MSEG 803 Equilibria in Material Systems 5: Maxwell Relations & Stability Prof. Juejun (JJ) Hu hujuejun@udel.edu Second order derivatives Heat capacity 2G Q S CP T T 2 dT T T P P Coefficient of thermal expansion 1 V 1 2G V T P V T P 2 F S CV T T 2 T T V 3 L Isotropy: 3 L L T P Isothermal compressibility 1 V 1 2G T V P T V P 2 Maxwell relations 2 V G S V T T P P P T LHS: volume change as a function of temperature (thermal expansion) RHS: entropy change as a function of pressure Connects two seemingly unrelated quantities! General form conj (Y ) X Y conj ( X ) conj ( X ) Y Maxwell relations in single component simple systems Energy representation dU TdS PdV dN 2U T P V S V S S , N V , N 2U T N S N S S ,V V , N 2U P N P N V S ,V S , N Note the sign difference for terms involving P in the U representation Second order derivatives Of all second order derivatives, only 3 can be independent, and any given derivative can be expressed in terms of an arbitrarily chosen set of 3 basic derivatives The conventional choice: 2G S CP T T T 2 T P 1 V 1 2G V T P V T P 1 V 1 2G T V P T V P 2 3 physical observables in the Gibbs potential representation Procedures for reducing derivatives If the derivative contains any potentials, bring them to the numerator and eliminate using the differential form of fundamental equations If the derivative contains the chemical potential, bring it to the numerator and eliminate by means of the Gibbs-Duhem relation: d = -sdT + udP If the derivative contains the entropy, bring it to the numerator. If one of the Maxwell relations now eliminates the entropy, invoke it. If the Maxwell relations do not eliminate the entropy take the deriative of S with respect to T. The numerator will then be expressible as one of the specific heats (cv or cP) Bring the volume to the numerator. The remaining derivative will be expressible in terms of and T cv can be eliminated by the equation: cv = cP - Tv2/T Some useful relations X Y 1 X Z Y Z X X W Z Y Z X Z Y X Y Z Y W Z Z X Y Connecting CV and CP 2G S CP T T T 2 T P 2 F S CV T T T 2 T V S S S P CV T T T P T T V V P T S V V T T P T P T P V P T S V 2 TV 2 T CP T T T P Molar heat capacity: cV cP Tv 2 T Joule-Thomson (throttling) process T H P T P H H T P Isenthalpic curves T S S V T P T P T V T V CP T P T 1 V CP Inversion temperature: T 1 V 0 CP T 0 P H Inversion point: P > Pinv, J-T process leads to heating P < Pinv, J-T process leads to cooling Magnetic systems Quasi-static magnetic work: HdM M is an unconstrainable parameter! Fundamental equation: d SdT dN V i x, y , z M 1 V 1 V Unmagnetized (H = 0) ii Magnetized (H > 0) d ii MdH 1 V V V H T M V T H H T T M V V M H T T H T H thermal expansion 1 M H V H T V M H T T H 1 M xx Magnetostriction and piezomagnetic effect: V xx H H M Magnetic refrigeration S H=0 H = H1 0 T Fundamental equation: d SdT dN S M H T T H V i x, y , z ii d ii MdH Note that here H denotes the field not enthalpy Optomechanical force in science fictions: solar sail Count Dooku’s solar sailer: Star Wars Episode II: Attack of the Clones Optomechanical force x Photons confined in a resonant cavity (bouncing back and forth between two mirrors) Fundamental equation: dN dN Fdx Optomechanical force exerted by photons on the movable mirror: F N x x N FN F N x N The sign of , CV and T can either be positive or negative Positive : most materials Negative : liquid water (< 4 °C), cubic zirconium tungstate, quartz (over certain T range) CV and T are positive in stable TD systems Q If CV < 0, thermal fluctuation will be amplified leading to instability dV If T < 0, volume fluctuation will be amplified leading to instability Stability criteria 2 S 1 T 2 U U V , N Molar entropy s Ext. var. x x0 - Dx x0 1 T 1 0 2 2 T U V , N NT cV 2 F 1 P 0 2 V V T , N V T x0 + Dx 1 1 S ( x D x ) S ( x0 D x) S ( x0 ) Stability: 0 2 2 cV 0 T 0 General criterion: 2S 0 2 x 2 2S 2S 2S 0 U 2 V 2 U V Stable thermodynamic function Molar entropy s E G A to B, E to F: stable F D 2 S x 2 0 C to D: locally unstable 2 S x 2 0 B A C Ext. var. x B to C, D to E: locally stable, globally unstable 2 S x 2 0 The stable thermodynamic function S is the envelope of tangents everywhere above the underlying function S The line BGE corresponds to inhomogeneous mixtures of the two phases B and E: 1st order phase transition Le Chatelier-Braun principle If a chemical system at equilibrium experiences a change in concentration, temperature, volume, or partial pressure, then the equilibrium shifts to counteract the imposed change and a new equilibrium is established. Indirectly induced secondary processes also act to attenuate the initial perturbation