Chapter 5 the Laws of Thermodynamics: Entropy, Free
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Thermodynamics Notes
Thermodynamics Notes Steven K. Krueger Department of Atmospheric Sciences, University of Utah August 2020 Contents 1 Introduction 1 1.1 What is thermodynamics? . .1 1.2 The atmosphere . .1 2 The Equation of State 1 2.1 State variables . .1 2.2 Charles' Law and absolute temperature . .2 2.3 Boyle's Law . .3 2.4 Equation of state of an ideal gas . .3 2.5 Mixtures of gases . .4 2.6 Ideal gas law: molecular viewpoint . .6 3 Conservation of Energy 8 3.1 Conservation of energy in mechanics . .8 3.2 Conservation of energy: A system of point masses . .8 3.3 Kinetic energy exchange in molecular collisions . .9 3.4 Working and Heating . .9 4 The Principles of Thermodynamics 11 4.1 Conservation of energy and the first law of thermodynamics . 11 4.1.1 Conservation of energy . 11 4.1.2 The first law of thermodynamics . 11 4.1.3 Work . 12 4.1.4 Energy transferred by heating . 13 4.2 Quantity of energy transferred by heating . 14 4.3 The first law of thermodynamics for an ideal gas . 15 4.4 Applications of the first law . 16 4.4.1 Isothermal process . 16 4.4.2 Isobaric process . 17 4.4.3 Isosteric process . 18 4.5 Adiabatic processes . 18 5 The Thermodynamics of Water Vapor and Moist Air 21 5.1 Thermal properties of water substance . 21 5.2 Equation of state of moist air . 21 5.3 Mixing ratio . 22 5.4 Moisture variables . 22 5.5 Changes of phase and latent heats . -
ENERGY, ENTROPY, and INFORMATION Jean Thoma June
ENERGY, ENTROPY, AND INFORMATION Jean Thoma June 1977 Research Memoranda are interim reports on research being conducted by the International Institute for Applied Systems Analysis, and as such receive only limited scientific review. Views or opinions contained herein do not necessarily represent those of the Institute or of the National Member Organizations supporting the Institute. PREFACE This Research Memorandum contains the work done during the stay of Professor Dr.Sc. Jean Thoma, Zug, Switzerland, at IIASA in November 1976. It is based on extensive discussions with Professor HAfele and other members of the Energy Program. Al- though the content of this report is not yet very uniform because of the different starting points on the subject under consideration, its publication is considered a necessary step in fostering the related discussion at IIASA evolving around th.e problem of energy demand. ABSTRACT Thermodynamical considerations of energy and entropy are being pursued in order to arrive at a general starting point for relating entropy, negentropy, and information. Thus one hopes to ultimately arrive at a common denominator for quanti- ties of a more general nature, including economic parameters. The report closes with the description of various heating appli- cation.~and related efficiencies. Such considerations are important in order to understand in greater depth the nature and composition of energy demand. This may be highlighted by the observation that it is, of course, not the energy that is consumed or demanded for but the informa- tion that goes along with it. TABLE 'OF 'CONTENTS Introduction ..................................... 1 2 . Various Aspects of Entropy ........................2 2.1 i he no me no logical Entropy ........................ -
31 Jan 2021 Laws of Thermodynamics . L01–1 Review of Thermodynamics. 1
31 jan 2021 laws of thermodynamics . L01{1 Review of Thermodynamics. 1: The Basic Laws What is Thermodynamics? • Idea: The study of states of physical systems that can be characterized by macroscopic variables, usu- ally equilibrium states (mechanical, thermal or chemical), and possible transformations between them. It started as a phenomenological subject motivated by practical applications, but it gradually developed into a coherent framework that we will view here as the macroscopic counterpart to the statistical mechanics of the microscopic constituents, and provides the observational context in which to verify many of its predictions. • Plan: We will mostly be interested in internal states, so the allowed processes will include heat exchanges and the main variables will always include the internal energy and temperature. We will recall the main facts (definitions, laws and relationships) of thermodynamics and discuss physical properties that characterize different substances, rather than practical applications such as properties of specific engines. The connection with statistical mechanics, based on a microscopic model of each system, will be established later. States and State Variables for a Thermodynamical System • Energy: The internal energy E is the central quantity in the theory, and is seen as a function of some complete set of variables characterizing each state. Notice that often energy is the only relevant macroscopic conservation law, while momentum, angular momentum or other quantities may not need to be considered. • Extensive variables: For each system one can choose a set of extensive variables (S; X~ ) whose values specify ~ the equilibrium states of the system; S is the entropy and the X are quantities that may include V , fNig, ~ ~ q, M, ~p, L, .. -
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. -
Entropy and Life
Entropy and life Research concerning the relationship between the thermodynamics textbook, states, after speaking about thermodynamic quantity entropy and the evolution of the laws of the physical world, that “there are none that life began around the turn of the 20th century. In 1910, are established on a firmer basis than the two general American historian Henry Adams printed and distributed propositions of Joule and Carnot; which constitute the to university libraries and history professors the small vol- fundamental laws of our subject.” McCulloch then goes ume A Letter to American Teachers of History proposing on to show that these two laws may be combined in a sin- a theory of history based on the second law of thermo- gle expression as follows: dynamics and on the principle of entropy.[1][2] The 1944 book What is Life? by Nobel-laureate physicist Erwin Schrödinger stimulated research in the field. In his book, Z dQ Schrödinger originally stated that life feeds on negative S = entropy, or negentropy as it is sometimes called, but in a τ later edition corrected himself in response to complaints and stated the true source is free energy. More recent where work has restricted the discussion to Gibbs free energy because biological processes on Earth normally occur at S = entropy a constant temperature and pressure, such as in the atmo- dQ = a differential amount of heat sphere or at the bottom of an ocean, but not across both passed into a thermodynamic sys- over short periods of time for individual organisms. tem τ = absolute temperature 1 Origin McCulloch then declares that the applications of these two laws, i.e. -
The First Law of Thermodynamics for Closed Systems A) the Energy
Chapter 3: The First Law of Thermodynamics for Closed Systems a) The Energy Equation for Closed Systems We consider the First Law of Thermodynamics applied to stationary closed systems as a conservation of energy principle. Thus energy is transferred between the system and the surroundings in the form of heat and work, resulting in a change of internal energy of the system. Internal energy change can be considered as a measure of molecular activity associated with change of phase or temperature of the system and the energy equation is represented as follows: Heat (Q) Energy transferred across the boundary of a system in the form of heat always results from a difference in temperature between the system and its immediate surroundings. We will not consider the mode of heat transfer, whether by conduction, convection or radiation, thus the quantity of heat transferred during any process will either be specified or evaluated as the unknown of the energy equation. By convention, positive heat is that transferred from the surroundings to the system, resulting in an increase in internal energy of the system Work (W) In this course we consider three modes of work transfer across the boundary of a system, as shown in the following diagram: Source URL: http://www.ohio.edu/mechanical/thermo/Intro/Chapt.1_6/Chapter3a.html Saylor URL: http://www.saylor.org/me103#4.1 Attributed to: Israel Urieli www.saylor.org Page 1 of 7 In this course we are primarily concerned with Boundary Work due to compression or expansion of a system in a piston-cylinder device as shown above. -
Law of Conversation of Energy
Law of Conservation of Mass: "In any kind of physical or chemical process, mass is neither created nor destroyed - the mass before the process equals the mass after the process." - the total mass of the system does not change, the total mass of the products of a chemical reaction is always the same as the total mass of the original materials. "Physics for scientists and engineers," 4th edition, Vol.1, Raymond A. Serway, Saunders College Publishing, 1996. Ex. 1) When wood burns, mass seems to disappear because some of the products of reaction are gases; if the mass of the original wood is added to the mass of the oxygen that combined with it and if the mass of the resulting ash is added to the mass o the gaseous products, the two sums will turn out exactly equal. 2) Iron increases in weight on rusting because it combines with gases from the air, and the increase in weight is exactly equal to the weight of gas consumed. Out of thousands of reactions that have been tested with accurate chemical balances, no deviation from the law has ever been found. Law of Conversation of Energy: The total energy of a closed system is constant. Matter is neither created nor destroyed – total mass of reactants equals total mass of products You can calculate the change of temp by simply understanding that energy and the mass is conserved - it means that we added the two heat quantities together we can calculate the change of temperature by using the law or measure change of temp and show the conservation of energy E1 + E2 = E3 -> E(universe) = E(System) + E(Surroundings) M1 + M2 = M3 Is T1 + T2 = unknown (No, no law of conservation of temperature, so we have to use the concept of conservation of energy) Total amount of thermal energy in beaker of water in absolute terms as opposed to differential terms (reference point is 0 degrees Kelvin) Knowns: M1, M2, T1, T2 (Kelvin) When add the two together, want to know what T3 and M3 are going to be. -
Thermodynamic State Variables Gunt
Fundamentals of thermodynamics 1 Thermodynamic state variables gunt Basic knowledge Thermodynamic state variables Thermodynamic systems and principles Change of state of gases In physics, an idealised model of a real gas was introduced to Equation of state for ideal gases: State variables are the measurable properties of a system. To make it easier to explain the behaviour of gases. This model is a p × V = m × Rs × T describe the state of a system at least two independent state system boundaries highly simplifi ed representation of the real states and is known · m: mass variables must be given. surroundings as an “ideal gas”. Many thermodynamic processes in gases in · Rs: spec. gas constant of the corresponding gas particular can be explained and described mathematically with State variables are e.g.: the help of this model. system • pressure (p) state process • temperature (T) • volume (V) Changes of state of an ideal gas • amount of substance (n) Change of state isochoric isobaric isothermal isentropic Condition V = constant p = constant T = constant S = constant The state functions can be derived from the state variables: Result dV = 0 dp = 0 dT = 0 dS = 0 • internal energy (U): the thermal energy of a static, closed Law p/T = constant V/T = constant p×V = constant p×Vκ = constant system. When external energy is added, processes result κ =isentropic in a change of the internal energy. exponent ∆U = Q+W · Q: thermal energy added to the system · W: mechanical work done on the system that results in an addition of heat An increase in the internal energy of the system using a pressure cooker as an example. -
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. -
Nonequilibrium Thermodynamics and Scale Invariance
Article Nonequilibrium Thermodynamics and Scale Invariance Leonid M. Martyushev 1,2,* and Vladimir Celezneff 3 1 Technical Physics Department, Ural Federal University, 19 Mira St., Ekaterinburg 620002, Russia 2 Institute of Industrial Ecology, Russian Academy of Sciences, 20 S. Kovalevskaya St., Ekaterinburg 620219, Russia 3 The Racah Institute of Physics, Hebrew University of Jerusalem, Jerusalem 91904, Israel; [email protected] * Correspondence: [email protected]; Tel.: +7-92-222-77-425 Academic Editors: Milivoje M. Kostic, Miguel Rubi and Kevin H. Knuth Received: 30 January 2017; Accepted: 14 March 2017; Published: 16 March 2017 Abstract: A variant of continuous nonequilibrium thermodynamic theory based on the postulate of the scale invariance of the local relation between generalized fluxes and forces is proposed here. This single postulate replaces the assumptions on local equilibrium and on the known relation between thermodynamic fluxes and forces, which are widely used in classical nonequilibrium thermodynamics. It is shown here that such a modification not only makes it possible to deductively obtain the main results of classical linear nonequilibrium thermodynamics, but also provides evidence for a number of statements for a nonlinear case (the maximum entropy production principle, the macroscopic reversibility principle, and generalized reciprocity relations) that are under discussion in the literature. Keywords: dissipation function; nonequilibrium thermodynamics; generalized fluxes and forces 1. Introduction Classical nonequilibrium thermodynamics is an important field of modern physics that was developed for more than a century [1–5]. It is fundamentally based on thermodynamics and statistical physics (including kinetic theory and theory of random processes) and is widely applied in biophysics, geophysics, chemistry, economics, etc. -
Chapter 6. Time Evolution in Quantum Mechanics
6. Time Evolution in Quantum Mechanics 6.1 Time-dependent Schrodinger¨ equation 6.1.1 Solutions to the Schr¨odinger equation 6.1.2 Unitary Evolution 6.2 Evolution of wave-packets 6.3 Evolution of operators and expectation values 6.3.1 Heisenberg Equation 6.3.2 Ehrenfest’s theorem 6.4 Fermi’s Golden Rule Until now we used quantum mechanics to predict properties of atoms and nuclei. Since we were interested mostly in the equilibrium states of nuclei and in their energies, we only needed to look at a time-independent description of quantum-mechanical systems. To describe dynamical processes, such as radiation decays, scattering and nuclear reactions, we need to study how quantum mechanical systems evolve in time. 6.1 Time-dependent Schro¨dinger equation When we first introduced quantum mechanics, we saw that the fourth postulate of QM states that: The evolution of a closed system is unitary (reversible). The evolution is given by the time-dependent Schrodinger¨ equation ∂ ψ iI | ) = ψ ∂t H| ) where is the Hamiltonian of the system (the energy operator) and I is the reduced Planck constant (I = h/H2π with h the Planck constant, allowing conversion from energy to frequency units). We will focus mainly on the Schr¨odinger equation to describe the evolution of a quantum-mechanical system. The statement that the evolution of a closed quantum system is unitary is however more general. It means that the state of a system at a later time t is given by ψ(t) = U(t) ψ(0) , where U(t) is a unitary operator. -
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.