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Closed Brayton Cycle Power Conversion Design James C. Conklin 18 February 2004 conklinjc@ornl.gov
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The Advanced High Temperature Reactor 03-239R
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Brayton Cycles Brief History Open cycle –G. Brayton, 1872, piston –A. Elling, 1903, gas turbine –O. von Ohain & F. Whittle, 1930’s, aircraft Closed cycle –Ackeret & Keller, 1935 2 MWe demonstration, 1939 –~20 systems built
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Brayton Cycle Demonstrator 3-kWe, 1962
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Experimental Split-shaft Automotive Turbomachine
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CBC Design Outline Cycle performance –Calculate flows and state points Heat exchanger design –Pressure drop –Size, footprint Turbomachine design –Flow path –Stage design
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Simple CBC
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Heat Flows Simple Cycle
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Three Reheat-Intercooling
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Cycle Performance Parameters Determine Performance Compressor pressure ratio Allowable pressure drop Turbomachine polytropic efficiencies Turbine inlet/compressor inlet temp ratio Recuperator effectiveness Compressor intercooling Turbine reheat
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Simple Cycle Performance
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Derivation of Cycle Performance Simple Cycle-I
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Derivation of Cycle Performance Simple Cycle-II
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Derivation of Cycle Performance Simple Cycle-III
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Derivation of Cycle Performance Simple Cycle-IIII
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Compressor Intercooling
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Sample Parameter Variations- Helium
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“Spider Plot” Shows Parameter Sensitivity
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Working Fluid Affects Cycle Performance
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Heat Exchanger Design Method from Kays & London
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Ntu-effectiveness method For sizing problem with balanced flow For rating problem with balanced flow
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Recuperator Design Requires Finned Surface Detail
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Working Fluid, Pressure and Pressure Drop Affects Size (and Costs)
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Turbomachinery Characteristics Choice of flow geometry, determine mass and volume flow of working fluid from cycle efficiency and state point calculations –Radial (<1 MW) –Axial (>1 MW)
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Euler Pump/Turbine Fundamental Relationship
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Flow and Stage Loading Coefficient Determination
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Turbomachine Map To Determine Velocity Triangle(s)
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Blade Speed Must Be Chosen Tip speed/sonic <1 Blade stress Generator limit –Gearbox might be necessary –Frequency conversion –Bearings
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For constant mass flow and shaft power, annulus area varies inversely with pressure, resulting in smaller and faster machine
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Design Trade-offs Must Be Evaluated-I Working fluid choice –Nitrogen: well-developed turbomachine infrastructure(+), higher thermal efficiency(+), large heat exchangers(-), low sonic speed(-) –Helium: turbomachine infrastructure development needed(-), larger turbomachine (-), lower efficiency(-), small heat exchangers(+), high sonic speed(+) –HeXe mixtures: Sonic speed low(-), good compromise for other parameters, but development done only for small (~100 kWe), radial flow machines.
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Design Trade-offs Must Be Evaluated-II Pressure: High pressure generally results in smaller, but heavier equipment. Possible increase in number of stages Pressure drop: efficiency & size as P/P HX effectiveness: efficiency & size as Intercooling and reheat: efficiency & size as number . Increased P/P might negate possible efficiency gain
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References Staundt, R.L., 1987, Design Study of an MGR Direct Brayton-Cycle Power Plant, MITNPI-TR-018, The Massachusetts Institute of Technology, Cambridge, Massachusetts. Kays, W.M., and London, A.L, 1984, Compact Heat Exchangers, 3 rd Edition, McGraw Hill Pierce, B.L., 1982, “The Influence of Recent Heat Transfer Data on Gas Mixtures (He-Ar, H 2 -CO 2 ) on Closed Cycle Gas Turbines, Journal of Engineering for Power, Vol. 103, pp. 114-117 Wilson, D.G., and Korakianitis, T. 1998, The Design of High Efficiency Turbomachinery and Gas Turbines, 2 nd Edition, Prentice Hall
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