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Introduction Combined statement of 1st and 2nd Laws of Thermodynamics: dU = TdS – PdV. This equation provides: Relationship between U versus V and S: U = U(S,V) or dU = (∂U/∂S)VdS + (∂U/∂V)SdV The criteria for equilibrium: in a system of constant V and S; the internal energy has its ……….. value, or, in a system of constant U and V, the entropy has its ………… value. Outline • Introduction • Enthalpy and entropy dependence on P and T • Gibbs free energy dependence on P and T • Clapeyron equation • Gibbs-Duhem equation The problem is that the pair of independent variables (S,V) is rather inconvenient since entropy is hard to measure or control. Therefore it is desired to have fundamental equations with independent variables that are easier to control. The two convenient choices are: • Unary phase diagrams • Gibbs phase rule • Driving force for a phase transition • P and T The practical usefulness of thermo of materials is determined by the • First order and second-order phase transitions • V and T Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/1 MECH6661 lecture 5/2 Gibbs Free Energy From practical point of view, P and T pair is the best choice because they are easy to control and measure. - For systems with constant pressure the most suitable state function is the Gibbs free energy G = H - TS On the other hand, V and T pair is easy to examine in statistical mechanics. - For systems with constant volume (and variable pressure), the most suitable state function is the ………….. free energy A = U – TS In principle, any state function can be used to describe any system at equilibrium, but for a given system some are more convenient than others. The most convenient one for materials (usually under constant pressure) is the ……… free energy. Mech. Eng. Dept. - Concordia University Mech. Eng. Dept. - Concordia University Dr. M. Medraj Introduction Dr. M. Medraj practicality of the equations of state for the system (or the relationships which can be established among the thermo properties). MECH6661 lecture 5/3 G = H – TS = U + PV – TS ⇒ dG = dU+PdV+VdP–TdS–SdT From 1st law: dU = TdS – PdV Combine both: ⇒ dG = VdP – SdT G = G(P,T) ⇒ dG = (∂G/∂P)TdP + (∂G/∂T)PdT Comparing the two equations we see that: V = (∂G/∂P)T and S = – (∂G/∂T)P For isothermal-isobaric system the equilibrium state corresponds to the minimum of the Gibbs Free Energy (dG=0). - From G = H – TS, we see that low values of G are obtained with low values of H and high values of S. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/4 The Helmholtz Free Energy The Helmholtz Free Energy A = U – TS ⇒ dA = dU–TdS–SdT From 1st law: dU = TdS – PdV • This figure illustrates the criterion for equilibrium in a closed solid-vapor system at constant V and T. • The transfer of one atom to vapor increases U by a sublimation energy, whereas increase of entropy is slowing down with increasing number of atoms in the vapor phase, nv. Combine both: ⇒ dA = -PdV – SdT A = A(V,T) ⇒ dA = (∂A/∂V)TdV + (∂A/∂T)VdT Comparing the two equations we see that: P = – (∂A/∂V)T and S = – (∂A/∂T)V T1 < T2 Figure 5.3 - Gaskell At constant T and V the equilibrium state corresponds to the minimum of the Helmholtz Free Energy (dA=0). - From A = U – TS, we see that low values of A are obtained with low values of U and high values of S. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/5 Often, entropy and energies are opposed to each other: High entropies mean low energies and vice versa. And the entropy part becomes more important at high temperatures. Dr. M. Medraj Gibbs Free Energy Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/6 Chemical Potential G = H – TS Equilibrium is a tradeoff between enthalpy and entropy • A change to a lower enthalpy state (H < 0, exothermic) usually decreases the randomness (S < 0). (e.g. solidification and oxidation) • A change to a higher entropy state (S > 0) usually increases the enthalpy (H > 0, endothermic). (e.g. melting and evaporation processes) • All of these processes are characterized by a lowering of the Gibbs free energy: ∆G = ∆(H - TS) < 0 • A crystal at equilibrium has its …………. Gibbs energy. • If the composition of the system changes during a process, then two independent variables are …. sufficient to describe the state of the system. • Chemical reactions or exchange with surroundings can lead to the change in composition (number of moles of different species, ni, nj, nk, ….). • The Gibbs free energy (as well as other thermodynamic potentials) is an extensive property, i.e. depends on …… of the system and on ………….. ……….. of different species, G = G(T,P,ni,nj,nk,…..). Fundamental equations for a closed system: 1st law: U=q – w Enthalpy: H=U+PV Gibbs energy: G = H – TS dU = TdS – PdV dH = TdS + VdP dG = VdP – SdT Helmholtz energy: A = U – TS dA = -PdV – SdT Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/7 If composition is not changing, dG = VdP – SdT ⇒ S = – (∂G/∂T)P,ni,nj and V = (∂G/∂P)T,ni,nj,… Dr. M. Medraj If ni varies: ⇒ nj where nj is the number of moles of every species other than the ith species. Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/8 Chemical Potential Chemical Potential This is called the chemical potential of the species i ⇒ • The chemical potential of the species i is the rate of increase of G with ni when species i are added to the system at constant T, P and number of moles of all the other species. • The above equation can be applied to open systems that exchange both matter and heat with their surroundings, as well as to closed systems where changes in composition may occur due to chemical reactions. Also, we can rewrite the 1st law for a closed system undergoing a reversible change in composition due to a chemical reaction: Also, we can obtain the following relations: Similar equations can be written for U, H, and A: These fundamental relations can be used to derive Maxwell equations. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/9 Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/10 Maxwell’s Equations: Example 1 Maxwell’s Equations Consider the dependence of the entropy of an ideal gas on the independent variables T and V: S = S(T,V) Since U is a state function, the order of differentiation for its second derivative does not matter: For a reversible constant volume process TdS = δqv = dU = CvdT and Therefore, for a system with constant composition: Using the following Maxwell equation And from other fundamental equations we have: and the ideal gas law, PV = RT, which gives Maxwell’s equations allow one to derive dependences among experimentally measurable quantities. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/11 Integration between states 1 and 2 gives Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/12 Maxwell Equations: Example 2 Maxwell Equations: Example 2 Considering V = V(P,T): Recall that While P and can be directly measured experimentally, …….. • It would be useful to express this term through other variables. • Differentiating the combined 1st and 2nd laws, dU = TdS - PdV by V at constant T we have and differentiating by T at constant V we have: ⇒ since (∂V/∂T)P and (∂V/∂P)T are extensive properties It would be more convenient to express cp - cv through intensive properties. For isotropic materials we can define Using Maxwell’s equation: this is valid for any system, we have not used any approximation. coefficient of …………………. α is small for solids (e.g. 1.7×10-5 K-1 for isothermal ………………. Cu, 1.0×10-6 K-1 for diamond at T = 300 K) ⇒ Dr. M. Medraj MECH6661 lecture 5/13 Mech. Eng. Dept. - Concordia University Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/14 Gibbs-Duhem Equation For a homogenous phase of two components, A and B, the fundamental equation becomes: dG SdT VdP A dn A B dnB If we now specify equilibrium at constant T and P: dG Adn A B dnB 0 Now, we have shown that G An A B nB Differentiating this, we obtain dG Adn A B dnB n Ad A nB d B At equilibrium dG Adn A B dnB n Ad A nB d B 0 Substituting the previous expression dG Adn A B dnB 0 we obtain n Ad A nB d B 0 n In the general case we get the Gibbs-Duhem equation ni di 0 10 minutes Break i 1 nB B 0 If we divide through both sides by dXA we get: n A A X A T ,P ,n X A T ,P ,n B And now dividing by nA + nB we get: Dr. M. Medraj B X A A 0 1 X A B X A T ,P ,nB X A T ,P ,nB Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/15 Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/16 G as Function of T at Constant P H and S as Function of T at Constant P • In a closed one-component system equilibrium, at temperature T and pressure P, corresponds to the state with ………… Gibbs free energy G. • Therefore, in order to predict what phases are stable under different conditions, we have to examine the dependence of G on T and P. • Let us use thermodynamic relations to predict the temperature dependence of H, S, and G at constant P. G = H - TS dG = -SdT +VdP Therefore for constant P: …………. …………… For H(T) we have For S(T) we have Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/17 G(T) for two phases at P = const Dr. M. Medraj G(T) for a single phase at P = const • At all temperatures, the liquid has a higher internal energy U and enthalpy H as compared to the solid. Therefore Gl > Gs at low T. • The liquid phase, however, has a higher entropy S than the solid phase at all T. Therefore Gl decreases more rapidly with T as compared to Gs. • At Tm Gl(T) crosses Gs(T) and both liquid and solid phases can co-exist in equilibrium (Gl = Gs) Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/18 P-T Phase Diagram (PD) for a Pure Material G as Function of T at Constant P The solid lines (phase boundary lines) on the phase diagram show the conditions where different phases coexist in equilibrium: Gphase1 = Gphase2 G(T) for two phases at P = const At Tm the heat supplied to the system will not rise its temperature but will be used to supply the …………... of melting ∆Hm that is required to convert solid into liquid. At Tm the heat capacity Cp = (∂H/∂T)P is infinite, i.e. addition of heat does not increase T. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/19 Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/20 The Relationship between P and V for Pure Substance Equilibrium Between Liquid and Solid Phases As pressure is increased at T1, the volume of the gas decreases. When the pressure reaches a certain value, the volume suddenly reduces as the gas liquefies A further increase in pressure causes little further reduction in volume as liquid is generally not compressible to a large extent. When the P-V relationship is examined at different T, one may obtain the results shown in the diagram below: A T5 dG = -SdT +VdP As we can see from this fundamental equation, the free energy of a phase increases with pressure: This means that if the two phases have …………… molar volumes, their free energies will increase by different amounts when pressure changes at a fixed T. Vl < Vs for water At the point A the liquid and vapor are indistinguishable and their densities are identical. Vl > Vs for most materials T4 Tc T2 T1 Dr. M. Medraj What is the curvature of the G(P) at const. T? This is called isothermal ……………….. All gases exhibit this type of behavior, but values of critical pressure and critical temperature vary from one substance to another. Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/21 This is the ……………. Dr. M. Medraj Equilibrium Between Two Phases Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/22 G as Function of T and P for Two Phases • We have seen that if two phases in equilibrium have different molar volumes, their free energies will increase by different amounts when P changes at certain T. • The equilibrium, therefore will be disturbed by the change in pressure. • The only way to maintain equilibrium at different pressures is to change temperature as well. Schematic representation of the equilibrium surfaces of the solid and liquid phases of water in G-T-P space. For two phases (say liquid and solid) in equilibrium Gl = Gs and dGl = dGs for infinitesimal change in T and P (so that the system remains in equilibrium): The planes show the free energies of liquid and solid phases, the intersections of the planes correspond to the (P, T) conditions needed for maintaining equilibrium between the phases, Gl = Gs We know that at equilibrium ∆G = 0 ⇒ ∆H – T ∆S = 0 ∴ ∆S = ∆H/T Clapeyron equation: it gives the relationship between the variations of P and T required to ⇒ maintain the equilibrium between two phases. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/23 Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/24 Unary System - Density Clapeyron’s Equation – Example 1 For liquid to gas transition: ∆V = Vg - Vl >> 0 ∆H = Hg - Hl > 0 i.e. we have to add heat to convert liquid to gas. Pressure Liquid Solid Vapor ⇒ ⇒ A typical phase diagram for a pure material Liquid Mech. Eng. Dept. - Concordia University Dr. M. Medraj Vapor MECH6661 lecture 5/25 Dr. M. Medraj Temperature Example 2: Gibbs Phase Rule MECH6661 lecture 5/26 Mech. Eng. Dept. - Concordia University Example 3: Gibbs Phase Rule The following is the phase diagram for a pure substance. Calculate the number of degrees of freedom at the triple point c Calculate the number of degrees of freedom at the triple point A Gibbs phase rule: Temperature Vapor This is the case for H2O (ice floats in liquid water), Ga, Ge, diamond Liquid Solid1 Solid For some materials, however, ∆V = Vs - Vl > 0 ⇒ Solid2 Pressure The slope of the equilibrium lines in a P-T phase diagram of a pure material reflects the relative densities of the two phases. Note what happens along the isotherm when you increase the pressure. Temperature Pressure For liquid to solid transition: ∆V = Vs - Vl < 0 for most materials ∆H = Hs - Hl < 0 i.e. heat is released upon crystallization. Which is denser liquid or solid? Gibbs phase rule: f=c–p+2-r f=c–p+2-r 1 (liquid=vapor) c A This special condition is established only at definite T and P which are characteristic of the substance and outside our control. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/27 The critical point is ……….... Dr. M. Medraj Mech. Eng. Dept. - Concordia University The vapor–liquid critical point denotes the conditions above which distinct liquid and gas phases do not exist. MECH6661 lecture 5/28 Vapor–Liquid Critical Point for Pure Substances Clapeyron’s Equation – Example 4 Some materials may exist in more than one crystal structure, this is called ………...……. If the material is an elemental solid, it is called ………. Close-packed FCC γ-Fe has a smaller molar volume than BCC α-Fe: ∆V = Vγ - Vα < 0 And at the same time ∆H = Hγ - Hα > 0 ⇒ Diagram shows the stable phases for pure iron at varying T and P. The effect of increasing P is to increase the area of the PD over which the phases of the smaller molar V (higher density) are stable. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 4/29 Phase Diagrams of One-Component Materials Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/30 The Driving Force for the Phase Transformation • If solid and liquid are in equilibrium, Gs = Gl and a slow addition of heat leads to the melting of some part of the solid, but does not change the total G of the system: G = nl Gl + ns Gs = const, where nl and ns are the numbers of moles of liquid and solid phases, and Gl and Gs are the molar Gibbs free energies. graphite From the phase diagram, what phase has higher density near two-phase equilibrium conditions: - Diamond or graphite? - Diamond or liquid carbon? - Graphite or liquid carbon? Dr. M. Medraj Mech. Eng. Dept. - Concordia University diamond MECH6661 lecture 5/31 • However, if energy is added or removed quickly, the system can be brought out of equilibrium (overheated or undercooled), the melting/freezing process is spontaneous/irreversible and G is decreasing. For small undercooling ∆T, we can neglect the difference in Cp of liquid and solid phases and assume that ∆H and ∆S are independent of T. Dr. M. Medraj Mech. Eng. Dept. - Concordia University The driving force for …………….. MECH6661 lecture 5/32 First-Order and Second-Order Phase Transitions First-Order and Second-Order Phase Transitions The classification of phase transitions proposed by Ehrenfest is based on the behavior of G near the phase transformation. First-order phase transition: first derivatives of G are discontinuous. Second-order phase transition: first derivatives of G are continuous, but second derivatives of G are discontinuous. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/33 Dr. M. Medraj Summary • Second order phase transitions include the ferromagnetic phase transition in materials such as iron, where the magnetization (which is the first derivative of the free energy with the applied magnetic field strength) increases continuously from zero as the temperature is lowered below the Curie temperature. The magnetic susceptibility (the second derivative of the free energy with the field) changes discontinuously. Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/34 Summary • The various solid/liquid/gas transitions are classified as first-order transitions because they involve a discontinuous change in density, which is the first derivative of the free energy with respect to chemical potential. Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 4/35 • Just knowing the internal energy U of a system with a constant volume and temperature is not enough to tell us what the equilibrium configuration will be. • There could be many macrostates with the same U. That is why just minimizing U (or H) is not good enough, we have to minimize A = U TS or G = H - TS to find the equilibrium configuration of the system. • Of all the macrostates possible for a given U (or H) the one with the largest entropy at the given temperature will be the one that the system will adopt. • Equilibrium occurs when the balance between a small energy and a large entropy is achieved. High entropies often mean small energies and vice versa - both quantities are opposed to each other. • The entropy of a certain macrostate can be calculated by the statistical definition of the entropy S, using the “Boltzmann entropy equation”: S = k ln Ω Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/36 Next time: Binary Solutions Dr. M. Medraj Mech. Eng. Dept. - Concordia University MECH6661 lecture 5/37