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Analysis of Rankine Cycle with Multiple OFWHs. P M V Subbarao Professor Mechanical Engineering Department I I T Delhi. Translation of an Engineering solution into Mathematical Model ..…. Analysis of Regeneration through OFWH. Workoutput of bleed Steam. h5-h6. Progress in Rankine Cycle. - PowerPoint PPT Presentation
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Analysis of Rankine Cycle with Multiple OFWHs
P M V SubbaraoProfessor
Mechanical Engineering DepartmentI I T Delhi
Translation of an Engineering solution into Mathematical Model ..…..
Analysis of Regeneration through OFWH
26
23
hh
hhy
45 hhmQ in
171 hhymQOut
pumpscondbleednet WWWW
0
pumpsW
7565 1 hhyhhymWWW condbleednet
0
200
400
600
800
1000
1200
1400
1600
0 0.1 0.2 0.3 0.4 0.5
h5-h
6Workoutput of bleed Steam
26
23
hh
hhy
Progress in Rankine Cycle
Year 1907 1919 1938 1950 1958 1959 1966 1973 1975
MW 5 20 30 60 120 200 500 660 1300
p,MPa 1.3 1.4 4.1 6.2 10.3 16.2 15.9 15.9 24.1
Th oC 260 316 454 482 538 566 566 565 538
Tr oC -- -- -- -- 538 538 566 565 538
FHW -- 2 3 4 6 6 7 8 8
Pc,kPa 13.5 5.1 4.5 3.4 3.7 3.7 4.4 5.4 5.1
,% -- ~17 27.6 30.5 35.6 37.5 39.8 39.5 40
Open (Direct Contact) Feed Water Heater
Closed Feed Water Heater (Pumped Condensate)
Closed Feed Water Heater (Throttled Condensate)
Closed Feed Water Heater (Expanded Condensate)
Thermodynamic Analysis of A Power Plant
C
OFWH
OFWH
OFWH
Turbine
yj, hbjYj-11,hbj-1 Yj-2,hbj-2
1- yj – yj-1- yj-2
hf (j-3)
1- yj – yj-1
hf (j-2)
1- yj
hf (j-1)
1 ,hf (j)
A MATHEMATICAL MODEL
SG
A
B
C
n number of OFWHs require n+1 no of Pumps…..
ANALYSIS OF ‘ith’ FEED WATER HEATER
• Mass entering the turbine is STEAM TURBINE
n
iiSGcond ymm
1
1
y1,
hb1
yi,
hbi
y(i-1)
hb(i-1)
mie ,
hfi
mi,i,
hf(i-1)
STEAM IN
STEAM OUT
SGm
SGm
Mass of steam leaving the turbine is
OPTIMIZATION METHODOLOGY
The power developed by the bleed steam of ith heater before it is being extracted is given by
hs
yi
hbj
TURBINE
)( bisiSGbi hhymW
SGm
OPTIMIZATION METHODOLOGY (Contd..)
The work done by the all the feed water heaters is given by:
n
ibisiSG
n
ibi hhymW
11
)(
ANALYSIS OF ‘ith’ FEED WATER HEATER
)1(1
,
n
ijjSGei ymm
)1(,
n
ijjSGii ymm
yi , hbi
hfi h f i-1
ith heater
eim ,iim ,
Mass balance of the heater at inlet and exit is given by:
• Energy balance of the feed heater gives:
fi
n
ijjbiifi
n
ijj hyhyhy
11 11
yi , hbi
hfi h f i-1
ith heater
eim ,iim ,
fi
n
ijjbiifiifi
n
ijj hyhyhyhy
111
1
11
fieibiiSGfiii hmhymhm ,1,
fi
n
ijjSGbiiSGfi
n
ijjSG hymhymhym
11 11
1
11
1
ifif
n
ijjifbi hhyhhy
i
1
1
1
1
ifib
ififn
ijji hh
hhyy
Neglecting pump work
ifib
ififn
ijji hh
hhyy
1
1
21 1
1
11
2
1
ifib
ififi
n
ijji hh
hhyyy
1
1
1
1
22
11
ifib
ifif
ifib
ififn
ijj
n
ijji hh
hh
hh
hhyyy
1
1
1
1
2
11
ifib
ifif
ifib
ififn
ijji hh
hh
hh
hhyy
1
1
1
1
2
11
ifib
ifif
ifib
ififn
ijji hh
hh
hh
hhyy
1
1
1
12
3
11
ifib
ifif
ifib
ififi
n
ijji hh
hh
hh
hhyyy
12
12
32 1
ifib
ififn
ijji hh
hhyy
1
1
1
1
12
12
33
111
ifib
ifif
ifib
ifif
ifib
ififn
ijj
n
ijji hh
hh
hh
hh
hh
hhyyy
1
1
1
1
12
12
3
111
ifib
ifif
ifib
ifif
ifib
ififn
ijji hh
hh
hh
hh
hh
hhyy
1
1
1
1
12
12
3
111
ifib
ifif
ifib
ifif
ifib
ififn
ijji hh
hh
hh
hh
hh
hhyy
1
1
1
1
12
12
21
21 11.....11
ifib
ifif
ifib
ifif
ifib
ifif
nfnb
nfnf
ni hh
hh
hh
hh
hh
hh
hh
hhyy
1
1
nfnb
nfnfn hh
hhy
1
1
1
1
21
21
1
1 1.....11
ifib
ifif
ifib
ifif
nfnb
nfnf
nfnb
nfnfi hh
hh
hh
hh
hh
hh
hh
hhy
1
1
1 1
11
ifib
ififn
ij jfjb
jfjf
i hh
hh
hh
hhy
01
01
2 1
11 1
fb
ffn
j jfjb
jfjf
hh
hh
hh
hhy
1
1
1 1
11
ifib
ififn
ij jfjb
jfjf
i hh
hh
hh
hhy
1
1
1 1
1 111ifib
ififn
ij jfjb
jfjf
i hh
hh
hh
hhy
1
1
1 1
1 111ifib
ififn
ij jfjb
jfjf
i hh
hh
hh
hhy