Carnot Cycle and Heat Engine Fundamentals and Applications • Michel Feidt Carnot Cycle and Heat Engine Fundamentals and Applications
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Arxiv:2008.06405V1 [Physics.Ed-Ph] 14 Aug 2020 Fig.1 Shows Four Classical Cycles: (A) Carnot Cycle, (B) Stirling Cycle, (C) Otto Cycle and (D) Diesel Cycle
Investigating student understanding of heat engine: a case study of Stirling engine Lilin Zhu1 and Gang Xiang1, ∗ 1Department of Physics, Sichuan University, Chengdu 610064, China (Dated: August 17, 2020) We report on the study of student difficulties regarding heat engine in the context of Stirling cycle within upper-division undergraduate thermal physics course. An in-class test about a Stirling engine with a regenerator was taken by three classes, and the students were asked to perform one of the most basic activities—calculate the efficiency of the heat engine. Our data suggest that quite a few students have not developed a robust conceptual understanding of basic engineering knowledge of the heat engine, including the function of the regenerator and the influence of piston movements on the heat and work involved in the engine. Most notably, although the science error ratios of the three classes were similar (∼10%), the engineering error ratios of the three classes were high (above 50%), and the class that was given a simple tutorial of engineering knowledge of heat engine exhibited significantly smaller engineering error ratio by about 20% than the other two classes. In addition, both the written answers and post-test interviews show that most of the students can only associate Carnot’s theorem with Carnot cycle, but not with other reversible cycles working between two heat reservoirs, probably because no enough cycles except Carnot cycle were covered in the traditional Thermodynamics textbook. Our results suggest that both scientific and engineering knowledge are important and should be included in instructional approaches, especially in the Thermodynamics course taught in the countries and regions with a tradition of not paying much attention to experimental education or engineering training. -
Particular Characteristics of Transcritical CO2 Refrigeration Cycle with an Ejector
Applied Thermal Engineering 27 (2007) 381–388 www.elsevier.com/locate/apthermeng Particular characteristics of transcritical CO2 refrigeration cycle with an ejector Jian-qiang Deng a, Pei-xue Jiang b,*, Tao Lu b, Wei Lu b a Department of Process Equipment and Control Engineering, School of Energy and Power Engineering, Xi’an Jiaotong University, Xi’an 710049, China b Key Laboratory for Thermal Science and Power Engineering, Department of Thermal Engineering, Tsinghua University, Beijing 100084, China Received 4 April 2005; accepted 16 July 2006 Available online 26 September 2006 Abstract The present study describes a theoretical analysis of a transcritical CO2 ejector expansion refrigeration cycle (EERC) which uses an ejector as the main expansion device instead of an expansion valve. The system performance is strongly coupled to the ejector entrain- ment ratio which must produce the proper CO2 quality at the ejector exit. If the exit quality is not correct, either the liquid will enter the compressor or the evaporator will be filled with vapor. Thus, the ejector entrainment ratio significantly influences the refrigeration effect with an optimum ratio giving the ideal system performance. For the working conditions studied in this paper, the ejector expansion sys- tem maximum cooling COP is up to 18.6% better than the internal heat exchanger cycle (IHEC) cooling COP and 22.0% better than the conventional vapor compression refrigeration cycle (VCRC) cooling COP. At the conditions for the maximum cooling COP, the ejector expansion cycle refrigeration output is 8.2% better than the internal heat exchanger cycle refrigeration output and 11.5% better than the conventional cycle refrigeration output. -
Exergy Accounting - the Energy That Matters V
THE 8th LATIN-AMERICAN CONGRESS ON ELECTRICITY GENERATION AND TRANSMISSION - CLAGTEE 2009 1 Exergy Accounting - The Energy that Matters V. Fachina, PETROBRAS 1 Exergy means the maximum work which can be Abstract-- The exergy concept is introduced by utilizing a extracted from a control volume. Also it is the maximum general framework on which are based the model equations. An energy quantity which can be made useful after discounting exergy analysis is performed on a case study: a control volume the irreversible losses. Finally, exergy means a physical, for a power module is created by comprising gas turbine, chemical contrast level between a control volume and its reduction gearbox, AC generator, exhaustion ducts and heat nearby surroundings. regenerator. The implementation of the equations is carried out Now considering the economical realm, Fig. 1 can be by collecting test data of the equipment data sheets from the respective vendors. By utilizing an exergy map, one proposes translated as follows: the reversible losses as either business both mitigating and contingent countermeasures for maximizing productivity losses or refundable taxes; the irreversible ones the exergy efficiency. An exergy accounting is introduced by as either nonrefundable taxes or inflation; the right arrows as showing how the exergy concept might eventually be brought up product and service values; the left ones as product and to the traditional money accounting. At last, one devises a unified service investments. approach for efficiency metrics in order to bridge the gaps A word of advice: a control volume means either a between the physical and the economical realms. physical or logical reality subset bounded by our observation. -
Physics 170 - Thermodynamic Lecture 40
Physics 170 - Thermodynamic Lecture 40 ! The second law of thermodynamic 1 The Second Law of Thermodynamics and Entropy There are several diferent forms of the second law of thermodynamics: ! 1. In a thermal cycle, heat energy cannot be completely transformed into mechanical work. ! 2. It is impossible to construct an operational perpetual-motion machine. ! 3. It’s impossible for any process to have as its sole result the transfer of heat from a cooler to a hotter body ! 4. Heat flows naturally from a hot object to a cold object; heat will not flow spontaneously from a cold object to a hot object. ! ! Heat Engines and Thermal Pumps A heat engine converts heat energy into work. According to the second law of thermodynamics, however, it cannot convert *all* of the heat energy supplied to it into work. Basic heat engine: hot reservoir, cold reservoir, and a machine to convert heat energy into work. Heat Engines and Thermal Pumps 4 Heat Engines and Thermal Pumps This is a simplified diagram of a heat engine, along with its thermal cycle. Heat Engines and Thermal Pumps An important quantity characterizing a heat engine is the net work it does when going through an entire cycle. Heat Engines and Thermal Pumps Heat Engines and Thermal Pumps Thermal efciency of a heat engine: ! ! ! ! ! ! From the first law, it follows: Heat Engines and Thermal Pumps Yet another restatement of the second law of thermodynamics: No cyclic heat engine can convert its heat input completely to work. Heat Engines and Thermal Pumps A thermal pump is the opposite of a heat engine: it transfers heat energy from a cold reservoir to a hot one. -
Advanced Organic Vapor Cycles for Improving Thermal Conversion Efficiency in Renewable Energy Systems by Tony Ho a Dissertation
Advanced Organic Vapor Cycles for Improving Thermal Conversion Efficiency in Renewable Energy Systems By Tony Ho A dissertation submitted in partial satisfaction of the requirements for the degree of Doctor of Philosophy in Engineering – Mechanical Engineering in the Graduate Division of the University of California, Berkeley Committee in charge: Professor Ralph Greif, Co-Chair Professor Samuel S. Mao, Co-Chair Professor Van P. Carey Professor Per F. Peterson Spring 2012 Abstract Advanced Organic Vapor Cycles for Improving Thermal Conversion Efficiency in Renewable Energy Systems by Tony Ho Doctor of Philosophy in Mechanical Engineering University of California, Berkeley Professor Ralph Greif, Co-Chair Professor Samuel S. Mao, Co-Chair The Organic Flash Cycle (OFC) is proposed as a vapor power cycle that could potentially increase power generation and improve the utilization efficiency of renewable energy and waste heat recovery systems. A brief review of current advanced vapor power cycles including the Organic Rankine Cycle (ORC), the zeotropic Rankine cycle, the Kalina cycle, the transcritical cycle, and the trilateral flash cycle is presented. The premise and motivation for the OFC concept is that essentially by improving temperature matching to the energy reservoir stream during heat addition to the power cycle, less irreversibilities are generated and more power can be produced from a given finite thermal energy reservoir. In this study, modern equations of state explicit in Helmholtz energy such as the BACKONE equations, multi-parameter Span- Wagner equations, and the equations compiled in NIST REFPROP 8.0 were used to accurately determine thermodynamic property data for the working fluids considered. Though these equations of state tend to be significantly more complex than cubic equations both in form and computational schemes, modern Helmholtz equations provide much higher accuracy in the high pressure regions, liquid regions, and two-phase regions and also can be extended to accurately describe complex polar fluids. -
Physics 100 Lecture 7
2 Physics 100 Lecture 7 Heat Engines and the 2nd Law of Thermodynamics February 12, 2018 3 Thermal Convection Warm fluid is less dense and rises while cool fluid sinks Resulting circulation efficiently transports thermal energy 4 COLD Convection HOT Turbulent motion of glycerol in a container heated from below and cooled from above. The bright lines show regions of rapid temperature variation. The fluid contains many "plumes," especially near the walls. The plumes can be identified as mushroom-shaped objects with heat flowing through the "stalk" and spreading in the "cap." The hot plumes tend to rise with their caps on top; falling, cold plumes are cap-down. All this plume activity is carried along in an overall counterclockwise "wind" caused by convection. Note the thermometer coming down from the top of the cell. Figure adapted from J. Zhang, S. Childress, A. Libchaber, Phys. Fluids 9, 1034 (1997). See detailed discussion in Kadanoff, L. P., Physics Today 54, 34 (August 2001). 5 The temperature of land changes more quickly than the nearby ocean. Thus convective “sea breezes” blow ____ during the day and ____ during the night. A. onshore … onshore B. onshore … offshore C. offshore … onshore D. offshore … offshore 6 The temperature of land changes more quickly than the nearby ocean. Thus convective “sea breezes” blow ____ during the day and ____ during the night. A. onshore … onshore B.onshore … offshore C.offshore … onshore D.offshore … offshore 7 Thermal radiation Any object whose temperature is above zero Kelvin emits energy in the form of electromagnetic radiation Objects both absorb and emit EM radiation continuously, and this phenomenon helps determine the object’s equilibrium temperature 8 The electromagnetic spectrum 9 Thermal radiation We’ll examine this concept some more in chapter 6 10 Why does the Earth cool more quickly on clear nights than it does on cloudy nights? A. -
Analysis of a CO2 Transcritical Refrigeration Cycle with a Vortex Tube Expansion
sustainability Article Analysis of a CO2 Transcritical Refrigeration Cycle with a Vortex Tube Expansion Yefeng Liu *, Ying Sun and Danping Tang University of Shanghai for Science and Technology, Shanghai 200093, China; [email protected] (Y.S.); [email protected] (D.T.) * Correspondence: [email protected]; Tel.: +86-21-55272320; Fax: +86-21-55272376 Received: 25 January 2019; Accepted: 19 March 2019; Published: 4 April 2019 Abstract: A carbon dioxide (CO2) refrigeration system in a transcritical cycle requires modifications to improve the coefficient of performance (COP) for energy saving. This modification has become more important with the system’s more and more widely used applications in heat pump water heaters, automotive air conditioning, and space heating. In this paper, a single vortex tube is proposed to replace the expansion valve of a traditional CO2 transcritical refrigeration system to reduce irreversible loss and improve the COP. The principle of the proposed system is introduced and analyzed: Its mathematical model was developed to simulate and compare the system performance to the traditional system. The results showed that the proposed system could save energy, and the vortex tube inlet temperature and discharge pressure had significant impacts on COP improvement. When the vortex tube inlet temperature was 45 ◦C, and the discharge pressure was 9 MPa, the COP increased 33.7%. When the isentropic efficiency or cold mass fraction of the vortex tube increased, the COP increased about 10%. When the evaporation temperature or the cooling water inlet temperature of the desuperheater decreased, the COP also could increase about 10%. The optimal discharge pressure correlation of the proposed system was established, and its influences on COP improvement are discussed. -
Fuel Cells Versus Heat Engines: a Perspective of Thermodynamic and Production
Fuel Cells Versus Heat Engines: A Perspective of Thermodynamic and Production Efficiencies Introduction: Fuel Cells are being developed as a powering method which may be able to provide clean and efficient energy conversion from chemicals to work. An analysis of their real efficiencies and productivity vis. a vis. combustion engines is made in this report. The most common mode of transportation currently used is gasoline or diesel engine powered automobiles. These engines are broadly described as internal combustion engines, in that they develop mechanical work by the burning of fossil fuel derivatives and harnessing the resultant energy by allowing the hot combustion product gases to expand against a cylinder. This arrangement allows for the fuel heat release and the expansion work to be performed in the same location. This is in contrast to external combustion engines, in which the fuel heat release is performed separately from the gas expansion that allows for mechanical work generation (an example of such an engine is steam power, where fuel is used to heat a boiler, and the steam then drives a piston). The internal combustion engine has proven to be an affordable and effective means of generating mechanical work from a fuel. However, because the majority of these engines are powered by a hydrocarbon fossil fuel, there has been recent concern both about the continued availability of fossil fuels and the environmental effects caused by the combustion of these fuels. There has been much recent publicity regarding an alternate means of generating work; the hydrogen fuel cell. These fuel cells produce electric potential work through the electrochemical reaction of hydrogen and oxygen, with the reaction product being water. -
Recording and Evaluating the Pv Diagram with CASSY
LD Heat Physics Thermodynamic cycle Leaflets P2.6.2.4 Hot-air engine: quantitative experiments The hot-air engine as a heat engine: Recording and evaluating the pV diagram with CASSY Objects of the experiment Recording the pV diagram for different heating voltages. Determining the mechanical work per revolution from the enclosed area. Principles The cycle of a heat engine is frequently represented as a closed curve in a pV diagram (p: pressure, V: volume). Here the mechanical work taken from the system is given by the en- closed area: W = − ͛ p ⋅ dV (I) The cycle of the hot-air engine is often described in an idealised form as a Stirling cycle (see Fig. 1), i.e., a succession of isochoric heating (a), isothermal expansion (b), isochoric cooling (c) and isothermal compression (d). This description, however, is a rough approximation because the working piston moves sinusoidally and therefore an isochoric change of state cannot be expected. In this experiment, the pV diagram is recorded with the computer-assisted data acquisition system CASSY for comparison with the real behaviour of the hot-air engine. A pressure sensor measures the pressure p in the cylinder and a displacement sensor measures the position s of the working piston, from which the volume V is calculated. The measured values are immediately displayed on the monitor in a pV diagram. Fig. 1 pV diagram of the Stirling cycle 0210-Wei 1 P2.6.2.4 LD Physics Leaflets Setup Apparatus The experimental setup is illustrated in Fig. 2. 1 hot-air engine . 388 182 1 U-core with yoke . -
Finite-Time Thermodynamic Model for Evaluating Heat Engines in Ocean Thermal Energy Conversion
entropy Article Finite-Time Thermodynamic Model for Evaluating Heat Engines in Ocean Thermal Energy Conversion Takeshi Yasunaga * and Yasuyuki Ikegami Institute of Ocean Energy, Saga University, 1 Honjo-Machi, Saga 840-8502, Japan; [email protected] * Correspondence: [email protected] Received: 14 January 2020; Accepted: 11 February 2020; Published: 13 February 2020 Abstract: Ocean thermal energy conversion (OTEC) converts the thermal energy stored in the ocean temperature difference between warm surface seawater and cold deep seawater into electricity. The necessary temperature difference to drive OTEC heat engines is only 15–25 K, which will theoretically be of low thermal efficiency. Research has been conducted to propose unique systems that can increase the thermal efficiency. This thermal efficiency is generally applied for the system performance metric, and researchers have focused on using the higher available temperature difference of heat engines to improve this efficiency without considering the finite flow rate and sensible heat of seawater. In this study, our model shows a new concept of thermodynamics for OTEC. The first step is to define the transferable thermal energy in the OTEC as the equilibrium state and the dead state instead of the atmospheric condition. Second, the model shows the available maximum work, the new concept of exergy, by minimizing the entropy generation while considering external heat loss. The maximum thermal energy and exergy allow the normalization of the first and second laws of thermal efficiencies. These evaluation methods can be applied to optimized OTEC systems and their effectiveness is confirmed. Keywords: finite-time thermodynamics; reversible heat engine; normalized thermal efficiency; maximum work; exergy; entropy generation 1. -
15 Evaluating on Exergy Analysis of Refrigeration
International Journal of Engineering & Applied Sciences (IJEAS) Vol.4, Issue 4(2012)15-25 EVALUATING ON EXERGY ANALYSIS OF REFRIGERATION SYSTEM WITH TWO-STAGE AND ECONOMISER Bayram Kılıç 1* , Osman İpek 2, Sinan U ğuz 3 1Bucak Emin Gülmez Vocational School, Mehmet Akif Ersoy University, Bucak, 15300, Burdur, Turkey 2Engineering&Architecture Faculty, Mechanical Engineering, Süleyman Demirel University,32260,Isparta, Turkey 3Bucak Zeliha Tolunay Applied Technology and Management School, Mehmet Akif Ersoy University, , Bucak, 15300, Burdur, Turkey *Corresponding Author: E-mail: [email protected] Recived: 26 December 2012 Abstract In this study, the first and second law analysis of vapor compression refrigeration cycle with two-stage and economiser were carried out. R134a was used in system as refrigerant. The necessary thermodynamic values for analyses were calculated by Solkane program. The coefficient of performance (COP), exergetic efficiency ( ηex) and total irreversibility rate of the system in the different operating conditions were investigated for this refrigerant. As a result, the highest coefficient of performance value and exergy efficiency value was obtained in the condenser temperature 25 oC and evaporator temperature 5 oC in the refrigeration system with two-stage and economiser. The highest irreversibility value was obtained in the condenser temperature 45 oC and evaporator temperature -15 oC in the refrigeration system. Keywords: Refrigeration system, COP, exergy analysis, two-stage. 1. Introduction Single-stage compression process can give quite satisfactory results for the evaporation temperatures until -15 oC in vapor compression refrigeration cycles of condensation temperatures is not too high. However, the capacity of cooling cycle together with the coefficient of performance rapidly decreases in working conditions are very low evaporation temperatures. -
Energy and Exergy Analyses of Angra 2 Nuclear Power Plant
2017 International Nuclear Atlantic Conference - INAC 2017 Belo Horizonte, MG, Brazil, October 22-27, 2017 ASSOCIAÇÃO BRASILEIRA DE ENERGIA NUCLEAR – ABEN ENERGY AND EXERGY ANALYSES OF ANGRA 2 NUCLEAR POWER PLANT João G. O. Marques, Antonella L. Costa, Claubia Pereira, Ângela Fortini Universidade Federal de Minas Gerais Departamento de Engenharia Nuclear – Escola de Engenharia Av. Antônio Carlos Nº 6627, Campus Pampulha, CEP 31270-901, Belo Horizonte, MG, Brasil [email protected], [email protected], [email protected], [email protected] ABSTRACT Nuclear Power Plants (NPPs) based on Pressurized Water Reactors (PWRs) technology are considered an alternative to fossil fuels plants due to their reliability with low operational cost and low CO2 emissions. An example of PWR plant is Angra 2 built in Brazil. This NPP has a nominal electric power output of 1300 MW and made it possible for the country save its water resources during electricity generation from hydraulic plants, and improved Brazilian knowledge and technology in nuclear research area. Despite all these benefits, PWR plants generally have a relatively low thermal efficiency combined with a large amount of irreversibility generation or exergy destruction in their components, reducing their capacity to produce work. Because of that, it is important to assess such systems to understand how each component impacts on system efficiency. Based on that, the aim of this work is to evaluate Angra 2 by performing energy and exergy analyses to quantify the thermodynamic performance of this PWR plant and its components. The methodology consists in the development of a mathematical model in EES (Engineering Equation Solver) software based on thermodynamic states in addition to energy and exergy balance equations.