Fundamentals Of Thermodynamics
10th Edition
ISBN: 9781119494966
Author: Borgnakke, C. (claus), Sonntag, Richard Edwin, Author.
Publisher: Wiley,
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An industrial process discharges 75.3 kg/s of gaseous combustion products at 204°C, 100 kPa
(properties at state 1). As shown in the figure, a proposed system for utilizing the combustion products
combines a heat-recovery steam generator with a well-insulated turbine. At steady state, combustion
products exit the steam generator at 130°C, 100 kPa, and a separate stream of water enters at 350 kPa,
46°C with a mass flow rate of 150 kg/min. At the exit of the turbine, the pressure is 7.5 kPa and the
quality is 88%. Heat is lost from the steam generator at a rate of 93600 kJ/h. The changes in kinetic and
potential energies of the flowing streams can be ignored as can the pressure drop for the water flowing
through the steam generator. The combustion products can be modeled as air acting as an ideal gas with
constant specific heats of Cv= 0.718 kJ/kg-K and Cp=1.005 kJ/kg-K. Use Rair = 0.287 kJ/kg-K. Also, for
the compressed liquid, assume the substance is a saturated liquid at the given…
An industrial process discharges 75.3 kg/s of gaseous combustion products at 204°C, 100 kPa (properties at state 1). As shown in the figure, a proposed system for utilizing the combustion products combines a heat-recovery steam generator with a well-insulated turbine. At steady state, combustion products exit the steam generator at 130°C, 100 kPa, and a separate stream of water enters at 350 kPa, 46°C with a mass flow rate of 150 kg/min. At the exit of the turbine, the pressure is 7.5 kPa and the quality is 88%. Heat is lost from the steam generator at a rate of 93600 kJ/h. The changes in kinetic and potential energies of the flowing streams can be ignored as can the pressure drop for the water flowing through the steam generator. The combustion products can be modeled as air acting as an ideal gas with constant specific heats of Cv= 0.718 kJ/kg-K and Cp=1.005 kJ/kg-K. Use Rair = 0.287 kJ/kg-K. Also, for the compressed liquid, assume the substance is a saturated liquid at the given…
is true for first law & second law efficiency (exergetic efficiency),
respectively.
+ x Carnot efficiency
and
Carnot efficiency
To
Exergy used
Exeryy supplied
Desired output
and
Supplied Input
Desired output
Exergy lost
and
Supplied Input
Exergy used
Entropy generation
Energy generation
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Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, mechanical-engineering and related others by exploring similar questions and additional content below.Similar questions
- Apply exergy analysis and calculate the exergy of three pressurised tanks (units: MJ) at the fully charged state. Where relevant, assume constant specific heats for airarrow_forward(2) Describe briefly why the following statements are wrong. (a) "Hot cup of coffee becoming cold spontaneously is an entropy-decreasing process. So the law of entropy increase can be violated." (b) “Air conditioners require bulky external unit, exhausting heat to outside. With the technology constantly advancing, external unit will be eliminated in the future."arrow_forwardGive an example of Exergy Destroyed During Mixing of Fluid Streams.arrow_forward
- An adiabatic turbine operating under stable conditions, steam 30 bar, at 360 ° C with a mass of 0.12 kg / sIt enters with flow rate and exits at 5 bar, 200 ° C. Neglecting the effects of motion and gravitya) the power produced by the turbine b) the exergy loss of the turbine and c) the exergy efficiency of the turbine.Find. (Take T0 = 20 ° ? ?? P0 = 1 ???!)arrow_forward8.6 Nozzle Flow of Air In a jet engine, hot combustion product (treat as air) enters the nozzle at 1500 K, 4 bar and is adiabatically expanded to the outside pressure of 0.5 bar. Determine outflow velocity and temperature for a reversible nozzle and for an irreversible nozzle with isentropic efficiency of 0.94.arrow_forwardP.2 (Application on Reversible process) Why the Engineers are considered the reversible processes is very important to study? P.3 (Application on Thermochemical Data for Q, U, H, Cv, and Cp) Calculate the internal-energy and enthalpy changes that occur when air is changed from an initial state of 277K and 10 bar, where is molar volume is 2.28 m3/Kmole, to a final state of 333K and 1 atm. Assume for air that PV/T is a constant and that C, = 21 and C, = 29.3 kJ/kgmole K.arrow_forward
- I need the answer as soon as possiblearrow_forwardAttempt all three subparts. a proper explanation is a mustarrow_forwardů EJERCICIO-2 9.66 WP A combined gas turbine-vapor power plant operates as shown in Fig. P9.66. Pressure and temperature data are given at prin- cipal states, and the net power developed by the gas turbine is 147 MW. Using air-standard analysis for the gas turbine, determine a. the net power, in MW, developed by the power plant. b. the overall thermal efficiency of the plant. T₂ = 690 K P₂= 13.6 bar 2- Air inlet Exhaust Compressor Ts = 400 K P5 = 1 bar P6 P7 FIGURE DO 66 6 Combustor T₁ = 300 K 1 P₁ = 1 bar Gas turbine ein www www Heat exchanger Pump 1p = 80% Steam cycle T3= 1580 K +3 P3= 13 bar Turbine -4 T4 = 900 K P4 = 1 bar T₁ = 520°C P = 100 bar Turbine Condenser 1₁ = 85% P9 = Ps= 0.08 bar W - gas 147 MW W vap Cookarrow_forward
- s) The device shown below is the one that extracts work from combustion. Combusted products can be regarded as ideal gases with constant specific heats, Cp= 1.4 kJ/kg-K, c₂= 1.0 kJ/kg.K. Every heat transfer occurs via a reversible process, and all work is produced via adiabatic reversible processes. Determine The heat transfer rate to the ambient that makes the engine reversible T = 540 °C P = 100 kPa m = 5 kg/s Combustion Gas Flow T = 40 °C P = 100 kPa QH Engine QL Ambient T = 21 °C, P = 100 kPa Warrow_forwardApply exergy balance to closed systems and control volumes.arrow_forward8.5 Adiabatic Throttle As part of a cooling cycle, CO2 is throttled from 20°C, 7 MPa to 2.5 MPa. Determine temperature, specific volume, enthalpy, and entropy of initial and end state, and put all in a table. Determine the entropy generation per unit mass and estimate the corresponding work loss.arrow_forward
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