A Survey of Basic Thermodynamics

Total Page:16

File Type:pdf, Size:1020Kb

A Survey of Basic Thermodynamics A SURVEY OF BASIC THERMODYNAMICS W. F. Vinen School of Physics and Astronomy, University of Birmingham, Birmingham B15 2TT, UK Abstract A brief summary is given of the thermodynamics that underlies the use of su- perconducting and cryogenic techniques in particle accelerators and detectors. It is intended to remind participants at the School of basic principles, and it is not an introduction to the subject. A rigorous treatment is not possible within the limited space available. 1. INTRODUCTION: MACROSTATES AND MICROSTATES Thermodynamics is concerned with macroscopic systems, with the concept of temperature, and with the way in which the behaviour of such systems is constrained by very general principles, called the Laws of Thermodynamics, which originate from a recognition that the random motion of particles in the system is governed by general statistical principles. It describes macroscopic systems by macroscopic parameters, such as pressure, p, volume, V , magnetization, M~ , applied magnetic field, H~ , and total internal energy, E, all of which have obvious meanings, and it introduces new and more subtle macroscopic parameters, such the temperature, T , and entropy, S. The constraints are expressed in terms of allowed relationships between these parameters. The so-called extensive quantities, V; M~ ; E and S, are proportional to the mass of material present; we shall generally assume that each relates to one mole. The various macroscopic parameters define a macrostate of the system. We can also think about a microscopic state, or microstate, of the system, defined, for example, by specifying the energy or position of each individual atom or molecule. It is crucial to understand that a very large number of different microstates correspond to the same macrostate. For example, the same total internal energy, E, can come about from a very large number of different ways of distributing this energy among the individual atoms or molecules. We denote this large number by W . Other things being equal, the probability of the system being found in one microstate is the same as that of finding it in another microstate. Thus the probability that the system is in a given macrostate must be proportional to the corresponding number, W , of microstates. The number of microstates, W , is often called the statistical weight. 2. INTERNAL ENERGY AND THE FIRST LAW OF THERMODYNAMICS In essence the First Law states that, if the macroscopic parameters such as pressure, volume, magnetiza- tion and applied magnetic field are specified, then so also is the internal energy, E. For a non-magnetic fluid system, the important parameters are usually p and V . Then the First Law states that E is a properly defined function of p and V : E = E(p; V ). If you take a fluid system through some cycle and return it to its original p and V , its internal energy returns to its original value. We say that E is a function of state. Obvious? No, it depends on the fact that the individual molecules are very quickly randomized among all the accessible microstates, the accessible microstates being those that are consistent with the given p and V . The previous history is irrelevant. 3. ENTROPY AND THE SECOND LAW OF THERMODYNAMICS The number of microstates, W , is a very useful parameter because it relates to the probability of finding a given macrostate. But W is usually an inconveniently large number, so it is better to work in terms of ln W . We define the entropy as S = kB ln W , where kB is a constant, the value of which will be fixed later. Note that if we have two systems, A and B, the number of microstates of the combined system is WAWB, so that the combined entropy is additive; it is similarly proportional to the mass of the system. The Second Law of Thermodynamics states in part that S is a function of state: S = S(p; V ). Again, not obvious, but again depends on the fact that a system quickly randomizes over the accessible microstates (consistent with the given p and V ), independently of the previous history. 4. THE PRINCIPLE OF INCREASE IN ENTROPY This Principle completes our statement of the Second Law. Suppose that a system is isolated from its surroundings, so that any change in the system can have no effect on the surroundings and vice versa. Then, if the system can be imagined to exist in two macroscopic states, corresponding to two different values of W , it is more likely to be found in the one with the larger W . In practice, one value of W is usually enormously larger than the other, so that the system will almost certainly be found in the one with the larger W . In other words, in the one with the larger entropy. For example, consider a gas in a box. Suppose that at some initial time all the gas were in the left hand side of the box, corresponding to W = W1. If the gas were allowed to fill the whole box, W = W2. It turns out that W2 >>>> W1. So the gas must expand to fill the whole box, in the sense that it must have only a negligible probability of being found in one side of the box only. In this sense entropy tends to a maximum value. Note that the principle that a system tends to maximize its entropy applies only to an isolated system. Otherwise one would need to worry about changes in W or S for the surroundings. Often systems are not isolated, and therefore in due course we shall look for principles that are more convenient to use than the Principle of Increase in Entropy. 5. THE KELVIN TEMPERATURE We define the Kelvin temperature by the relation: T = (@E=@S)V . Why? And does this definition accord with our everyday experience? Suppose that we have two systems, A and B, between which energy can flow, while each is maintained at constant volume (this flow of energy is actually a flow of “heat”). The two systems are not isolated from each other, and therefore we can apply the principle of increase in entropy only to the combined system. If we transfer energy δE from one system to the other we have @S @S δS = A δE − B δE: (1) @E @E A V B V (Remember that S is additive.) Therefore maximizing the entropy means that TA = TB. Therefore equilibrium requires equality of Kelvin temperature, in accord with our experience. (Note that we have in fact proved that the concept of temperature is meaningful; this is related to what is sometimes called the Zeroth Law of Thermodynamics.) If initially TA > TB, (heat) energy must flow from A to B (hot to cold), if S is to increase, which again accords with our expectations. 6. THE BOLTZMANN DISTRIBUTION, AND THE MEANING OF T = 0 Imagine a volume of gas, at constant volume, V , and constant internal energy, E0. Focus on one particu- lar molecule of the gas. If its energy is , the rest of the gas has energy E0 − . Therefore the probability that the molecule has this energy is the probability that the rest of the system has energy E0 − . We might try writing for this probability @W W (E0 − ) = W (E0) − ; (2) @E but W varies too rapidly with E to allow us to use this formula (Taylor expansion). Therefore work with ln W , instead of W , and hence write @ ln W (E0 − ) = ln W (E0) − ln W = ln W (E0) − : (3) @E k T =0 B Therefore the probability that a molecule has energy is proportional to exp (−/kBT ). Note the mean- ing of T = 0. At this temperature no molecule can be in an excited state, and therefore the whole gas must be in its state of minimum energy. 7. THE EQUATION OF STATE, AND THE RELATIONSHIP BETWEEN THE KELVIN TEM- PERATURE AND THE IDEAL GAS TEMPERATURE The relation between p, V and T is called the equation of state. Given the Boltzmann distribution we can calculate the equation of state for an ideal gas. We find pV = NAkBT , where NA is Avogadro’s number. Therefore the Kelvin temperature is the same as the ideal gas temperature if we take kB = R=NA, where −23 −1 R is the gas constant. kB is then called Boltzmann's constant (1:38 × 10 JK ). 8. WORK AND HEAT Energy can be added to a system in the form of either work or heat. For example, work is done on a gas if it is compressed in a cylinder fitted with a piston. Heat can be added to the system by thermal conduction through the walls of the containing vessel. The total increase in energy is the sum of the heat added and the work done. dE = dq + dw: (4) Note the convention of signs: energy added to a system is positive. q and w are not functions of state (you cannot associate a particular amount of heat with a particular state), and therefore dq and dw are not proper differentials (hence the bars over the ds). 9. REVERSIBLE PROCESSES If the piston compresses the gas slowly and if there is no friction, the process is said to be reversible, because a small change in conditions (force on the piston) can reverse the direction of the process. The work done can then be written dwrev = −pdV: (5) If the compression is not slow the gas swirls around and the pressure is not defined. If the gas expands into a vacuum through a valve (an extremely irreversible process), no work is done. Heat can also flow reversibly, if the temperature difference is very small.
Recommended publications
  • 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 .
    [Show full text]
  • Thermodynamics
    ME346A Introduction to Statistical Mechanics { Wei Cai { Stanford University { Win 2011 Handout 6. Thermodynamics January 26, 2011 Contents 1 Laws of thermodynamics 2 1.1 The zeroth law . .3 1.2 The first law . .4 1.3 The second law . .5 1.3.1 Efficiency of Carnot engine . .5 1.3.2 Alternative statements of the second law . .7 1.4 The third law . .8 2 Mathematics of thermodynamics 9 2.1 Equation of state . .9 2.2 Gibbs-Duhem relation . 11 2.2.1 Homogeneous function . 11 2.2.2 Virial theorem / Euler theorem . 12 2.3 Maxwell relations . 13 2.4 Legendre transform . 15 2.5 Thermodynamic potentials . 16 3 Worked examples 21 3.1 Thermodynamic potentials and Maxwell's relation . 21 3.2 Properties of ideal gas . 24 3.3 Gas expansion . 28 4 Irreversible processes 32 4.1 Entropy and irreversibility . 32 4.2 Variational statement of second law . 32 1 In the 1st lecture, we will discuss the concepts of thermodynamics, namely its 4 laws. The most important concepts are the second law and the notion of Entropy. (reading assignment: Reif x 3.10, 3.11) In the 2nd lecture, We will discuss the mathematics of thermodynamics, i.e. the machinery to make quantitative predictions. We will deal with partial derivatives and Legendre transforms. (reading assignment: Reif x 4.1-4.7, 5.1-5.12) 1 Laws of thermodynamics Thermodynamics is a branch of science connected with the nature of heat and its conver- sion to mechanical, electrical and chemical energy. (The Webster pocket dictionary defines, Thermodynamics: physics of heat.) Historically, it grew out of efforts to construct more efficient heat engines | devices for ex- tracting useful work from expanding hot gases (http://www.answers.com/thermodynamics).
    [Show full text]
  • Module P7.4 Specific Heat, Latent Heat and Entropy
    FLEXIBLE LEARNING APPROACH TO PHYSICS Module P7.4 Specific heat, latent heat and entropy 1 Opening items 4 PVT-surfaces and changes of phase 1.1 Module introduction 4.1 The critical point 1.2 Fast track questions 4.2 The triple point 1.3 Ready to study? 4.3 The Clausius–Clapeyron equation 2 Heating solids and liquids 5 Entropy and the second law of thermodynamics 2.1 Heat, work and internal energy 5.1 The second law of thermodynamics 2.2 Changes of temperature: specific heat 5.2 Entropy: a function of state 2.3 Changes of phase: latent heat 5.3 The principle of entropy increase 2.4 Measuring specific heats and latent heats 5.4 The irreversibility of nature 3 Heating gases 6 Closing items 3.1 Ideal gases 6.1 Module summary 3.2 Principal specific heats: monatomic ideal gases 6.2 Achievements 3.3 Principal specific heats: other gases 6.3 Exit test 3.4 Isothermal and adiabatic processes Exit module FLAP P7.4 Specific heat, latent heat and entropy COPYRIGHT © 1998 THE OPEN UNIVERSITY S570 V1.1 1 Opening items 1.1 Module introduction What happens when a substance is heated? Its temperature may rise; it may melt or evaporate; it may expand and do work1—1the net effect of the heating depends on the conditions under which the heating takes place. In this module we discuss the heating of solids, liquids and gases under a variety of conditions. We also look more generally at the problem of converting heat into useful work, and the related issue of the irreversibility of many natural processes.
    [Show full text]
  • Thermodynamic Potentials
    THERMODYNAMIC POTENTIALS, PHASE TRANSITION AND LOW TEMPERATURE PHYSICS Syllabus: Unit II - Thermodynamic potentials : Internal Energy; Enthalpy; Helmholtz free energy; Gibbs free energy and their significance; Maxwell's thermodynamic relations (using thermodynamic potentials) and their significance; TdS relations; Energy equations and Heat Capacity equations; Third law of thermodynamics (Nernst Heat theorem) Thermodynamics deals with the conversion of heat energy to other forms of energy or vice versa in general. A thermodynamic system is the quantity of matter under study which is in general macroscopic in nature. Examples: Gas, vapour, vapour in contact with liquid etc.. Thermodynamic stateor condition of a system is one which is described by the macroscopic physical quantities like pressure (P), volume (V), temperature (T) and entropy (S). The physical quantities like P, V, T and S are called thermodynamic variables. Any two of these variables are independent variables and the rest are dependent variables. A general relation between the thermodynamic variables is called equation of state. The relation between the variables that describe a thermodynamic system are given by first and second law of thermodynamics. According to first law of thermodynamics, when a substance absorbs an amount of heat dQ at constant pressure P, its internal energy increases by dU and the substance does work dW by increase in its volume by dV. Mathematically it is represented by 풅푸 = 풅푼 + 풅푾 = 풅푼 + 푷 풅푽….(1) If a substance absorbs an amount of heat dQ at a temperature T and if all changes that take place are perfectly reversible, then the change in entropy from the second 풅푸 law of thermodynamics is 풅푺 = or 풅푸 = 푻 풅푺….(2) 푻 From equations (1) and (2), 푻 풅푺 = 풅푼 + 푷 풅푽 This is the basic equation that connects the first and second laws of thermodynamics.
    [Show full text]
  • Equation of State - Wikipedia, the Free Encyclopedia 頁 1 / 8
    Equation of state - Wikipedia, the free encyclopedia 頁 1 / 8 Equation of state From Wikipedia, the free encyclopedia In physics and thermodynamics, an equation of state is a relation between state variables.[1] More specifically, an equation of state is a thermodynamic equation describing the state of matter under a given set of physical conditions. It is a constitutive equation which provides a mathematical relationship between two or more state functions associated with the matter, such as its temperature, pressure, volume, or internal energy. Equations of state are useful in describing the properties of fluids, mixtures of fluids, solids, and even the interior of stars. Thermodynamics Contents ■ 1 Overview ■ 2Historical ■ 2.1 Boyle's law (1662) ■ 2.2 Charles's law or Law of Charles and Gay-Lussac (1787) Branches ■ 2.3 Dalton's law of partial pressures (1801) ■ 2.4 The ideal gas law (1834) Classical · Statistical · Chemical ■ 2.5 Van der Waals equation of state (1873) Equilibrium / Non-equilibrium ■ 3 Major equations of state Thermofluids ■ 3.1 Classical ideal gas law Laws ■ 4 Cubic equations of state Zeroth · First · Second · Third ■ 4.1 Van der Waals equation of state ■ 4.2 Redlich–Kwong equation of state Systems ■ 4.3 Soave modification of Redlich-Kwong State: ■ 4.4 Peng–Robinson equation of state Equation of state ■ 4.5 Peng-Robinson-Stryjek-Vera equations of state Ideal gas · Real gas ■ 4.5.1 PRSV1 Phase of matter · Equilibrium ■ 4.5.2 PRSV2 Control volume · Instruments ■ 4.6 Elliott, Suresh, Donohue equation of state Processes:
    [Show full text]
  • Use of Equations of State and Equation of State Software Packages
    USE OF EQUATIONS OF STATE AND EQUATION OF STATE SOFTWARE PACKAGES Adam G. Hawley Darin L. George Southwest Research Institute 6220 Culebra Road San Antonio, TX 78238 Introduction Peng-Robinson (PR) Determination of fluid properties and phase The Peng-Robison (PR) EOS (Peng and Robinson, conditions of hydrocarbon mixtures is critical 1976) is referred to as a cubic equation of state, for accurate hydrocarbon measurement, because the basic equations can be rewritten as cubic representative sampling, and overall pipeline polynomials in specific volume. The Peng Robison operation. Fluid properties such as EOS is derived from the basic ideal gas law along with other corrections, to account for the behavior of compressibility and density are critical for flow a “real” gas. The Peng Robison EOS is very measurement and determination of the versatile and can be used to determine properties hydrocarbon due point is important to verify such as density, compressibility, and sound speed. that heavier hydrocarbons will not condense out The Peng Robison EOS can also be used to of a gas mixture in changing process conditions. determine phase boundaries and the phase conditions of hydrocarbon mixtures. In the oil and gas industry, equations of state (EOS) are typically used to determine the Soave-Redlich-Kwong (SRK) properties and the phase conditions of hydrocarbon mixtures. Equations of state are The Soave-Redlich-Kwaon (SRK) EOS (Soave, 1972) is a cubic equation of state, similar to the Peng mathematical correlations that relate properties Robison EOS. The main difference between the of hydrocarbons to pressure, temperature, and SRK and Peng Robison EOS is the different sets of fluid composition.
    [Show full text]
  • PHYS 521: Statistical Mechanics Homework #1
    PHYS 521: Statistical Mechanics Homework #1 Prakash Gautam April 17, 2018 1. A particular system obeys two equations of state 3As2 As3 T = (thermal equation of state);P = (mechanical equation of state): v v2 Where A is a constant. (a) Find µ as a function of s and v, and then find the fundamental equation. Solution: Given P and T the differential of each of them can be calculated as 6As 3As2 6As2 3As3 dT = ds − dv ) sdT = ds − dv v v2 v v2 3As2 2As3 3As2 2As3 dP = ds − dv ) vdP = ds − dv v2 v3 v v2 The Gibbs-Duhem relation in energy representation allows to calculate the value of µ. dµ = vdP − sdT 3As2 2As3 6As2 3As3 = ds − dv − ds + dv v[ v2 ] v ( v)2 3As2 As3 As3 = − ds − dv = −d v v2 v As3 This can be identified as the total derivative of v so the rel ( ) As3 As3 dµ = −d ) µ = − + k v v Where k is arbitrary constant. We can plug this back to Euler relation to find the fundamental equation as. u = T s − P v + µ 3As3 As3 As3 As3 = − − + k = + k v v v v As3 □ So the fundamental equation of the system is v + k. (b) Find the fundamental equation of this system by direct integration of the molar form of the equation. Solution: The differential form of internal energy is du = T ds − P dv 3As2 As3 = ds − dv v v2 1 As3 As before this is just the total differential of v so the relation leads to ( ) As3 As3 du = d ) u = + k v2 v This k should be the same arbitrary constant that we got in the previous problem.
    [Show full text]
  • Thermal and Statistical Physics (Part II) Examples Sheet 1 ————————————————————————————
    Michaelmas 2010 Thermal and Statistical Physics (Part II) Examples Sheet 1 ————————————————————————————- 1. Show that, for a van der Waals gas, the specific heat at constant volume, CV , obeys ∂C V = 0. ∂V T 2. The Gibbs free energy of an imperfect gas containing N molecules is given, in terms of its natural variables T , p and N, by p G = NkBT ln − NA(T ) p, p0 where p0 is a constant and A is a function of T only. Derive expressions in terms of T , p, V , and N for: (a) the equation of state of the gas; (b) the entropy, S; (c) the enthalpy, H; (d) the internal energy, U; (e) the Helmholtz free energy, F . Can all equilibrium thermodynamic information about the gas be obtained from a knowledge of: (i) F (T, V, N); (ii) the equation of state and U(T, p, N)? 3. The entropy of a monatomic ideal gas is given by the Sackur-Tetrode equation which can be written in the form: 3 2 V U / S(U, V, N)= Nk ln α , B N N ( ) where α is a constant to be derived later in the course. Invert this expression to get U(S, V, N). From this, obtain the equation of state expressing p as a function of V, N and T . 4. Use a Maxwell relation and the chain rule to show that for any substance the rate of change of T with p in a reversible adiabatic compression is given by ∂T T ∂V = . ∂p C ∂T S p p Find an equivalent expression for the adiabatic rate of change of T with V , and check that both results are valid for an ideal monatomic gas.
    [Show full text]
  • Thermodynamically Consistent Modeling and Simulation of Multi-Component Two-Phase Flow Model with Partial Miscibility
    THERMODYNAMICALLY CONSISTENT MODELING AND SIMULATION OF MULTI-COMPONENT TWO-PHASE FLOW MODEL WITH PARTIAL MISCIBILITY∗ JISHENG KOU† AND SHUYU SUN‡ Abstract. A general diffuse interface model with a realistic equation of state (e.g. Peng- Robinson equation of state) is proposed to describe the multi-component two-phase fluid flow based on the principles of the NVT-based framework which is a latest alternative over the NPT-based framework to model the realistic fluids. The proposed model uses the Helmholtz free energy rather than Gibbs free energy in the NPT-based framework. Different from the classical routines, we combine the first law of thermodynamics and related thermodynamical relations to derive the entropy balance equation, and then we derive a transport equation of the Helmholtz free energy density. Furthermore, by using the second law of thermodynamics, we derive a set of unified equations for both interfaces and bulk phases that can describe the partial miscibility of two fluids. A relation between the pressure gradient and chemical potential gradients is established, and this relation leads to a new formulation of the momentum balance equation, which demonstrates that chemical potential gradients become the primary driving force of fluid motion. Moreover, we prove that the proposed model satisfies the total (free) energy dissipation with time. For numerical simulation of the proposed model, the key difficulties result from the strong nonlinearity of Helmholtz free energy density and tight coupling relations between molar densities and velocity. To resolve these problems, we propose a novel convex-concave splitting of Helmholtz free energy density and deal well with the coupling relations between molar densities and velocity through very careful physical observations with a mathematical rigor.
    [Show full text]
  • Maxwell Relations
    MAXWELLRELATIONS 7.I THE MAXWELL RELATIONS In Section 3.6 we observedthat quantities such as the isothermal compressibility, the coefficientof thermal expansion,and the molar heat capacities describe properties of physical interest. Each of these is essentiallya derivativeQx/0Y)r.r..,. in which the variablesare either extensiveor intensive thermodynaini'cparameters. with a wide range of extensive and intensive parametersfrom which to choose, in general systems,the numberof suchpossible derivatives is immense.But thire are azu azu ASAV AVAS (7.1) -tI aP\ | AT\ as),.*,.*,,...: \av)s.N,.&, (7.2) This relation is the prototype of a whole class of similar equalities known as the Maxwell relations. These relations arise from the equality of the mixed partial derivatives of the fundamental relation expressed in any of the various possible alternative representations. 181 182 Maxwell Relations Given a particular thermodynamicpotential, expressedin terms of its (l + 1) natural variables,there are t(t + I)/2 separatepairs of mixed second derivatives.Thus each potential yields t(t + l)/2 Maxwell rela- tions. For a single-componentsimple systemthe internal energyis a function : of three variables(t 2), and the three [: (2 . 3)/2] -arUTaSpurs of mixed second derivatives are A2U/ASAV : AzU/AV AS, AN : A2U / AN AS, and 02(J / AVA N : A2U / AN 0V. Thecompleteser of Maxwell relations for a single-componentsimple systemis given in the following listing, in which the first column states the potential from which the ar\ U S,V I -|r| aP\ \ M)',*: ,s/,,' (7.3) dU: TdS- PdV + p"dN ,S,N (!t\ (4\ (7.4) \ dNls.r, \ ds/r,r,o V,N _/ii\ (!L\ (7.5) \0Nls.v \0vls.x UITI: F T,V ('*),,.: (!t\ (7.6) \0Tlv.p dF: -SdT - PdV + p,dN T,N -\/ as\ a*) ,.,: (!"*),.
    [Show full text]
  • Thermodynamics.Pdf
    1 Statistical Thermodynamics Professor Dmitry Garanin Thermodynamics February 24, 2021 I. PREFACE The course of Statistical Thermodynamics consist of two parts: Thermodynamics and Statistical Physics. These both branches of physics deal with systems of a large number of particles (atoms, molecules, etc.) at equilibrium. 3 19 One cm of an ideal gas under normal conditions contains NL = 2:69×10 atoms, the so-called Loschmidt number. Although one may describe the motion of the atoms with the help of Newton's equations, direct solution of such a large number of differential equations is impossible. On the other hand, one does not need the too detailed information about the motion of the individual particles, the microscopic behavior of the system. One is rather interested in the macroscopic quantities, such as the pressure P . Pressure in gases is due to the bombardment of the walls of the container by the flying atoms of the contained gas. It does not exist if there are only a few gas molecules. Macroscopic quantities such as pressure arise only in systems of a large number of particles. Both thermodynamics and statistical physics study macroscopic quantities and relations between them. Some macroscopics quantities, such as temperature and entropy, are non-mechanical. Equilibruim, or thermodynamic equilibrium, is the state of the system that is achieved after some time after time-dependent forces acting on the system have been switched off. One can say that the system approaches the equilibrium, if undisturbed. Again, thermodynamic equilibrium arises solely in macroscopic systems. There is no thermodynamic equilibrium in a system of a few particles that are moving according to the Newton's law.
    [Show full text]
  • Equation of State of Ideal Gases
    Equation of state of ideal gases Objective For a constant amount of gas (air) investigate the correlation of 1. Volume and pressure at constant temperature (Boyles law) 2. Volume and temperature at constant pressure (Gay-Lussac's law) 3. Pressure and temperature at constant volume Charles's law Introduction The gas laws are thermodynamic relationships that express the behavior of a quantity of gas in terms of the pressure P , volume V , and temperature T . The kinetic energy of gases expresses the behavior of a "perfect" or ideal gas to be PV = nRT , which is commonly referred to as the ideal gas law. However, the general relationships among P , V and T contained in this equation had been expressed earlier in the classical gas laws for real gases. These gas laws were Based on the empirical observations of early investigators, in particular the English scientist Robert Boyle and the French scientists Jacques Charles and Joseph Gay-Lussac. Theory I Boyle's law: Around 1660, Robert Boyle had established an empirical relationship between the pressure and the volume of a gas, which is known as Boyle's law: At constant temperature, the volume occupied by a given mass of gas is inversely proportional to its pressure. In mathematical notation, we write 1 V / ; (1) P In equation form, we may write k ¢V = : (2) P Where k is the constant of proportionality for a given temperature. The pressure of a con¯ned gas is commonly measured by means of a manometer. The gas pressure for such an open-tube manometer is the sum of the atmospheric pressure Pa and the pressure of the height di®erence of mercury P = Pa + ½m £ g £ hm: (3) 1 but Pa = 76 cm Hg = ½m £ g £ 76 then equation (3) becomes: P = ½m £ g £ (hm + 76): (4) 3 2 where ½m = 13:6 gm=cm and g = 980cm=s The volume of the enclosed gas is the volume of the measuring tube segment marked in brown added to the volume calculated from the length of the column of air: V = Vl + 1:01 ml (5) or V = ¼r2l + 1:01 ml µ ¶ 1:14 2 = ¼ l + 1:01 ml 2 = 1:02l + 1:01 »= l + 1 = l0 (6) Substituting with P and V in eq.
    [Show full text]