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Thermodynamics
Tutorial 3
Dr. SUN Weimeng
swe3@np.edu.sg
Office no.:6460 8342
Question 1
Solution:
(a) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
Question 1
2 2
1 2
1 2
1 2
2 2
in out
c c
mgZ mgZ m m
Q mh Q mh
 
   
1 2
2 1
159.1 / , 2803 /
( )
350 2.8(2803 159.1) 7752.92 /
in out
h kJ kg h kJ kg
Q Q m h h
kJ s
 
   
   
❶ compressed water at 38°C
❷dry saturated steam at 30 bar
Question 1
Solution:
(b) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
2 2
1 2
1 20; 0; ;
2 2
in in
c c
W Q mgZ mgZ m m   
1 2( )out outW m h h Q  
Question 1
❶ 450 °C and 30 bar superheated steam:
h1=3343 kJ/kg
❷ 0.42 bar and x=0.95 wet steam:
hf=323 kJ/kg; hg=2638 kJ/kg
2 (1 )
0.95 2638 0.05 323 2522.25 /
g fh xh x h
kJ kg
  
    
1 2( )
2.8(3343 2522.25) 130
2168.1 /
out outW m h h Q
kJ s
   
  

Question 2
Solution:
(a) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
2 2
1 2
1 20; 0; ;
2 2
in in
c c
W Q mgZ mgZ m m   
1 2( )out outW m h h Q  
Question 2
❶ 450 °C and 40 bar superheated steam:
h1=3330 kJ/kg
❷ 1.2 bar and x=0.95 wet steam:
hf=439 kJ/kg; hg=2683 kJ/kg
2 (1 )
0.95 2683 0.05 439 2570.8 /
g fh xh x h
kJ kg
  
    
1 2( )
2.8(3330 2570.8) 125
2000.76 /
out outW m h h Q
kJ s
   
  

Question 2
Solution:
(b) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
2 2
1 2
1 20; 0; 0; ;
2 2
in out in
c c
W W Q mgZ mgZ m m    
1 2( )outQ m h h 
Question 2
❶ Same as the 2nd stage of part (a):
h1=2570.8 kJ/kg
❷ 1.2 bar :
h2=hf=439 kJ/kg
1 2( )
2.8(2570.8 439)
5969.04 /
outQ m h h
kJ s
 
 

Question 3
Solution:
(a) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
2 2
1 2
1 20; 0; ;
2 2
in out
c c
W W mgZ mgZ m m   
2 1( )in outQ m h h Q  
Question 3
❶ 28 °C compressed water
h1=hf=117.3 kJ/kg
❷ 5 bar and x=0.68 wet steam:
hf=640 kJ/kg; hg=2749 kJ/kg
2 (1 )
0.68 2749 (1 0.68) 640 2074.12 /
g fh xh x h
kJ kg
  
     
2 1( )
1.2(2074.12 117.3) 30
2378.18 /
in outQ m h h Q
kJ s
  
  

Question 3
Solution:
(b) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
1 2 3
in outm m
m m m

 
 
22 2
31 2
1 1 1 2 2 2 3 3 3( ) ( ) ( )
2 2 2
in in out out
cc c
Q W m h gZ m h gZ Q W m h gZ           
22 2
31 2
1 1 2 2 3 3 1 2 3
0; 0; 0; 0;
;
2 2 2
in out in outW W Q Q
cc c
m gZ m gZ m gZ m m m
   
   
1 1 2 2 3 3m h m h m h 
Question 3
❶ Same as the 2nd stage of part (a):
h1=2074.12 kJ/kg
❷ 28 °C compressed water:
h2=hf=117.3 kJ/kg
❸ 75 °C compressed water:
h3=hf=313.9 kJ/kg
1 1 2 2 3 3
2 2
2
1.2 2074.12 117.3 (1.2 ) 313.9
10.74 /
m h m h m h
m m
m kg s
 
     

3 10.74 1.2 11.94 /m kg s   
Question 4
Solution:
(a) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
1 2 3
in outm m
m m m

 
 
22 2
31 2
1 1 1 2 2 2 3 3 3( ) ( ) ( )
2 2 2
in in out out
cc c
Q W m h gZ m h gZ Q W m h gZ           
22 2
31 2
1 1 2 2 3 3 1 2 3
0; 0; 0; 0;
;
2 2 2
in out in outW W Q Q
cc c
m gZ m gZ m gZ m m m
   
   
1 1 2 2 3 3m h m h m h 
1
2
3
m wet steam
m cold water
m hot water



Question 4
❶ 5 bar and x=0.62 wet steam:
hf=640 kJ/kg; hg=2749 kJ/kg
❷ 29 °C compressed water:
h2=hf=121.5 kJ/kg
❸ 70 °C compressed water:
h3=hf=293 kJ/kg
1 (1 )
0.62 2749 (1 0.62) 640
1947.58 /
g fh xh x h
kJ kg
  
    

Question 4
Take
Hence
Apply
Since
Hence
1 1 2 2 3 3m h m h m h 
1
2
m
x
m

1 2 3m m m 
1 2m xm
3 2(1 )m x m  
2 1 2 2 2 3(1 )xm h m h x m h   
1 2 3(1 )xh h x h  
3 2
1 3
293 121.5
0.1037
1947.58 293
h h
x
h h
 
  
 
Question 4
Solution:
(b) Apply the continuity flow equation
Apply the steady flow energy
Since
Hence
1 2 3
in outm m
m m m

 
 
22 2
31 2
1 1 1 2 2 2 3 3 3( ) ( ) ( )
2 2 2
in in out out
cc c
Q W m h gZ m h gZ Q W m h gZ           
22 2
31 2
1 1 2 2 3 3 1 2 3
0; 0; 0; 0;
;
2 2 2
in out in outW W Q Q
cc c
m gZ m gZ m gZ m m m
   
   
1 1 2 2 3 3m h m h m h 
1
2
3
m wet steam
m cold water
m hot water



Question 4
❶ 5 bar and x=0.62 wet steam:
hf=640 kJ/kg; hg=2749 kJ/kg
❷ 29 °C compressed water:
h2=hf=121.5 kJ/kg
1 (1 )
0.62 2749 (1 0.62) 640
1947.58 /
g fh xh x h
kJ kg
  
    

Question 4
Apply
Since
Hence
1 1 2 2 3 3m h m h m h 
1 2 3m m m 
3 0.6 5.2 5.8 /m kg s   
1 1 2 2
3
3
0.6 1947.58 5.2 121.5
5.8
310.4 /
m h m h
h
m
kJ kg
   
  

70 ; 293 /
?; 310.4 /
75 ; 313.9 /
f
f
f
t C h kJ kg
t h kJ kg
t C h kJ kg
 
 
 
70 310.4 293
75 70 313.9 293
74.16
t
t C
 

 
 
Thank you
Q & A

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Thermodynamics t3

  • 1. Thermodynamics Tutorial 3 Dr. SUN Weimeng swe3@np.edu.sg Office no.:6460 8342
  • 2. Question 1 Solution: (a) Apply the continuity flow equation Apply the steady flow energy Since Hence
  • 3. Question 1 2 2 1 2 1 2 1 2 2 2 in out c c mgZ mgZ m m Q mh Q mh       1 2 2 1 159.1 / , 2803 / ( ) 350 2.8(2803 159.1) 7752.92 / in out h kJ kg h kJ kg Q Q m h h kJ s           ❶ compressed water at 38°C ❷dry saturated steam at 30 bar
  • 4. Question 1 Solution: (b) Apply the continuity flow equation Apply the steady flow energy Since Hence 2 2 1 2 1 20; 0; ; 2 2 in in c c W Q mgZ mgZ m m    1 2( )out outW m h h Q  
  • 5. Question 1 ❶ 450 °C and 30 bar superheated steam: h1=3343 kJ/kg ❷ 0.42 bar and x=0.95 wet steam: hf=323 kJ/kg; hg=2638 kJ/kg 2 (1 ) 0.95 2638 0.05 323 2522.25 / g fh xh x h kJ kg         1 2( ) 2.8(3343 2522.25) 130 2168.1 / out outW m h h Q kJ s        
  • 6. Question 2 Solution: (a) Apply the continuity flow equation Apply the steady flow energy Since Hence 2 2 1 2 1 20; 0; ; 2 2 in in c c W Q mgZ mgZ m m    1 2( )out outW m h h Q  
  • 7. Question 2 ❶ 450 °C and 40 bar superheated steam: h1=3330 kJ/kg ❷ 1.2 bar and x=0.95 wet steam: hf=439 kJ/kg; hg=2683 kJ/kg 2 (1 ) 0.95 2683 0.05 439 2570.8 / g fh xh x h kJ kg         1 2( ) 2.8(3330 2570.8) 125 2000.76 / out outW m h h Q kJ s        
  • 8. Question 2 Solution: (b) Apply the continuity flow equation Apply the steady flow energy Since Hence 2 2 1 2 1 20; 0; 0; ; 2 2 in out in c c W W Q mgZ mgZ m m     1 2( )outQ m h h 
  • 9. Question 2 ❶ Same as the 2nd stage of part (a): h1=2570.8 kJ/kg ❷ 1.2 bar : h2=hf=439 kJ/kg 1 2( ) 2.8(2570.8 439) 5969.04 / outQ m h h kJ s     
  • 10. Question 3 Solution: (a) Apply the continuity flow equation Apply the steady flow energy Since Hence 2 2 1 2 1 20; 0; ; 2 2 in out c c W W mgZ mgZ m m    2 1( )in outQ m h h Q  
  • 11. Question 3 ❶ 28 °C compressed water h1=hf=117.3 kJ/kg ❷ 5 bar and x=0.68 wet steam: hf=640 kJ/kg; hg=2749 kJ/kg 2 (1 ) 0.68 2749 (1 0.68) 640 2074.12 / g fh xh x h kJ kg          2 1( ) 1.2(2074.12 117.3) 30 2378.18 / in outQ m h h Q kJ s       
  • 12. Question 3 Solution: (b) Apply the continuity flow equation Apply the steady flow energy Since Hence 1 2 3 in outm m m m m      22 2 31 2 1 1 1 2 2 2 3 3 3( ) ( ) ( ) 2 2 2 in in out out cc c Q W m h gZ m h gZ Q W m h gZ            22 2 31 2 1 1 2 2 3 3 1 2 3 0; 0; 0; 0; ; 2 2 2 in out in outW W Q Q cc c m gZ m gZ m gZ m m m         1 1 2 2 3 3m h m h m h 
  • 13. Question 3 ❶ Same as the 2nd stage of part (a): h1=2074.12 kJ/kg ❷ 28 °C compressed water: h2=hf=117.3 kJ/kg ❸ 75 °C compressed water: h3=hf=313.9 kJ/kg 1 1 2 2 3 3 2 2 2 1.2 2074.12 117.3 (1.2 ) 313.9 10.74 / m h m h m h m m m kg s          3 10.74 1.2 11.94 /m kg s   
  • 14. Question 4 Solution: (a) Apply the continuity flow equation Apply the steady flow energy Since Hence 1 2 3 in outm m m m m      22 2 31 2 1 1 1 2 2 2 3 3 3( ) ( ) ( ) 2 2 2 in in out out cc c Q W m h gZ m h gZ Q W m h gZ            22 2 31 2 1 1 2 2 3 3 1 2 3 0; 0; 0; 0; ; 2 2 2 in out in outW W Q Q cc c m gZ m gZ m gZ m m m         1 1 2 2 3 3m h m h m h  1 2 3 m wet steam m cold water m hot water   
  • 15. Question 4 ❶ 5 bar and x=0.62 wet steam: hf=640 kJ/kg; hg=2749 kJ/kg ❷ 29 °C compressed water: h2=hf=121.5 kJ/kg ❸ 70 °C compressed water: h3=hf=293 kJ/kg 1 (1 ) 0.62 2749 (1 0.62) 640 1947.58 / g fh xh x h kJ kg         
  • 16. Question 4 Take Hence Apply Since Hence 1 1 2 2 3 3m h m h m h  1 2 m x m  1 2 3m m m  1 2m xm 3 2(1 )m x m   2 1 2 2 2 3(1 )xm h m h x m h    1 2 3(1 )xh h x h   3 2 1 3 293 121.5 0.1037 1947.58 293 h h x h h       
  • 17. Question 4 Solution: (b) Apply the continuity flow equation Apply the steady flow energy Since Hence 1 2 3 in outm m m m m      22 2 31 2 1 1 1 2 2 2 3 3 3( ) ( ) ( ) 2 2 2 in in out out cc c Q W m h gZ m h gZ Q W m h gZ            22 2 31 2 1 1 2 2 3 3 1 2 3 0; 0; 0; 0; ; 2 2 2 in out in outW W Q Q cc c m gZ m gZ m gZ m m m         1 1 2 2 3 3m h m h m h  1 2 3 m wet steam m cold water m hot water   
  • 18. Question 4 ❶ 5 bar and x=0.62 wet steam: hf=640 kJ/kg; hg=2749 kJ/kg ❷ 29 °C compressed water: h2=hf=121.5 kJ/kg 1 (1 ) 0.62 2749 (1 0.62) 640 1947.58 / g fh xh x h kJ kg         
  • 19. Question 4 Apply Since Hence 1 1 2 2 3 3m h m h m h  1 2 3m m m  3 0.6 5.2 5.8 /m kg s    1 1 2 2 3 3 0.6 1947.58 5.2 121.5 5.8 310.4 / m h m h h m kJ kg         70 ; 293 / ?; 310.4 / 75 ; 313.9 / f f f t C h kJ kg t h kJ kg t C h kJ kg       70 310.4 293 75 70 313.9 293 74.16 t t C       