - 2006 Spring - 13
• Example 5-1
Steam at a pressure of 1.4Mpa, 300°C, is flowing in a pipe. An
evacuated tank is connected to this pipe through a valve. The valve is opened, the tank fills with steam until the pressure is 1.4 Mpa, and then the valve is closed. The process takes place adiabatically.
Kinetic energies and potential energies are negligible. Determine the final temperature of the steam.
0 0
=
=
= PE KE Q
δ δ δ
= 0 m
e여재익, [email protected], (02) 880-9334 - 2006 Spring - 14
• Solution to 5-1
1st law for this unsteady process is
The first law becomes
using continuity (*)
then the first law gives
cv e
e i
i
cv
m h m h m u m u W
Q + ( ) = ( ) +
2 2−
1 1+ 0
, 0
1=
= m m
e2 2
u m h m
i i=
0 )
( m
2− m
1+ m
e− m
i=
1
2
m
m =
u
2h
i=
여재익, [email protected], (02) 880-9334 - 2006 Spring - 15
Solution continued…
That is, the final internal energy of the steam in the tank is equal to the enthalpy of the steam entering the tank.
Look up superheated steam tank at
C T
MPa
p = 1 . 4 , = 300 °
, we findkJkg hi =3040.4
4 2
.
3040
u
h
i = =T
2 p2 =1.4MPaC T
2~ 450 °
Then use to find state from the table at
여재익, [email protected], (02) 880-9334 - 2006 Spring - 16
• Example 5-2
Consider the same tank as in 5-1. Let volume , saturated vapor at . The valve is then opened and steam from the line at 1.4 Mpa, 300°C flows into the tank until the pressure is 1.4 Mpa.
Calculate the mass of steam that flows into the tank.
4 3
. 0 m V= kPa
p1=350
= 0 m
e여재익, [email protected], (02) 880-9334 - 2006 Spring - 17
• Solution to 5-2
First consider mass balance (*)
1stLaw (**) becomes,
From saturated steam table at of saturated vapor. Thus
1
0
2
− m + m
e− m
i= m
1 1 2
2
u m u
m h
m
i i= −
m kg v
kPa
p
1= 350 ,
g= 0 . 52
3kg kg m
m v
m V
g
77 . 52 0
. 0
4 . 0
3 3 1
1
= = =
u kg kJ u
g= 2548 =
여재익, [email protected], (02) 880-9334 - 2006 Spring - 18
Solution 5-2 continued…
Again from the superheated steam table, as before at
(Trial & Error) Assume
Look up steam (superheated) vapor table at and
Must use 1st law (**) to check if guess was good.
kg kJ h
C T
MPa
p = 114 , = 300 ° ,
i= 3040 . 4
C T
2= 342 °
C
T2=342° p2=1.4MPa kg
kJ u
kg m
v2=0.1974 3 , 2=2855.8 -> kg
v
m V 2.026
2 2
2 = =
T2
3823 74 . 3818
) 2548 ( 77 . 0 ) 8 . 2855 ( 026 . 2 4 . 3040 ) 77 . 0 026 . 2 (
)
( 2 1 2 2 1 1
≈
−
≈
−
+
=
−m h mu mu
m i
여재익, [email protected], (02) 880-9334 - 2006 Spring - 19
OK guess was good!
Using C (*)
kg m m mi
256 . 1
77 . 0 026 . 2
1 2
=
−
=
−
=
여재익, [email protected], (02) 880-9334 - 2006 Spring - 20
• Example 5-3 (steady state case)
The mass rate of flow into a steam turbine is , and the heat transfer from the turbine is . The following data are known for the steam entering and leaving the turbine.
8 . 5 kW
s kg
5 . 1Determine the Power ( ) of the turbine.
W
여재익, [email protected], (02) 880-9334 - 2006 Spring - 21
• Solution to 5-3
This is a steady state problem.
Thus c
1stLaw (**) becomes
For , use superheated vapor table at
i e
i e cv
m m or
m m m m
=
=
− +
− ) 0
( 2 1
cv e e e e cv i i
i
cv V gz W
h t m d E gz d h V
m
Q + + + = + + + )+
( 2 2 )
(
2 2
1
hi pi=2MPaandTi =350°C Æ hi =3137kJkg
In the case of exit, use saturate vapor
kJ kg h
h
x MPa p
g e
e e
5 . 2675
% 100 ,
1 . 0
=
=
>
−
−
=
=
Upon substitution, kW W =655.7
여재익, [email protected], (02) 880-9334 - 2006 Spring - 22
• TA will solve extra practice problems from Chapter 5.
• We will next study the Second Law of Thermodynamics!
• GOOD LUCK, folks!
여재익, [email protected], (02) 880-9334 - 2006 Spring - 23
• Homework Set #4
• due 4/6 (We will have Midterm #1 on the same day)
• 5-3, 5-4, 5-6, 5-9, 5-15, 5-20, 5-26, 5-27, 5-31, 5-33