Fiveable

๐ŸงŠThermodynamics II Unit 7 Review

QR code for Thermodynamics II practice questions

7.1 Maxwell Relations and Thermodynamic Derivatives

7.1 Maxwell Relations and Thermodynamic Derivatives

Written by the Fiveable Content Team โ€ข Last updated August 2025
Written by the Fiveable Content Team โ€ข Last updated August 2025
๐ŸงŠThermodynamics II
Unit & Topic Study Guides

Maxwell Relations and Thermodynamic Derivatives

Maxwell relations and thermodynamic derivatives let you calculate properties that are hard to measure directly (like entropy) using properties that are easy to measure (like pressure, volume, and temperature). These tools are essential for analyzing real substances and designing engineering systems where you need to predict how a material responds to changing conditions.

Maxwell Relations for Thermodynamics

Derivation of Maxwell Relations

Maxwell relations come from a single mathematical fact: for any state function, the order of mixed second partial derivatives doesn't matter. Since thermodynamic potentials are state functions, their differentials are exact, which means:

โˆ‚2zโˆ‚xโ€‰โˆ‚y=โˆ‚2zโˆ‚yโ€‰โˆ‚x\frac{\partial^2 z}{\partial x \, \partial y} = \frac{\partial^2 z}{\partial y \, \partial x}

Each of the four thermodynamic potentials has two natural variables. When you apply the equality of mixed partials to each potential, you get one Maxwell relation:

PotentialNatural VariablesMaxwell Relation
Internal energy UUS,VS, V(โˆ‚Tโˆ‚V)S=โˆ’(โˆ‚Pโˆ‚S)V\left(\frac{\partial T}{\partial V}\right)_S = -\left(\frac{\partial P}{\partial S}\right)_V
Enthalpy HHS,PS, P(โˆ‚Tโˆ‚P)S=(โˆ‚Vโˆ‚S)P\left(\frac{\partial T}{\partial P}\right)_S = \left(\frac{\partial V}{\partial S}\right)_P
Helmholtz AAT,VT, V(โˆ‚Sโˆ‚V)T=(โˆ‚Pโˆ‚T)V\left(\frac{\partial S}{\partial V}\right)_T = \left(\frac{\partial P}{\partial T}\right)_V
Gibbs GGT,PT, Pโˆ’(โˆ‚Sโˆ‚P)T=(โˆ‚Vโˆ‚T)P-\left(\frac{\partial S}{\partial P}\right)_T = \left(\frac{\partial V}{\partial T}\right)_P
To derive any one of these, start with the differential form of the potential (e.g., dG=โˆ’Sโ€‰dT+Vโ€‰dPdG = -S\,dT + V\,dP), identify the first partial derivatives, then take the cross-partials and set them equal.

Interconnectedness of Thermodynamic Properties

Maxwell relations connect properties that seem unrelated at first glance. The Gibbs relation, for instance, links how entropy changes with pressure to how volume changes with temperature. There's no intuitive reason those two quantities should be equal, yet they are, for any substance.

  • They let you replace a derivative involving entropy (which you can't measure with a gauge) with one involving PP, VV, and TT (which you can).
  • They underpin more advanced results like the Clapeyron equation (phase boundary slopes) and the Gibbs-Duhem equation (multicomponent systems).
  • They reveal constraints: not every combination of property changes is physically independent, because Maxwell relations tie them together.

Applications of Maxwell Relations

Calculating Thermodynamic Properties and Derivatives

The most common use of Maxwell relations is converting an unmeasurable derivative into a measurable one. Here's the general approach:

  1. Identify the target derivative. Write down the partial derivative you need, noting which variables are held constant.
  2. Match it to a Maxwell relation. Find the relation that contains your target derivative (or use a combination of Maxwell relations with the triple product rule or chain rule if needed).
  3. Substitute measurable quantities. Replace the derivative with its Maxwell-equivalent, which should involve PP, VV, TT, or tabulated material properties like ฮฑP\alpha_P and ฮบT\kappa_T.
  4. Integrate if needed. If you need a finite change (not just a derivative), integrate over the appropriate path, applying boundary conditions.

Concrete example: Suppose you need (โˆ‚Sโˆ‚P)T\left(\frac{\partial S}{\partial P}\right)_T for a gas. You can't measure entropy directly, but the Gibbs-derived Maxwell relation gives:

(โˆ‚Sโˆ‚P)T=โˆ’(โˆ‚Vโˆ‚T)P\left(\frac{\partial S}{\partial P}\right)_T = -\left(\frac{\partial V}{\partial T}\right)_P

The right side is just โˆ’VฮฑP-V\alpha_P, where ฮฑP\alpha_P is the isobaric expansivity, a quantity you can look up or measure with standard lab equipment.

Designing and Optimizing Engineering Systems

Maxwell relations show up whenever you need to predict how a working fluid responds to changing conditions:

  • Heat engines and power cycles: Analyzing how entropy changes with pressure helps you evaluate irreversibilities and optimize cycle efficiency.
  • Refrigeration systems: Understanding (โˆ‚Tโˆ‚P)S\left(\frac{\partial T}{\partial P}\right)_S (related to the isentropic expansion/compression process) guides refrigerant selection and compressor design.
  • Chemical process design: When you need thermodynamic properties at conditions where no experimental data exists, Maxwell relations let you extrapolate from available PVTPVT data or equations of state.

Significance of Maxwell Relations

Connecting Seemingly Unrelated Properties

The deeper point of Maxwell relations is that thermodynamic properties are not independent. Knowing how volume responds to temperature at constant pressure automatically tells you how entropy responds to pressure at constant temperature. This means a single set of PVTPVT measurements, combined with heat capacity data, can in principle give you every thermodynamic property of a substance.

Enabling the Calculation of Hard-to-Measure Properties

Entropy, internal energy, and Helmholtz free energy cannot be read off an instrument. Maxwell relations provide the bridge:

  • You measure PP, VV, TT, and heat capacities.
  • You use Maxwell relations (and related identities) to express entropy changes, energy changes, and other derived quantities in terms of those measurements.
  • This eliminates the need for calorimetric experiments at every single state point, saving significant time and cost in both research and engineering practice.

Thermodynamic Derivatives for Analysis

Quantifying the Response of Substances to Changes

Thermodynamic derivatives put a number on how a substance responds when you change conditions. The three most important material derivatives are:

  • Isobaric expansivity ฮฑP=1V(โˆ‚Vโˆ‚T)P\alpha_P = \frac{1}{V}\left(\frac{\partial V}{\partial T}\right)_P โ€” fractional volume change per unit temperature increase at constant pressure. For liquid water near 20ยฐC, ฮฑPโ‰ˆ2.07ร—10โˆ’4โ€‰Kโˆ’1\alpha_P \approx 2.07 \times 10^{-4} \, \text{K}^{-1}.
  • Isothermal compressibility ฮบT=โˆ’1V(โˆ‚Vโˆ‚P)T\kappa_T = -\frac{1}{V}\left(\frac{\partial V}{\partial P}\right)_T โ€” fractional volume decrease per unit pressure increase at constant temperature. The negative sign ensures ฮบT>0\kappa_T > 0 for normal substances (volume decreases as pressure increases).
  • Heat capacities CPC_P and CVC_V โ€” energy required to raise temperature by one degree at constant pressure or constant volume, respectively.

These three quantities, combined with Maxwell relations, let you express any second-order thermodynamic derivative for a simple compressible substance. A useful identity connecting them:

CPโˆ’CV=TVฮฑP2ฮบTC_P - C_V = \frac{TV\alpha_P^2}{\kappa_T}

This relation shows that CPC_P is always greater than or equal to CVC_V, with equality only when ฮฑP=0\alpha_P = 0 (which happens for water at 4ยฐC, its density maximum).

Predicting Substance Behavior Under Specific Conditions

The signs and magnitudes of thermodynamic derivatives tell you what a substance will actually do:

  • A positive ฮฑP\alpha_P means the substance expands when heated at constant pressure (most materials). A negative ฮฑP\alpha_P means it contracts when heated (water between 0ยฐC and 4ยฐC).
  • A large ฮบT\kappa_T means the substance is highly compressible (gases), while a small ฮบT\kappa_T indicates near-incompressibility (liquids and solids).
  • The ratio CP/CVC_P/C_V (often written ฮณ\gamma) governs the speed of sound in a material and the slope of isentropic processes on a PVPV diagram.

This predictive capability matters for material selection (choosing alloys that won't warp under thermal cycling), process design (sizing expansion valves in refrigeration), and safety analysis (predicting pressure buildup in sealed containers during heating).