Thermodynamic Quantities G H-TS

Total Page:16

File Type:pdf, Size:1020Kb

Thermodynamic Quantities G H-TS So ItS Some randomness of distribution. entropP GIBBS AND HELMHOLTZ FUNCTIONS function as Gibbs function (G) and Helmholtz (A) thermodynamic quantities it is the Gibbs function G is otherwise called Gibbs free energy and called Helmholtz net work function. Helmholtz Function A is otherwise function free energy and it is the maximum work The Gibbs free energy G - Net work function Definition G H-TS Gibbs ree energy (also called enelgy funetion) G is detined. thetmodynamie a n which e. 1G property, decrease gives thee e wotk that can be obtained frem a system during a change G W PAV Relationship between Gibd's tree energy change and enthalpy chans. From detinition Since HT and S are state properties, G Is also a state property For change at constant temperature change in Gis given as Fora dG dH -T dS dG IS an exact differential Gibbs free energy is useful to study ch. at constant pressure and temperature For a ftinite change 1G= H TAS Relation between helmholtz free energy and Gibbs tree energy we knew H=NE PAV 1G E PAV-T 1S But E TIS = 4 So AG= 14 PIV work To show that the in decrease Gibb's tree energy gives the net work other than be work work of expansion done by a system) ree We knew IG JA PAV stud But A-W NG-W PAV Difs or-AG W-P1G= W The Helmholtz free energy A Maximum work function Definition : A=E- TS Helmoholtz tree also caled work A energy function) s defined as a a decrease in which i thermodynamie property, e,A gives he maximum work that can be otained trom a system duning a qive change A 91 Toshow AA W. From definition A E TS Since E T and S are state properties A is also a state property he change in A for a change in the system at constant temperature is given below dA dE TdS Since A is a state property, dA Is an exact different:al For a finite change A E- TAS Where A Is the change in the function A E Is the correspondi ng change in internal energy and 1S Is the change in the entropy of the system For a reversible change at constant T the heat absorped is From definition Q,T=AS Substituting this in the above equation we get AA E Q But from First law of thermodynamics E = W W E e A =-W rev A W done is the max1mum We know in a reversible process the werk -JA work thust can work So, the decrease in A, e, gives the maximum So the Heimholts be obtained from a system during a given change A, useful to work function Heimhoitz free energy is free energy is called a and volume study change at constant temperature and Gibb's free Differences between Helmholtz free energy energy Helmholtz Free ener9y Gibb's Free energy A E- TS Definition that ceig be Maximum work Usefu wers Indicatess content of a system octaned (Networ alue A W 92 Two show how TAS determines the randomness of a reactinn We know AG= AH - TAS action or TAS AH AG =Enthalpy useful work (Heat absorbed) unavailable enerqy Thus TaS is a measure of which unavailable energy, i.e., the ene. could not be converted into work energ, If TAS > AH; then AG negative Such a process will be All lead spontaneous. spontaneous to an increase in the processe disorderliness or randomness of the So if TAS is > AH system randomness will increase. if < randomness will decrease. Similarly TAS AH then Thus TAS determines the randomness of a reaction. TAS us an idea of the also gives unavailable energy. AA AND aG AS EQUILIBRIUM AND SPONTANEITYCRITERIA FOR THERMODYNAMIC General condition for equilibrium and spontaneity / condition for a reversible and Criteria Helmholts free spontaneous process in terms of energy (or) Condition for under Constant Equilibrium and spontaneity termperature and constant volume Consider the general conditions for equilibrium and spontaneity - dE-Pon dV - du + T dS 20 At Constant volume PopdV = 0 du - o-(dE - du dV TdS) >0 At constant = temperature dA dE - T dS So - dA - du 2 0 No work other than work of expansion takes in reactions and place the chemical ordinary physical changes. For these changes du=0 and o-dA 20 dA 0 Condition for equilibrium dA 0 Condition for spontaneity dA < 0 93 Criteria/ condition for a reversible and spontaneous procesS In terms of Gibb's free energy (or) Condition for equilibrium and Spontaneity under constant Temperature and Pressure. Consider the general condition for equlibrium and spontaneity dE-Pan dV - du + T dS >0 At constant pressure P Pop Therefore -dE- PdV du + Tds 20 (dE PdV) - du+ TdS20;-dH- du+ TdS 20 - At constant temperature dH - TdS = dG; -dG du>20 reactions takes in chemical No work other than work of expansion place For these changes and ordinary physical changes, dG20: dGS0 T dG0 Condition for equilibrium at constant and P and P dG <0 Condition for spontaneity at constant.T constant temperature carried out at chemical reactions are Many free energy of the system reactions the Gibbs In these will not and pressure. the free energy attains equilibrium, a reaction decreases. When decrease. Conclusion tell whether a change law is unable to earlier that first have seen not. That was why We spontaneously or reaction can take place law is able to state or a how the second of let us see second law. Now needed a a reaction. we spontaneity of or the predict the feasibility accordit is reaction own or on its Feasibility ofa spontaneously take place /f a reaction can reaction said to be feasible of a the feasibility method in predict feasible gives a will be Second law AS> 0 the reaction AG <0 or if to second law, if We know According spontaneous. reactions are exothermic Normaliy G IH TAS n Pvoetle feattions H is So hegative 1 will be in te invided 1S ie poeitive So nermally exothermic reactins, 1 hanentis bwe fat an bvothetmic et reactions are spontana. i h owee exetherimic teaction where AH IS anenus ale le negativa hegative is will be negative Ih such a case - 1S) 1G-H TAs Now ill be negative only if- H> T1S peelle iT1S>- H then iG i thie imeane that the reaction e cannot take place Thus ws ha ales sene cattot determine the feasibiity of a reaction ah ehdothetimie teartion is positive 11S beeohmee hedative 1S is negative than e - H-1 1S ositive hegativel= positivePositive Positive hat enine stuch a teaction cannot take place t atn ehdothettmie procese to S eitive take place nust be highly so that-1S is greater than Hwhich is positive ie- 1S >H hett il wil ecome hegativve tth tottee fot We maturat changes khow tree that the enetdv of a system decreases during ptaheois A natura lhange definite change in Iree ih the energy for a ahge system at constant natural eietelhh temperature is given by the following 13 - T1S When C ie hegative the change is eld t spontaneous or natural The depends AH and 1S If H is e megative and 1S hegative is elated to the is positive 1G take ener gv ef the system For natural t rlare the etnetdy of the changes systetm should decrease hisutd netease is and his observed in entropy excthermic If teee in a reactions rettain eharge then the enthalpy itst entropy should inctease to ramp eneate the increase in larger enthalpy This is etdti te tom observed in artime thesp We can conchide ie t th at the drivina haas ap fhp fart eaee entlalp a/1d inre ase in 95 CHANGE ENTROPY ADVANTÁGES OVER is AND equilibrium (AA AG) towards THEIR physico-chemical systerm movement of the energy The the other entropy and one involving towao by two factors, ontrolled processes proceed we know, spontaneous of entropy the system. the value f At equilibrium, with increase of entropy process equilibrium of a spontaneous the other hand the passage of the maximum. On of energy, a decrease s accompanied by equilibrium is is minimurm the system towards the energy of Hence at equilibrium. may or sportaneity system. thermochemical equilibrium for a Thus the criteria follows be given as (SVT20 (i) (OE) v1 () conditions of studied under are rarely at chemical reactions carried out Dut reactions are Usually or constant energy. temperature entropy constant constant and at (atmospheric pressure) volume (in constant pressure out at constant are carried Sometimes they necessary thermostat). it becomes (in a temperature. So and at constant or AG. bomb calorimeter) in terms of AA or spontaneity the criteria for equilibrium to specify as follows: They are given (AT0:(G)p0 more that are over AS is they of AA and AG Thus the advantage concrete problems. some the of practicaly, in study convenient will be whether the process will indicate of AG or AA Thus The sign is spontaneous. 2 the reaction is negative or not, If it spontaneous with respect to AS can not say the we in deciding more important and AS. AS is Between AG reaction: than AS is spontaneity advantageous AS, ofa is more seen that AG is we have as AG itself Though a reaction spontanity of in deciding the more important dependant on 1S AG AH- TJS and AH negative and If,AS is positive on AH 1S. so see G, depends sufficiently large We is negative and But if 1S not will be negative.
Recommended publications
  • Thermodynamic Potentials and Natural Variables
    Revista Brasileira de Ensino de Física, vol. 42, e20190127 (2020) Articles www.scielo.br/rbef cb DOI: http://dx.doi.org/10.1590/1806-9126-RBEF-2019-0127 Licença Creative Commons Thermodynamic Potentials and Natural Variables M. Amaku1,2, F. A. B. Coutinho*1, L. N. Oliveira3 1Universidade de São Paulo, Faculdade de Medicina, São Paulo, SP, Brasil 2Universidade de São Paulo, Faculdade de Medicina Veterinária e Zootecnia, São Paulo, SP, Brasil 3Universidade de São Paulo, Instituto de Física de São Carlos, São Carlos, SP, Brasil Received on May 30, 2019. Revised on September 13, 2018. Accepted on October 4, 2019. Most books on Thermodynamics explain what thermodynamic potentials are and how conveniently they describe the properties of physical systems. Certain books add that, to be useful, the thermodynamic potentials must be expressed in their “natural variables”. Here we show that, given a set of physical variables, an appropriate thermodynamic potential can always be defined, which contains all the thermodynamic information about the system. We adopt various perspectives to discuss this point, which to the best of our knowledge has not been clearly presented in the literature. Keywords: Thermodynamic Potentials, natural variables, Legendre transforms. 1. Introduction same statement cannot be applied to the temperature. In real fluids, even in simple ones, the proportionality Basic concepts are most easily understood when we dis- to T is washed out, and the Internal Energy is more cuss simple systems. Consider an ideal gas in a cylinder. conveniently expressed as a function of the entropy and The cylinder is closed, its walls are conducting, and a volume: U = U(S, V ).
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [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]
  • Vector Calculus and Differential Forms with Applications To
    Vector Calculus and Differential Forms with Applications to Electromagnetism Sean Roberson May 7, 2015 PREFACE This paper is written as a final project for a course in vector analysis, taught at Texas A&M University - San Antonio in the spring of 2015 as an independent study course. Students in mathematics, physics, engineering, and the sciences usually go through a sequence of three calculus courses before go- ing on to differential equations, real analysis, and linear algebra. In the third course, traditionally reserved for multivariable calculus, stu- dents usually learn how to differentiate functions of several variable and integrate over general domains in space. Very rarely, as was my case, will professors have time to cover the important integral theo- rems using vector functions: Green’s Theorem, Stokes’ Theorem, etc. In some universities, such as UCSD and Cornell, honors students are able to take an accelerated calculus sequence using the text Vector Cal- culus, Linear Algebra, and Differential Forms by John Hamal Hubbard and Barbara Burke Hubbard. Here, students learn multivariable cal- culus using linear algebra and real analysis, and then they generalize familiar integral theorems using the language of differential forms. This paper was written over the course of one semester, where the majority of the book was covered. Some details, such as orientation of manifolds, topology, and the foundation of the integral were skipped to save length. The paper should still be readable by a student with at least three semesters of calculus, one course in linear algebra, and one course in real analysis - all at the undergraduate level.
    [Show full text]
  • Notes on the Calculus of Thermodynamics
    Supplementary Notes for Chapter 5 The Calculus of Thermodynamics Objectives of Chapter 5 1. to understand the framework of the Fundamental Equation – including the geometric and mathematical relationships among derived properties (U, S, H, A, and G) 2. to describe methods of derivative manipulation that are useful for computing changes in derived property values using measurable, experimentally accessible properties like T, P, V, Ni, xi, and ρ . 3. to introduce the use of Legendre Transformations as a way of alternating the Fundamental Equation without losing information content Starting with the combined 1st and 2nd Laws and Euler’s theorem we can generate the Fundamental Equation: Recall for the combined 1st and 2nd Laws: • Reversible, quasi-static • Only PdV work • Simple, open system (no KE, PE effects) • For an n component system n dU = Td S − PdV + ∑()H − TS i dNi i=1 n dU = Td S − PdV + ∑µidNi i=1 and Euler’s Theorem: • Applies to all smoothly-varying homogeneous functions f, f(a,b,…, x,y, … ) where a,b, … intensive variables are homogenous to zero order in mass and x,y, extensive variables are homogeneous to the 1st degree in mass or moles (N). • df is an exact differential (not path dependent) and can be integrated directly if Y = ky and X = kx then Modified: 11/19/03 1 f(a,b, …, X,Y, …) = k f(a,b, …, x,y, …) and ⎛ ∂f ⎞ ⎛ ∂f ⎞ x⎜ ⎟ + y⎜ ⎟ + ... = ()1 f (a,b,...x, y,...) ⎝ ∂x ⎠a,b,...,y,.. ⎝ ∂y ⎠a,b,..,x,.. Fundamental Equation: • Can be obtained via Euler integration of combined 1st and 2nd Laws • Expressed in Energy (U) or Entropy (S) representation n U = fu []S,V , N1, N2 ,..., Nn = T S − PV + ∑µi Ni i=1 or n U P µi S = f s []U,V , N1, N2 ,..., Nn = + V − ∑ Ni T T i=1 T The following section summarizes a number of useful techniques for manipulating thermodynamic derivative relationships Consider a general function of n + 2 variables F ( x, y,z32,...,zn+ ) where x ≡ z1, y ≡ z2.
    [Show full text]
  • 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.........................................
    [Show full text]
  • 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.
    [Show full text]
  • W. M. White Geochemistry Appendix II Summary of Important Equations
    W. M. White Geochemistry Appendix II Summary of Important Equations Equations of State: Ideal GasLaw: PV = NRT Coefficient of Thermal Expansion: ∂ α≡α ≡ 1 V V ∂T Compressibility: ∂V β≡β≡± 1 V ∂P Van der Waals Equation: RT a P= - 2 V ± b V The Laws of Thermdynamics: First Law: ∆U = Q + W 1 written in differential form: dU = dQ + dW 2 work done on the system and heat added to the system are positive. The first law states the equivalence of heat and work and the conservation of energy. Second Law: dQrev = TdS 3 Two ways of stating the second law are Every system left to itself will, on average, change to a condition of maximum probability and Heat cannot be extracted from a body and turned entirely into work. Third Law: lim S= 0 T → 0 3 This follows from the facts that S = R ln Ω and Ω =1 at T = 0 for a perfectly crystalline pure substance. Primary Variables of Thermodynamics The leading thermodynamic properties of a fluid are determined by the relations which exist between the volume, pressure, termperature, energy and entropy of a given mass of fluid in a state of thermodynamic equilibrium - J. W. Gibbs The primary variables of thermodynamics are P, V, T, U, and S. Other thermodynamic functions can be stated in terms of these variables. For various combination of these variables there are 1 W. M. White Geochemistry Appendix II Equation Summary characteristics functions. The characteristic function for S and V is one of the primary variables: U. Thus dU = TdS + PdV 5 Other Important Thermodynamic Functions What then is the use of thermodynamic equations? They are useful precisely because some quantities are easier to measure than others.
    [Show full text]
  • Basic Thermodynamics
    Basic Thermodynamics Handout 1 First Law of Thermodynamics Basically a statement of conservation of energy which includes heat as a form of energy: dU = ¯dQ + ¯dW; where ¯dQ is heat absorbed by the system, and ¯dW is work done on the system. U is a function of state called internal energy. Zeroth Law of Thermodynamics Suppose A, B and C are distinct thermodynamic systems. If A is in thermal equilibrium with B, and B is in thermal equilibrium with C, then A is in thermal equilibrium with C. Systems in thermodynamic equilibrium can be described in terms of physical variables that do not change with time. The Zeroth Law implies that there exists some physical property which systems that are in thermal equilibrium have in common, regardless of their size, shape, substance, etc. We call this property temperature.A thermometer is a device that can be used to assign a numerical value to temperature through measurements of a physical property. Constant-volume gas thermometer. The mercury reservoir is raised or lowered to adjust the difference in height h between the two mer- cury columns M and M 0 so that the volume of gas in the bulb + capillary is constant. Absolute temperature (perfect gas scale) lim ! (pV ) T (K) = 273:16 p 0 T ; limp!0(pV )TP where TP stands for the triple point of water. Right: Readings of a constant- volume gas thermometer for the temperature of condensing steam as a function of the pressure p3 at the triple point of water. Curves for different gases are shown.
    [Show full text]
  • Exact Differential Equations Section 2.4
    Exact Differential Equations Section 2.4 ● Motivation ● Definition of an Exact Equation ● Criterion Theorem ● Solution Method ● Examples of Solving Exact DEs ● Making Equations Exact Motivating Exact Equations Our tools so far allow us to solve first-order DEs which are: separable, and linear. But what about something like: tan x−sin x sin ydxcos x cos ydy=0 The problem is: ● This equation is not separable. Why? ● This equation is not linear. Why? ● We need a new way to solve such equations! Solving Such a Problem In this section we will develop a method for solving differential equations by working backward. That is, we will start with a solution function and determine what sorts of differential equations such a function will solve. f x , y=c From calculus, the total differential for such a function is: ∂ f ∂ f dz= dx dy Renaming, rearranging, ∂ x ∂ y and computing dz yields: M x , ydxN x , ydy=0 Definition of an Exact Equation Definition 2.3 A differential expression M(x,y) dx + N(x,y) dy is an exact differential in a region R of the xy-plane if it corresponds to the differential of some function f(x,y) defined on R. A first-order differential equation of the form M x , ydxN x , ydy=0 is said to be an exact equation if the expression on the left-hand side is an exact differential. In this case, an implicit solution is: f x , y=c Criterion for an Exact DE Theorem 2.1 Let M(x,y) and N(x,y) be continuous and have continuous first partial derivatives in a rectangular region R.
    [Show full text]
  • Chapter 3: the Math of Thermodynamics
    Winter 2013 Chem 254: Introductory Thermodynamics Chapter 3: The Math of Thermodynamics .................................................................................... 25 Derivatives of functions of a single variable ............................................................................. 25 Partial Derivatives ..................................................................................................................... 26 Total Differentials ..................................................................................................................... 28 Differential Forms ..................................................................................................................... 31 Integrals .................................................................................................................................... 32 Line Integrals ............................................................................................................................. 32 Exact vs Inexact Differential ...................................................................................................... 33 Definition of β and κ ................................................................................................................. 36 Dependence of U on T and V .................................................................................................... 37 Dependence of H on T and P .................................................................................................... 37 Derivations
    [Show full text]