Thermodynamics: An Engineering Approach
8th Edition
ISBN: 9780073398174
Author: Yunus A. Cengel Dr., Michael A. Boles
Publisher: McGraw-Hill Education
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Chapter 13.3, Problem 60P
To determine
The isentropic work output of the turbine.
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Chapter 13 Solutions
Thermodynamics: An Engineering Approach
Ch. 13.3 - Consider a mixture of several gases of identical...Ch. 13.3 - Somebody claims that the mass and mole fractions...Ch. 13.3 - The sum of the mole fractions for an ideal-gas...Ch. 13.3 - Consider a mixture of two gases. Can the apparent...Ch. 13.3 - What is the apparent molar mass for a gas mixture?...Ch. 13.3 - Prob. 6PCh. 13.3 - Consider a mixture of two gases A and B. Show that...Ch. 13.3 - The composition of moist air is given on a molar...Ch. 13.3 - Prob. 9PCh. 13.3 - Prob. 10P
Ch. 13.3 - Prob. 11PCh. 13.3 - Prob. 12PCh. 13.3 - Prob. 13PCh. 13.3 - Is a mixture of ideal gases also an ideal gas?...Ch. 13.3 - Express Daltons law of additive pressures. Does...Ch. 13.3 - Express Amagats law of additive volumes. Does this...Ch. 13.3 - How is the P-v-T behavior of a component in an...Ch. 13.3 - Prob. 18PCh. 13.3 - Prob. 19PCh. 13.3 - Prob. 20PCh. 13.3 - Prob. 21PCh. 13.3 - Consider a rigid tank that contains a mixture of...Ch. 13.3 - Is this statement correct? The volume of an...Ch. 13.3 - Is this statement correct? The temperature of an...Ch. 13.3 - Is this statement correct? The pressure of an...Ch. 13.3 - Prob. 26PCh. 13.3 - Prob. 27PCh. 13.3 - Prob. 28PCh. 13.3 - 13–29 A gas mixture at 350 K and 300 kPa has the...Ch. 13.3 - Prob. 30PCh. 13.3 - Prob. 31PCh. 13.3 - A rigid tank that contains 2 kg of N2 at 25C and...Ch. 13.3 - Prob. 33PCh. 13.3 - Prob. 34PCh. 13.3 - Prob. 35PCh. 13.3 - Prob. 36PCh. 13.3 - A 30 percent (by mass) ethane and 70 percent...Ch. 13.3 - Prob. 38PCh. 13.3 - Prob. 39PCh. 13.3 - Prob. 40PCh. 13.3 - Prob. 41PCh. 13.3 - Prob. 42PCh. 13.3 - Prob. 43PCh. 13.3 - Is the total internal energy of an ideal-gas...Ch. 13.3 - Prob. 45PCh. 13.3 - Prob. 46PCh. 13.3 - 13–47C Is the total internal energy change of an...Ch. 13.3 - Prob. 48PCh. 13.3 - Prob. 49PCh. 13.3 - The volumetric analysis of a mixture of gases is...Ch. 13.3 - Prob. 52PCh. 13.3 - Prob. 53PCh. 13.3 - Prob. 54PCh. 13.3 - Prob. 55PCh. 13.3 - Prob. 56PCh. 13.3 - An insulated tank that contains 1 kg of O2at 15C...Ch. 13.3 - Prob. 59PCh. 13.3 - Prob. 60PCh. 13.3 - Prob. 61PCh. 13.3 - Prob. 62PCh. 13.3 - Prob. 63PCh. 13.3 - Prob. 64PCh. 13.3 - Prob. 66PCh. 13.3 - Prob. 67PCh. 13.3 - Prob. 69PCh. 13.3 - A pistoncylinder device contains 6 kg of H2 and 21...Ch. 13.3 - Prob. 71PCh. 13.3 - Prob. 72PCh. 13.3 - Prob. 73PCh. 13.3 - Prob. 74PCh. 13.3 - Prob. 75PCh. 13.3 - Prob. 76PCh. 13.3 - Prob. 77PCh. 13.3 - Prob. 78PCh. 13.3 - Prob. 80PCh. 13.3 - Prob. 81PCh. 13.3 - Fresh water is obtained from seawater at a rate of...Ch. 13.3 - Prob. 83PCh. 13.3 - Prob. 84RPCh. 13.3 - The products of combustion of a hydrocarbon fuel...Ch. 13.3 - Prob. 89RPCh. 13.3 - Prob. 91RPCh. 13.3 - Prob. 92RPCh. 13.3 - A spring-loaded pistoncylinder device contains a...Ch. 13.3 - Prob. 94RPCh. 13.3 - Reconsider Prob. 1395. Calculate the total work...Ch. 13.3 - A rigid tank contains a mixture of 4 kg of He and...Ch. 13.3 - Prob. 97RPCh. 13.3 - Prob. 100RPCh. 13.3 - An ideal-gas mixture whose apparent molar mass is...Ch. 13.3 - 13–102 An ideal-gas mixture consists of 2 kmol of...Ch. 13.3 - An ideal-gas mixture consists of 2 kmol of N2and 4...Ch. 13.3 - Prob. 104FEPCh. 13.3 - Prob. 105FEPCh. 13.3 - An ideal-gas mixture consists of 3 kg of Ar and 6...Ch. 13.3 - Prob. 107FEPCh. 13.3 - Prob. 108FEPCh. 13.3 - Prob. 109FEPCh. 13.3 - Prob. 110FEP
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- A mixture of hydrocarbon gases is composed of 60 percent methane, 25 percent propane, and 15 percent butane by weight. This mixture is compressed from 100 kPa and 20°C to 1400 kPa in a reversible, isothermal, steady-flow compressor. Calculate the work and heat transfer for this compression per unit mass of the mixture. The universal gas constant is R₁ = 8.314 kPa-m³/kmol-K. Use the table containing the molar mass, gas constant, and critical-point properties. P₂ 60% CH4 25% C₂H₂ 15% C₂H10 (by mass) 100 kPa 20°C W The work input for this compression per unit mass of the mixture is The heat transfer for this compression per unit mass of the mixture is kJ/kg. kJ/kg.arrow_forwardA frictionless piston-cylinder device contains a saturated liquid-vapor mixture of water at 400K. During a constant pressure, process, 960 kJ of heat is transferred to the surrounding air at 300K. As a result, part of the water vapor contained in the cylinder condenses. Determine the entropy change of the water in kJ/K.arrow_forwardPls. refer to the answer key so that i will know if my solution is wrong.arrow_forward
- Determine the entropy change of 1.5 moles of ammonia that is heated from 180°C to 750°C. The system operates at an atmospheric pressure on a steady flow process.arrow_forwardIn a closed feedwater (FW) heater, a mixture enters the heater with a mass flow rate m1 and enthalpy h1 and leaves with an enthalpy h2. A second stream into the heater has a mass flow rate m2 and enthalpy h3 and it leaves with an enthalpy h4. What is a correct first law equation for this FW heater? m1·(h3 - h4) = m2·(h1 - h2) m1·(h1 - h2) = m2·(h4 - h3) m1·(h1 - h2) = m2·(h3 - h4) m1·m2 = (h1 -h2)·(h3 - h4) m1·(h1 - h3) = m2·(h2 - h4)arrow_forward2. In a power station, saturated steam is generated at 252°C by transferring heat from the hot gases gener- ated in the combustion chamber. The gases are cooled from 1100°C to 550°C during transferring the heat for steam generation. Determine the increase in total entropy of the combined system of gas and steam and increase in unavailable energy on the basis of one kg of steam generated. Assume water enters the boiler at saturated condition and leaves as saturated steam. [Ans. 1.99 kJ/K ; 597 kJ/kg of steam formed]arrow_forward
- a petrol working on a constant volume cycle has a compression ratio of 9 to 1. if the pressure and temperature of the petrol-vapor mixture at the beginning of compression assuming it follows the law PV^1.4=Carrow_forwardAn inventor claims to have created a machine that isothermally compresses 1 lbmol/hr of anideal gas at 1000 oR releasing 3000 Btu which is transferred to another 1 lbmol/hr of idealgas that expands isothermally from 2.72 atm to 1 atm. Is such a device possible or does thisprocess violate the second law? Assume the process is reversible. R = 1.987 Btu/lbmol oR.arrow_forwardA1 m3 vessel contains saturated vapor water at 100 kPa. The vessel was cooled to 70°C. The surrounding is at 27°C. Select all correct statements. O a. If cooling was done while maintaining the pressure at 100 kPa, the process would result in superheated steam. O b. The total mass of water in the vessel is 590.42 g. O c. Assuming the heat removed from cooling dissipated into the surroundings, the total change in entropy, AST, is 0.483 kJ/K. O d. After the cooling process, approximately 33.5% of the water is in the vapor phase O e. A total of 875.53 kJ of heat was removed from the system for the cooling process. Of. A total of 758.53 kJ of heat was removed from the system for the cooling process. g. Assuming the heat removed from cooling dissipated into the surroundings, the total change in entropy, AST, is 0.834 kJ/K.arrow_forward
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What is entropy? - Jeff Phillips; Author: TED-Ed;https://www.youtube.com/watch?v=YM-uykVfq_E;License: Standard youtube license