On the Two Main Laws of Thermodynamics
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Math Background for Thermodynamics ∑
MATH BACKGROUND FOR THERMODYNAMICS A. Partial Derivatives and Total Differentials Partial Derivatives Given a function f(x1,x2,...,xm) of m independent variables, the partial derivative ∂ f of f with respect to x , holding the other m-1 independent variables constant, , is defined by i ∂ xi xj≠i ∂ f fx( , x ,..., x+ ∆ x ,..., x )− fx ( , x ,..., x ,..., x ) = 12ii m 12 i m ∂ lim ∆ xi x →∆ 0 xi xj≠i i nRT Example: If p(n,V,T) = , V ∂ p RT ∂ p nRT ∂ p nR = = − = ∂ n V ∂V 2 ∂T V VT,, nTV nV , Total Differentials Given a function f(x1,x2,...,xm) of m independent variables, the total differential of f, df, is defined by m ∂ f df = ∑ dx ∂ i i=1 xi xji≠ ∂ f ∂ f ∂ f = dx + dx + ... + dx , ∂ 1 ∂ 2 ∂ m x1 x2 xm xx2131,...,mm xxx , ,..., xx ,..., m-1 where dxi is an infinitesimally small but arbitrary change in the variable xi. nRT Example: For p(n,V,T) = , V ∂ p ∂ p ∂ p dp = dn + dV + dT ∂ n ∂ V ∂ T VT,,, nT nV RT nRT nR = dn − dV + dT V V 2 V B. Some Useful Properties of Partial Derivatives 1. The order of differentiation in mixed second derivatives is immaterial; e.g., for a function f(x,y), ∂ ∂ f ∂ ∂ f ∂ 22f ∂ f = or = ∂ y ∂ xx ∂ ∂ y ∂∂yx ∂∂xy y x x y 2 in the commonly used short-hand notation. (This relation can be shown to follow from the definition of partial derivatives.) 2. Given a function f(x,y): ∂ y 1 a. = etc. ∂ f ∂ f x ∂ y x ∂ f ∂ y ∂ x b. -
6CCP3212 Statistical Mechanics Homework 1
6CCP3212 Statistical Mechanics Homework 1 Lecturer: Dr. Eugene A. Lim 2018-19 Year 3 Semester 1 https://nms.kcl.ac.uk/eugene.lim/teach/statmech/sm.html 1) (i) For the following differentials with α and β non-zero real constants, which are exact and which are inexact? Integrate the equation if it is exact. (a) x dG = αdx + β dy (1) y (b) α dG = dx + βdy (2) x (c) x2 dG = (x + y)dx + dy (3) 2 (ii) Show that the work done on the system at pressure P d¯W = −P dV (4) where dV is the change in volume is an inexact differential by showing that there exists no possible function of state for W (P; V ). (iii) Consider the differential dF = (x2 − y)dx + xdy : (5) (a) Show that this is not an exact differential. And hence integrate this equation in two different straight paths from (1; 1) ! (2; 2) and from (1; 1) ! (1; 2) ! (2; 2), where (x; y) indicates the locations. Compare the results { are they identical? (b) Define a new differential with dF y 1 dG ≡ = 1 − dx + dy : (6) x2 x2 x Show that dG is exact, and find G(x; y). 2) This problem asks you to derive some derivative identities of a system with three variables x, y and z, with a single constraint x(y; z). This kind of system is central to thermodynamics as we often use three state variables P , V and T , with an equation of state P (V; T ) (i.e. the constraint) to describe a system. -
3 More Applications of Derivatives
3 More applications of derivatives 3.1 Exact & inexact di®erentials in thermodynamics So far we have been discussing total or \exact" di®erentials µ ¶ µ ¶ @u @u du = dx + dy; (1) @x y @y x but we could imagine a more general situation du = M(x; y)dx + N(x; y)dy: (2) ¡ ¢ ³ ´ If the di®erential is exact, M = @u and N = @u . By the identity of mixed @x y @y x partial derivatives, we have µ ¶ µ ¶ µ ¶ @M @2u @N = = (3) @y x @x@y @x y Ex: Ideal gas pV = RT (for 1 mole), take V = V (T; p), so µ ¶ µ ¶ @V @V R RT dV = dT + dp = dT ¡ 2 dp (4) @T p @p T p p Now the work done in changing the volume of a gas is RT dW = pdV = RdT ¡ dp: (5) p Let's calculate the total change in volume and work done in changing the system between two points A and C in p; T space, along paths AC or ABC. 1. Path AC: dT T ¡ T ¢T ¢T = 2 1 ´ so dT = dp (6) dp p2 ¡ p1 ¢p ¢p T ¡ T1 ¢T ¢T & = ) T ¡ T1 = (p ¡ p1) (7) p ¡ p1 ¢p ¢p so (8) R ¢T R ¢T R ¢T dV = dp ¡ [T + (p ¡ p )]dp = ¡ (T ¡ p )dp (9) p ¢p p2 1 ¢p 1 p2 1 ¢p 1 R ¢T dW = ¡ (T ¡ p )dp (10) p 1 ¢p 1 1 T (p ,T ) 2 2 C (p,T) (p1,T1) A B p Figure 1: Path in p; T plane for thermodynamic process. -
Thermodynamics and Phase Diagrams
Thermodynamics and Phase Diagrams Arthur D. Pelton Centre de Recherche en Calcul Thermodynamique (CRCT) École Polytechnique de Montréal C.P. 6079, succursale Centre-ville Montréal QC Canada H3C 3A7 Tél : 1-514-340-4711 (ext. 4531) Fax : 1-514-340-5840 E-mail : [email protected] (revised Aug. 10, 2011) 2 1 Introduction An understanding of phase diagrams is fundamental and essential to the study of materials science, and an understanding of thermodynamics is fundamental to an understanding of phase diagrams. A knowledge of the equilibrium state of a system under a given set of conditions is the starting point in the description of many phenomena and processes. A phase diagram is a graphical representation of the values of the thermodynamic variables when equilibrium is established among the phases of a system. Materials scientists are most familiar with phase diagrams which involve temperature, T, and composition as variables. Examples are T-composition phase diagrams for binary systems such as Fig. 1 for the Fe-Mo system, isothermal phase diagram sections of ternary systems such as Fig. 2 for the Zn-Mg-Al system, and isoplethal (constant composition) sections of ternary and higher-order systems such as Fig. 3a and Fig. 4. However, many useful phase diagrams can be drawn which involve variables other than T and composition. The diagram in Fig. 5 shows the phases present at equilibrium o in the Fe-Ni-O2 system at 1200 C as the equilibrium oxygen partial pressure (i.e. chemical potential) is varied. The x-axis of this diagram is the overall molar metal ratio in the system. -
Physical Chemistry II “The Mistress of the World and Her Shadow” Chemistry 402
Physical Chemistry II “The mistress of the world and her shadow” Chemistry 402 L. G. Sobotka Department of Chemistry Washington University, St Louis, MO, 63130 January 3, 2012 Contents IIntroduction 7 1 Physical Chemistry II - 402 -Thermodynamics (mostly) 8 1.1Who,when,where.............................................. 8 1.2CourseContent/Logistics.......................................... 8 1.3Grading.................................................... 8 1.3.1 Exams................................................. 8 1.3.2 Quizzes................................................ 8 1.3.3 ProblemSets............................................. 8 1.3.4 Grading................................................ 8 2Constants 9 3 The Structure of Physical Science 10 3.1ClassicalMechanics.............................................. 10 3.2QuantumMechanics............................................. 11 3.3StatisticalMechanics............................................. 11 3.4Thermodynamics............................................... 12 3.5Kinetics.................................................... 13 4RequisiteMath 15 4.1 Exact differentials.............................................. 15 4.2Euler’sReciprocityrelation......................................... 15 4.2.1 Example................................................ 16 4.3Euler’sCyclicrelation............................................ 16 4.3.1 Example................................................ 16 4.4Integratingfactors.............................................. 17 4.5LegendreTransformations......................................... -
Exact and Inexact Differentials in the Early Development of Mechanics
Revista Brasileira de Ensino de Física, vol. 42, e20190192 (2020) Articles www.scielo.br/rbef cb DOI: http://dx.doi.org/10.1590/1806-9126-RBEF-2019-0192 Licença Creative Commons Exact and inexact differentials in the early development of mechanics and thermodynamics Mário J. de Oliveira*1 1Universidade de São Paulo, Instituto de Física, São Paulo, SP, Brasil Received on July 31, 2019. Revised on October 8, 2019. Accepted on October 13, 2019. We give an account and a critical analysis of the use of exact and inexact differentials in the early development of mechanics and thermodynamics, and the emergence of differential calculus and how it was applied to solve some mechanical problems, such as those related to the cycloidal pendulum. The Lagrange equations of motions are presented in the form they were originally obtained in terms of differentials from the principle of virtual work. The derivation of the conservation of energy in differential form as obtained originally by Clausius from the equivalence of heat and work is also examined. Keywords: differential, differential calculus, analytical mechanics, thermodynamics. 1. Introduction variable x. If another variable y depends on the indepen- dent variable x, then the resulting increment dy of y is It is usual to formulate the basic equations of thermo- its differential. The quotient of these two differentials, dynamics in terms of differentials. The conservation of dy/dx, was interpreted geometrically by Leibniz as the energy is written as ratio of the ordinate y of a point on a curve and the length of the subtangent associated to this point. -
The First Law: the Machinery the Power of Thermodynamics – How to Establish Relations Between Different Properties of a System
The First Law: the machinery The power of thermodynamics – how to establish relations between different properties of a system. The procedure is based on the experimental fact that the internal energy and the enthalpy are state functions. We shall see that a property can be measured indirectly by measuring others and then combining their values. We shall also discuss the liquefaction of gases and establish the relation between Cp and CV. State functions and exact differentials State and path functions The initial state of the system is i and in this state the internal energy is Ui. Work is done by the system as it expands adiabatically to a state f (an internal energy Uf). The work done on the system as it changes along Path 1 from i to f is w. U – a property of the state; w – a property of the path. Consider another process, Path 2: the initial and final states are the same, but the expansion is not adiabatic. Because U is a state function, the internal energy of both the initial and the final states are the same as before, but an energy q’ enters the system as heat and the work w’ is not the same as w. The work and the heat are path functions. Exact and inexact differentials If a system is taken along a path, U changes from Ui to Uf and the overall change is the sum (integral) of all infinitesimal changes along the path: f ΔU = dU ∫i ΔU depends on the initial and final states but is independent of the path between them. -
Comparative Examination of Nonequilibrium Thermodynamic Models of Thermodiffusion in Liquids †
Proceedings Comparative Examination of Nonequilibrium Thermodynamic Models of Thermodiffusion in Liquids † Semen N. Semenov 1,* and Martin E. Schimpf 2 1 Institute of Biochemical Physics RAS, Moscow 119334, Russia 2 Department of Chemistry, Boise State University, Boise, ID 83725, USA; [email protected] * Correspondence: [email protected] † Presented at the 5th International Electronic Conference on Entropy and Its Applications, 18–30 November 2019; Available online: https://ecea-5.sciforum.net/. Published: 17 November 2019 Abstract: We analyze existing models for material transport in non-isothermal non-electrolyte liquid mixtures that utilize non-equilibrium thermodynamics. Many different sets of equations for material have been derived that, while based on the same fundamental expression of entropy production, utilize different terms of the temperature- and concentration-induced gradients in the chemical potential to express the material flux. We reason that only by establishing a system of transport equations that satisfies the following three requirements can we obtain a valid thermodynamic model of thermodiffusion based on entropy production, and understand the underlying physical mechanism: (1) Maintenance of mechanical equilibrium in a closed steady-state system, expressed by a form of the Gibbs–Duhem equation that accounts for all the relevant gradients in concentration, temperature, and pressure and respective thermodynamic forces; (2) thermodiffusion (thermophoresis) is zero in pure unbounded liquids (i.e., in the absence of wall effects); (3) invariance in the derived concentrations of components in a mixture, regardless of which concentration or material flux is considered to be the dependent versus independent variable in an overdetermined system of material transport equations. The analysis shows that thermodiffusion in liquids is based on the entropic mechanism. -
Thermodynamic Temperature
Thermodynamic temperature Thermodynamic temperature is the absolute measure 1 Overview of temperature and is one of the principal parameters of thermodynamics. Temperature is a measure of the random submicroscopic Thermodynamic temperature is defined by the third law motions and vibrations of the particle constituents of of thermodynamics in which the theoretically lowest tem- matter. These motions comprise the internal energy of perature is the null or zero point. At this point, absolute a substance. More specifically, the thermodynamic tem- zero, the particle constituents of matter have minimal perature of any bulk quantity of matter is the measure motion and can become no colder.[1][2] In the quantum- of the average kinetic energy per classical (i.e., non- mechanical description, matter at absolute zero is in its quantum) degree of freedom of its constituent particles. ground state, which is its state of lowest energy. Thermo- “Translational motions” are almost always in the classical dynamic temperature is often also called absolute tem- regime. Translational motions are ordinary, whole-body perature, for two reasons: one, proposed by Kelvin, that movements in three-dimensional space in which particles it does not depend on the properties of a particular mate- move about and exchange energy in collisions. Figure 1 rial; two that it refers to an absolute zero according to the below shows translational motion in gases; Figure 4 be- properties of the ideal gas. low shows translational motion in solids. Thermodynamic temperature’s null point, absolute zero, is the temperature The International System of Units specifies a particular at which the particle constituents of matter are as close as scale for thermodynamic temperature. -
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: -
Seoul National University Prof. Sang-Im, Yoo 2.7 Standard Enthalpy Changes the Enthalpy Change for a Process in the Standard States
Lecture Contents 2.2. TheThe FirstFirst LawLaw Thermochemistry 2.7 Standard enthalpy changes 2.8 Standard enthalpies of formation 2.9 The temperature-dependence of reaction enthalpies State functions and exact differentials 2.10 Exact and inexact differentials 2.11 Changes in internal energy 2.12 The Joule-Thomson effect Seoul National University Prof. Sang-im, Yoo 2.7 Standard enthalpy changes The enthalpy change for a process in the standard states ► The standard state of a substance: Its pure form at a specific temperature and 1 bar ex) The standard state of ethanol at 298 K : a pure liquid ethanol at 298 K and 1 bar The standard state of iron at 500 K : a pure solid iron at 500 K and 1 bar ► Standard enthalpy change for a reaction: The difference between the products in their standard states and the reactants in their standard states at the same specified temperature o ex) The standard enthalpy of vaporization, ΔH vap The enthalpy change per mole when a pure liquid at 1 bar vaporizes to gas at 1 bar o H2O(l) → H2O(g) ΔH vap(373 K) = +40.66 kJ/mol - Conventional temperature for reporting thermodynamic data? 298.15K (25.00oC) Contents (a) Enthalpies of physical change (b) Enthalpies of chemical change (c) Hess’s law Seoul National University Prof. Sang-im, Yoo 2.7 Standard enthalpy changes (a) Enthalpies of physical change o - Standard enthalpy of transition, ΔH trs: the standard enthalpy change that accompanies change of physical state (see Table 2.3) o ex) Standard enthalpy of vaporization, ΔH vap o Standard enthalpy of fusion, ΔH fus o H2O(l) → H2O(s) ΔH fus(273 K) = +6.01 kJ/mol - Enthalpy is a state function (Independent of the path between the two states) (i) Directly from solid to vapor: sublimation o H2O(s) → H2O(g) ΔH sub (ii) In two steps : fusion + vaporization o H2O(s) → H2O(l) ΔH fus o H2O(l) → H2O(g) ΔH vap o o o H2O(s) → H2O(g) ΔH sub = ΔH fus + ΔH vap - The standard enthalpy changes of a forward process and its reverse differ only in sign ΔHo(A → B) = − ΔHo(B → A) Seoul National University Prof. -
Definition of the Ideal Gas
ON THE DEFINITION OF THE IDEAL GAS. By Edgar Bucidngham. I . Nature and purpose of the definition.—The notion of the ideal gas is that of a gas having particularly simple physical properties to which the properties of the real gases may be considered as approximations; or of a standard to which the real gases may be referred, the properties of the ideal gas being simply defined and the properties of the real gases being then expressible as the prop- erties of the standard plus certain corrections which pertain to the individual gases. The smaller these corrections the more nearly the real gas approaches to being in the "ideal state." This con- ception grew naturally from the fact that the earlier experiments on gases showed that they did not differ much in their physical properties, so that it was possible to define an ideal standard in such a way that the corrections above referred to should in fact all be ''small" in terms of the unavoidable errors of experiment. Such a conception would hardly arise to-day, or if it did, would not be so simple as that which has come down to us from earlier times when the art of experimenting upon gases was less advanced. It is evident that a quantitative definition of the ideal standard gas needs to be more or less complete and precise according to the nature of the problem under immediate consideration. If changes of temperature and of internal energy play no part, all that is usually needed is a standard relation between pressure and volume.