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ENGR 2213 Thermodynamics F. C. Lai School of Aerospace and Mechanical Engineering University of Oklahoma
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First Law of Thermodynamics E: total energy includes kinetic energy, potential energy and other forms of energy All other forms of energy are lumped together as the internal energy U. Internal energy U is an extensive property. Specific internal energy u = U/m is an intensive property Closed Systems
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Energy Analysis for a Control Volume Conservation of Mass Net Change in Mass within CV Total Mass Entering CV Total Mass Leaving CV = - Steady State
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Steady-Flow Process Conservation of mass Conservation of energy
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Steady-Flow Process Conservation of mass Conservation of energy For single-stream steady-flow process
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Uniform-Flow Process Conservation of Mass Conservation of Energy + (m 2 u 2 – m 1 u 1 ) CV
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Second Law of Thermodynamics It is impossible for any device that operates on a cycle to receive heat from a single reservoir and produce an equivalent amount of work. No heat engine can have a thermal efficiency of 100% Kelvin-Planck Statement The impossibility of having 100% efficiency heat engine is not due to friction or other dissipative effects.
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Second Law of Thermodynamics It is impossible to construct a device that operates on a cycle and produce no effect other than the transfer of heat from a low-temperature body to a high-temperature body. Clausius Statement Equivalence of the two statements A violation of one statement leads to the violation of the other statement.
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Second Law of Thermodynamics Carnot Principles 1.The efficiency of an irreversible heat engine is always less than that of a reversible one operating between the same two reservoirs. 2.The efficiencies of all reversible heat engines operating between the same two reservoirs are the same. A violation of either statement results in the Violation of the second law of thermodynamics.
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Entropy Change of an Ideal Gas T ds = du + p dv For an ideal gas, du = c v dT, pv = RT
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Entropy Change of an Ideal Gas T ds = dh - v dp For an ideal gas, dh = c p dT, pv = RT
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Isentropic Processes of Ideal Gases 1. Constant Specific Heats (a) (b)
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Isentropic Processes of Ideal Gases 1. Constant Specific Heats R = c p – c v k = c p /c v R/c v = k – 1 (a)
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Isentropic Processes of Ideal Gases 1. Constant Specific Heats R = c p – c v k = c p /c v R/c p = (k – 1)/k (b)
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Isentropic Processes of Ideal Gases 1. Constant Specific Heats Polytropic Processes pV n = constant n = 0 constant pressure isobaric processes n = 1 constant temperature isothermal processes n = k constant entropy isentropic processes n = ±∞ constant volume isometric processes p 1 V 1 k = p 2 V 2 k
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Isentropic Processes of Ideal Gases 2. Variable Specific Heats Relative Pressure p r = exp[sº(T)/R] ► is not truly a pressure ► is a function of temperature
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Isentropic Processes of Ideal Gases 2. Variable Specific Heats Relative Volume v r = RT/p r (T) ► is not truly a volume ► is a function of temperature
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Work reversible work in closed systems reversible work associated with an internally reversible process an steady-flow device ► The larger the specific volume, the larger the reversible work produced or consumed by the steady-flow device.
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Ideal Rankine Cycles T S 1 2 3 4 Process 1-2: isentropic compression in a pump Process 2-3: constant-pressure heat addition in a boiler Process 3-4: isentropic expansion in a turbine Process 4-1: constant-pressure heat rejection in a condenser Turbine Boiler Condenser Pump 1 2 3 4
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Ideal Reheat Rankine Cycles T S 1 2 3 4 Turbine Boiler Condenser Pump 1 2 3 4 Boiler Condenser Pump 1 2 3 6 4 5 T S 1 2 3 4 5 6
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Ideal Regenerative Rankine Cycles 1 2 3 7 4 5 6 P 1 Turbine Boiler Condenser P 2 FWH T S 1 2 3 4 5 7 6 Open Feedwater Heater
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Ideal Regenerative Rankine Cycles Closed Feedwater Heater 1 2 3 7 4 5 6 8 Trap TurbineBoiler Condenser P FWH y 1-y T S 1 2 3 4 5 7 68 y 1-y
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Otto Cycles Nikolaus A. Otto (1876) – four-stroke engine Beau de Rochas (1862)
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Diesel Cycles Rudolph Diesel (1890)
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Brayton Cycles
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