a. A house ![]() |
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b. A physical property of a system that is independent of the system size and mass ![]() |
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c. An extensive property ![]() |
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d. A product of two extensive properties ![]() |
a. A traditional unit of energy equal to 1055 J ![]() |
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b. A traditional unit of energy equal to 1055 N ![]() |
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c. A unit of energy that stand for British Transition Unit ![]() |
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d. A unit of energy that stands for British Thermal Union ![]() |
a. In a closed system, no mass may be transferred in or out of the system boundaries. ![]() |
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b. In a closed system, no energy may be transferred in or out of the system boundaries. ![]() |
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c. In a closed system, both mass and energy cannot be transferred in or out of the system boundaries. ![]() |
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d. In a closed system, no work may be transferred in or out of the system boundaries. ![]() |
a. A specific property ![]() |
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b. A physical property of a system that depends on the system size and mass ![]() |
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c. An intensive property ![]() |
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d. A product of two intensive properties ![]() |
a. 203°K ![]() |
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b. 294°K ![]() |
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c. 270°K ![]() |
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d. 343°K ![]() |
a. 303°K ![]() |
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b. 260°K ![]() |
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c. 533°K ![]() |
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d. 500°K ![]() |
a. A series of identical thermodynamic processes ![]() |
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b. A thermodynamic process ![]() |
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c. A system in equilibrium ![]() |
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d. A series of thermodynamic processes that return to the first state of the first process ![]() |
a. Internal energy ![]() |
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b. Temperature ![]() |
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c. Heat capacity ![]() |
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d. Entropy ![]() |
a. kg/m ![]() |
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b. inch/lb ![]() |
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c. kg ![]() |
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d. m ![]() |
a. Boyle's law ![]() |
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b. Ideal gas law ![]() |
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c. Newton’s second law ![]() |
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d. f(P,V,T) = 0 ![]() |
a. 1.5 m3 ![]() |
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b. 1.1 m3 ![]() |
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c. 0.1 m3 ![]() |
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d. 1.9 m3 ![]() |
a. Vapor ![]() |
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b. Liquid-vapor mixture ![]() |
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c. Liquid ![]() |
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d. Solid ![]() |
a. Vapor ![]() |
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b. Liquid-vapor mixture ![]() |
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c. Liquid ![]() |
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d. Solid ![]() |
a. 0.52 kg/s ![]() |
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b. 0.152 kg/s ![]() |
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c. 0.258 kg/s ![]() |
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d. 1.65 kg/s ![]() |
a. 280°C ![]() |
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b. 100°C ![]() |
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c. 300°C ![]() |
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d. 250°C ![]() |
a. 300°C ![]() |
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b. 30°K ![]() |
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c. 30°C ![]() |
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d. 300°K ![]() |
a. 150°C ![]() |
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b. 200°K ![]() |
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c. 202°C ![]() |
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d. 100°K ![]() |
a. 3.25 MPa ![]() |
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b. 4.76 MPa ![]() |
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c. 1.76 bar ![]() |
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d. 15 atm ![]() |
a. 2 T ![]() |
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b. 1.5 T ![]() |
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c. 0.6 T ![]() |
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d. 0.5 T ![]() |
a. 100°C and 1 atm ![]() |
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b. 0°K and 611 Pa ![]() |
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c. 273°K and 1 MPa ![]() |
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d. 273°K and 611 Pa ![]() |
a. A process in which the system is perfectly insulated and heat transfer is zero ![]() |
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b. A process in which the temperature stays constant ![]() |
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c. A process in which the pressure stays constant ![]() |
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d. A process in which the volume of the system stays constant ![]() |
a. 29.5 kJ ![]() |
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b. 19.5 kJ ![]() |
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c. 49.5 kJ ![]() |
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d. 89.5 kJ ![]() |
a. Heat ![]() |
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b. Work ![]() |
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c. Potential energy ![]() |
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d. Entropy ![]() |
a. The transfer of thermal energy between regions of matter due to a temperature gradient ![]() |
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b. The transfer of energy due to bulk movement of liquids ![]() |
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c. The transfer of electrical energy from one object to another ![]() |
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d. The transfer of kinetic energy due to collision ![]() |
a. Radiation, friction, and convection ![]() |
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b. Convection, isobaric, and radiation ![]() |
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c. Conduction, isothermal, and isentropic ![]() |
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d. Conduction, convection, and radiation ![]() |
a. 70°C ![]() |
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b. 50°C ![]() |
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c. 30°C ![]() |
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d. 20°C ![]() |
a. 35.9°C ![]() |
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b. 75.2°C ![]() |
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c. 125.6°C ![]() |
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d. 25.4°C ![]() |
a. 219 kg ![]() |
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b. 299 kg ![]() |
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c. 179 kg ![]() |
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d. 359 kg ![]() |
a. 1223 kg ![]() |
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b. 142 kg ![]() |
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c. 697 kg ![]() |
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d. 47 kg ![]() |
a. Exergy ![]() |
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b. Entropy ![]() |
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c. Energy ![]() |
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d. Enthalpy ![]() |
a. 256 kJ ![]() |
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b. 22 kJ ![]() |
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c. 742 kJ ![]() |
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d. 1920 kJ ![]() |
a. -2.31 kJ ![]() |
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b. 4.52 kJ ![]() |
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c. -6.53 kJ ![]() |
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d. -3.55 kJ ![]() |
a. 610 kJ/kg ![]() |
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b. 510 kJ/kg ![]() |
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c. 710 kJ/kg ![]() |
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d. 210 kJ/kg ![]() |
a. Heat conduction happens only on solid materials. ![]() |
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b. Heat convection is independent of fluid velocity. ![]() |
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c. Heat transfer due to radiation increases linearly with temperature. ![]() |
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d. None of the above ![]() |
a. The first law of thermodynamics is an expression of the principle of conservation of energy. ![]() |
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b. The first law of thermodynamics states that energy can be transformed but cannot be created nor destroyed. ![]() |
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c. The internal energy of an isolated system is not constant. ![]() |
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d. Changes in internal energy (U) are due to a combination of heat (Q) added to the system and work done by the system (W). ![]() |
a. 3.6 kJ ![]() |
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b. 9.6 kJ ![]() |
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c. 6.4 kJ ![]() |
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d. 5.1 kJ ![]() |
a. The temperature of the system increases. ![]() |
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b. The temperature of the system decreases. ![]() |
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c. The internal energy of the system stays constant. ![]() |
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d. No energy is exchanged between the system and the surrounding. ![]() |
a. For any spontaneous process, the entropy of the universe increases. ![]() |
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b. Entropy cannot be created or destroyed. ![]() |
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c. Energy cannot be created or destroyed. ![]() |
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d. Energy = internal energy + kinetic energy + potential energy. ![]() |
a. Heat is always transferred from a hot object to a colder object. ![]() |
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b. Heat transfer occurs when the temperature of a system is different from the temperature of its surroundings. ![]() |
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c. The three major modes of heat transfer are conduction, convection, and radiation. ![]() |
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d. Internal energy of a system can only be changed due to heat transfer. ![]() |
a. It is not possible to build Carnot power cycle in practice. ![]() |
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b. A Carnot power cycle consists of 2 isentropic processes and 2 isothermal processes. ![]() |
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c. No engine operating between two heat reservoirs can be more efficient than a Carnot engine operating between those same reservoirs. ![]() |
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d. The thermal efficiency of a Rankine cycle can be made to be equal to that of a Carnot power cycle operating between the same cold and hot reservoirs. ![]() |
a. 0.13 ![]() |
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b. 0.52 ![]() |
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c. 0.22 ![]() |
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d. 0.76 ![]() |
a. Exergy is the minimum useful work possible during a process that brings the system into equilibrium with a heat reservoir. ![]() |
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b. Exergy is always destroyed in a process involving a temperature change. ![]() |
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c. Exergy is equivalent to entropy. ![]() |
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d. Exergy never reaches zero even after the system and surroundings reach equilibrium. ![]() |
a. For any spontaneous process, the entropy of the universe increases. ![]() |
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b. Entropy cannot be created or destroyed. ![]() |
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c. Energy cannot be created or destroyed. ![]() |
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d. Energy = internal energy + kinetic energy + potential energy. ![]() |
a. Two reversible isothermal processes and two adiabatic processes ![]() |
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b. Two irreversible isothermal processes and two adiabatic processes ![]() |
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c. Two isobaric processes and two adiabatic processes ![]() |
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d. Two reversible isentropic processes and two adiabatic processes ![]() |
a. T(s1 + s2)/2 ![]() |
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b. T (s2 - s1) ![]() |
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c. T (s1 - s2) ![]() |
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d. T s1/s2 ![]() |
a. Entropy expresses the degree of disorder in a system. ![]() |
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b. Entropy of an isolated system never decreases. ![]() |
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c. Entropy has the dimension of energy divided by temperature and a unit of joules per kelvin (J/K). ![]() |
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d. Entropy measures the energy available for useful work in a thermodynamic process. ![]() |
a. 75% ![]() |
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b. 40% ![]() |
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c. 65% ![]() |
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d. 50% ![]() |
a. Energy ![]() |
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b. Entropy ![]() |
||
c. Work ![]() |
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d. Exergy ![]() |
a. 0.123 ![]() |
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b. 0.232 ![]() |
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c. 0.517 ![]() |
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d. 0.721 ![]() |
a. 75% ![]() |
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b. 35% ![]() |
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c. 45% ![]() |
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d. 25% ![]() |
a. Isobaric ![]() |
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b. Isothermal ![]() |
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c. Adiabatic expansion ![]() |
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d. Isochoric ![]() |
a. 76% ![]() |
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b. 46% ![]() |
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c. 5% ![]() |
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d. 29% ![]() |
a. 0.31 ![]() |
||
b. 0.71 ![]() |
||
c. 0.41 ![]() |
||
d. 0.61 ![]() |
a. Carnot ![]() |
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b. Brayton ![]() |
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c. Diesel ![]() |
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d. Otto ![]() |
a. Carnot ![]() |
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b. Brayton ![]() |
||
c. Diesel ![]() |
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d. Otto ![]() |
a. Rankine ![]() |
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b. Lenoir ![]() |
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c. Diesel ![]() |
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d. Otto ![]() |
a. 6.3% ![]() |
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b. 17.2% ![]() |
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c. 15.3% ![]() |
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d. 20.2% ![]() |
a. 1 ![]() |
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b. 0.5 ![]() |
||
c. 2 ![]() |
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d. 4 ![]() |
a. 1.693 kJ/kg-K ![]() |
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b. 2.693 kJ/kg-K ![]() |
||
c. 3.693 kJ/kg-K ![]() |
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d. 0.693 kJ/kg-K ![]() |
a. 30% ![]() |
||
b. 50% ![]() |
||
c. 71% ![]() |
||
d. 60% ![]() |
a. 2.0 MJ ![]() |
||
b. 1.5 MJ ![]() |
||
c. 25.3 MJ ![]() |
||
d. 2.8 MJ ![]() |
a. 2.4% ![]() |
||
b. 25% ![]() |
||
c. 3.8% ![]() |
||
d. 5.2% ![]() |
a. 3.5 kJ ![]() |
||
b. 20 kJ ![]() |
||
c. 38 kJ ![]() |
||
d. 336 kJ ![]() |
a. 1.36 kW ![]() |
||
b. 2.25 kW ![]() |
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c. 3.10 kW ![]() |
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d. 0.53 kW ![]() |
a. 0.5 m3 ![]() |
||
b. 2 m3 ![]() |
||
c. 1 m3 ![]() |
||
d. 0.1 m3 ![]() |
a. 24% ![]() |
||
b. 5% ![]() |
||
c. 72% ![]() |
||
d. 10% ![]() |
a. 394 kJ/kmol K ![]() |
||
b. 19 kJ/kmol K ![]() |
||
c. 1.5 kJ/kmol K ![]() |
||
d. 80 kJ/kmol K ![]() |
a. 1113 kJ ![]() |
||
b. 2312 kJ ![]() |
||
c. 52 kJ ![]() |
||
d. 4905 kJ ![]() |
a. 6 kJ ![]() |
||
b. 600 kJ ![]() |
||
c. 0.6 kJ ![]() |
||
d. 6000 kJ ![]() |