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Carnotization of Rankine Cycle
P M V Subbarao Professor Mechanical Engineering Department Enhance Mean Temperature of Heat Additions thru Additional Process …..
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Structure of Healthy Rankine Cycle
3sup 4sup 3sub 4sub T 2 1 s
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Historical Progress in Rankine Cycle
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Ill Effects of High Pressure Cycles
Why so? Why should an isentropic expansion lead to condensation??? x Pressure, MPa
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Few Low Temperature Resources and Their Capacities
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Characterization of Working Fluids for Rankine Cycle
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Working Fluids for Low Temperature Resources
Organic Substances must be selected in accordance to the heat source temperature level (Tcr < Tin source)
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Family of Rankine Cycles
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World Installed Capacity of ORC Plants
Total installed capacity : MWel, in 563 power plants New capacity planned : MWel in 75 plants
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Law of Recognition of New Concepts
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Progress in Steam 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 24.1 Th oC 260 316 454 482 538 566 565 Tr oC -- FHW 2 3 4 6 7 8 Pc,kPa 13.5 5.1 4.5 3.4 3.7 4.4 5.4 h,% ~17 27.6 30.5 35.6 37.5 39.8 39.5 40
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Reheating of Steam to Enhance Quality at the Turbine Exit
Single Turbine drum
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Analysis of Reheat Cycle
Consider reheat cycle as a combination of Rankine cycle and horn cycle. Cycle = Cycle ’-1 + Cycle 4’ ’. Therefore, 4’ 6
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Analysis of the Horn Cycle
4’ – 4 Isentropic Compression. 4 – 5 Isobaric Heat Addition. 5 – 6 Isentropic Expansion 6 – 4’ Isobaric(thermal) cooling. 4’ 6
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Clues to Achieve Double Benefit
Select appropriate reheat pressure, pRH, such that above function is maximum with better value of x.
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Procedure to Determine Optimum Reheat Pressure
Calculate the efficiency of Rankine cycle, hRankine. Calculate mean effective temperature of heat addition, Tm,in using s Find out pressure corresponding to Tm,in and entropy at HP turbine exit. Add reheating at this pressure and calculate efficiency of the Reheat Cycle.
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pmax= 15 MPa Tmax= 550 0C Tsat= C
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Effect of Reheat Pressure
Dh,% 1.0 0.2 0.4 0.6 0.8 ~0.3 prh/pmax
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Reheating : A Means to implement High Live Steam Pressure
Supercritical 593/6210C 593/5930C 565/5930C 565/5650C 538/5650C Improvement in Efficiency, % 538/5380C
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Super Critical Cycle ~ 1990
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Ultra Supercritical Installations of The World
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Single-Reheat Ultrasupercritical Product Line GE Power
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Double Reheat Ultra Super Critical Cycle
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Reheater Pressure Optimization for Double Reheat Units
97bar 110bar 69bar
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21st century Rankine Cycles
Improvement in Efficiency, %
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Super Critical Cycle of Year 2005
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Double Reheat Super Critical Plants
Net efficiency on natural gas is expected to reach 49%. Net efficiency on coal is expected to reach 47%.
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Double-Reheat Ultrasupercritical Product Line GE Power
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Advanced 700 8C Pulverised Coal-fired Power Plant Project
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FUTURE ULTRA SUPERCRITICAL PLANT – UNDER DEVELOPMENT
EFFICIENCY 55 %
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