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Selection of Rankine Cycles for Various Resources. P M V Subbarao Professor Mechanical Engineering Department. Match the Cycle and Resource …. Pressurised Water Reactor (PWR). - PowerPoint PPT Presentation
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Selection of Rankine Cycles for Various Resources
Match the Cycle and Resource …
P M V Subbarao
Professor
Mechanical Engineering Department
Pressurised Water Reactor (PWR)
– Over 60% of all installed commercial reactors are pressurised water reactors and like 85% of all reactors they use enriched Uranium as the fuel.
– The use of enriched fuel means that a higher power density is achievable in the core and thus better efficiency.
– PWR reactors use a two stage heat transfer system with ordinary (light) water acting as both a moderator and the coolant in the primary circuit.
– The water in the primary circuit reaches a temperature of about 325°C and must be at very high pressures, so that it can not boil.
– It gives up its heat in a second heat exchanger which produces the steam in the turbine circuit based on the Rankine cycle.
– Typical output power is 1000MW with a system efficiency of 33%.
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
Optimal Design of Vapour Power Plant
satcond pp
ambinCW TT ,
outCWT ,
?TTD
inssteam Tm , &
exitcsteam Tm , &
incwcw Tm , & exitcwcw Tm , &
Thermal Model of A Steam Condenser
Hot Well
Energy Balance of A Condenser
• Energy balance:
• The temperature rise of cooling water:
• 6 to 7 degree C for single pass.
• 7 to 9 degree C for double pass.
• 10 to 12 degree C for four pass.
LMWiWeWCWexitcincc TUATTCmhhm
,,
Condenser Temperature Vs Efficiency
0.30.320.340.360.380.4
0.420.440.46
0 20 40 60 80 100 120
Tc
Eff
Condenser Temperature Vs Quality
0.68
0.7
0.72
0.740.76
0.78
0.8
0.82
0 20 40 60 80 100 120
Tc
x4
0.265
0.270
0.275
0.280
0.2850.290
0.295
0.300
0.305
0.310
0 20 40 60 80 100 120
Tc
X4.E
ff
0
500
1000
1500
2000
2500
3000
3500
0 20 40 60 80 100 120
Qin
Wnet
c
Mean Effective Pressure
0100200300400500600700800
0 20 40 60 80 100 120
Tc
p, k
Pa
34
36
38
40
42
44
46
0 20 40 60 80 100 120 140
Pressure,bar
Eff
icie
ncy,%
tc=20 c ( 18 mm Hg)
tc=27 C (50 mm Hg)
tc=36 C (75 mm Hg)
Effect of inlet steam pressure (P) and condenser pressure on Rankine efficiency with constant inlet steam temperature of 470o C
Power Loss Due to Excess Back Pressure
Further Developments in Carnotization of Rankine Model
BY
P M V SubbaraoProfessor
Mechanical Engineering DepartmentI I T Delhi
Suppression of Non-Isothermal Heat Addition Zones…..
C
C
C
Reassessment Thru Carnot Model