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๐ŸงคPhysical Chemistry I

Maxwell Relations

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Why This Matters

Maxwell relations are the Swiss Army knife of thermodynamicsโ€”they let you convert quantities that are impossible to measure directly into ones you can actually work with in the lab. You're being tested on your ability to derive these relations from thermodynamic potentials, recognize which relation to apply in a given situation, and use them to simplify complex calculations. These relations demonstrate a fundamental mathematical truth about thermodynamic state functions: the order of differentiation doesn't matter, which reveals deep connections between seemingly unrelated properties.

When you encounter problems involving entropy changes, heat capacities, or equations of state, Maxwell relations are often the key to unlocking a solution. Don't just memorize the four equationsโ€”understand which thermodynamic potential each one comes from and what physical insight each relation provides. Exam questions frequently ask you to derive a Maxwell relation from scratch or apply one to transform an unmeasurable quantity into something accessible.


The Mathematical Foundation: Exact Differentials

Maxwell relations exist because thermodynamic potentials are state functions with exact differentialsโ€”meaning the mixed second partial derivatives are equal regardless of the order of differentiation.

Equality of Mixed Partial Derivatives

  • Schwarz's theorem guarantees that for any well-behaved function f(x,y)f(x,y), we have โˆ‚2fโˆ‚xโˆ‚y=โˆ‚2fโˆ‚yโˆ‚x\frac{\partial^2 f}{\partial x \partial y} = \frac{\partial^2 f}{\partial y \partial x}
  • This mathematical symmetry is the entire foundation of Maxwell relationsโ€”no physics required, just calculus
  • The physical consequence is profound: it reveals hidden connections between thermodynamic properties that appear unrelated

State Functions and Path Independence

  • State functions like UU, HH, AA, and GG depend only on the current state, not how the system got there
  • Their exact differentials can be written as dz=Mโ€‰dx+Nโ€‰dydz = M\,dx + N\,dy where (โˆ‚Mโˆ‚y)x=(โˆ‚Nโˆ‚x)y\left(\frac{\partial M}{\partial y}\right)_x = \left(\frac{\partial N}{\partial x}\right)_y
  • This exactness condition is precisely what generates each Maxwell relation when applied to thermodynamic potentials

Compare: State functions vs. path functionsโ€”UU, HH, AA, GG are state functions (exact differentials, Maxwell relations apply), while qq and ww are path functions (inexact differentials, no Maxwell relations). If an FRQ gives you a differential and asks whether Maxwell relations apply, check for path dependence first.


The Four Thermodynamic Potentials

Each Maxwell relation derives from one of the four fundamental thermodynamic potentials. The natural variables of each potential determine which Maxwell relation you get.

Internal Energy U(S,V)U(S,V)

  • Fundamental equation: dU=TdSโˆ’PdVdU = TdS - PdV, giving natural variables entropy and volume
  • Coefficients identify T=(โˆ‚Uโˆ‚S)VT = \left(\frac{\partial U}{\partial S}\right)_V and โˆ’P=(โˆ‚Uโˆ‚V)S-P = \left(\frac{\partial U}{\partial V}\right)_S
  • Maxwell relation: (โˆ‚Tโˆ‚V)S=โˆ’(โˆ‚Pโˆ‚S)V\left(\frac{\partial T}{\partial V}\right)_S = -\left(\frac{\partial P}{\partial S}\right)_Vโ€”connects adiabatic temperature-volume behavior to entropy-pressure relationships

Enthalpy H(S,P)H(S,P)

  • Fundamental equation: dH=TdS+VdPdH = TdS + VdP, with natural variables entropy and pressure
  • Coefficients identify T=(โˆ‚Hโˆ‚S)PT = \left(\frac{\partial H}{\partial S}\right)_P and V=(โˆ‚Hโˆ‚P)SV = \left(\frac{\partial H}{\partial P}\right)_S
  • Maxwell relation: (โˆ‚Tโˆ‚P)S=(โˆ‚Vโˆ‚S)P\left(\frac{\partial T}{\partial P}\right)_S = \left(\frac{\partial V}{\partial S}\right)_Pโ€”useful for adiabatic processes at constant pressure

Compare: U(S,V)U(S,V) vs. H(S,P)H(S,P)โ€”both have entropy as a natural variable, but UU pairs it with volume (useful for constant-volume processes) while HH pairs it with pressure (useful for constant-pressure processes). Choose based on which variable is held constant in your problem.

Helmholtz Free Energy A(T,V)A(T,V)

  • Fundamental equation: dA=โˆ’SdTโˆ’PdVdA = -SdT - PdV, with natural variables temperature and volume
  • Coefficients identify โˆ’S=(โˆ‚Aโˆ‚T)V-S = \left(\frac{\partial A}{\partial T}\right)_V and โˆ’P=(โˆ‚Aโˆ‚V)T-P = \left(\frac{\partial A}{\partial V}\right)_T
  • Maxwell relation: (โˆ‚Sโˆ‚V)T=(โˆ‚Pโˆ‚T)V\left(\frac{\partial S}{\partial V}\right)_T = \left(\frac{\partial P}{\partial T}\right)_Vโ€”the most frequently used relation, connects entropy to the equation of state

Gibbs Free Energy G(T,P)G(T,P)

  • Fundamental equation: dG=โˆ’SdT+VdPdG = -SdT + VdP, with natural variables temperature and pressure
  • Coefficients identify โˆ’S=(โˆ‚Gโˆ‚T)P-S = \left(\frac{\partial G}{\partial T}\right)_P and V=(โˆ‚Gโˆ‚P)TV = \left(\frac{\partial G}{\partial P}\right)_T
  • Maxwell relation: (โˆ‚Sโˆ‚P)T=โˆ’(โˆ‚Vโˆ‚T)P\left(\frac{\partial S}{\partial P}\right)_T = -\left(\frac{\partial V}{\partial T}\right)_Pโ€”connects entropy changes to thermal expansion, essential for chemical applications

Compare: A(T,V)A(T,V) vs. G(T,P)G(T,P)โ€”both have temperature as a natural variable and are most useful for isothermal processes. Use AA for constant-volume systems (like rigid containers) and GG for constant-pressure systems (like open beakers). The Gibbs relation appears most often in chemistry because lab work typically occurs at constant TT and PP.


Practical Applications

Maxwell relations transform unmeasurable quantities into experimentally accessible ones. The key is recognizing when a derivative you need can be replaced by one you can measure.

Calculating Entropy Changes

  • The problem: (โˆ‚Sโˆ‚V)T\left(\frac{\partial S}{\partial V}\right)_T and (โˆ‚Sโˆ‚P)T\left(\frac{\partial S}{\partial P}\right)_T cannot be measured directlyโ€”you can't "see" entropy
  • The solution: Use Maxwell relations to convert these to (โˆ‚Pโˆ‚T)V\left(\frac{\partial P}{\partial T}\right)_V and โˆ’(โˆ‚Vโˆ‚T)P-\left(\frac{\partial V}{\partial T}\right)_P, both measurable from equations of state
  • Exam application: When asked to find ฮ”S\Delta S for an isothermal process, immediately look for the appropriate Maxwell relation

Deriving Heat Capacity Relationships

  • CPโˆ’CVC_P - C_V derivation relies critically on Maxwell relations to eliminate entropy derivatives
  • The final result CPโˆ’CV=TVฮฑ2ฮบTC_P - C_V = \frac{TV\alpha^2}{\kappa_T} uses ฮฑ\alpha (thermal expansion) and ฮบT\kappa_T (isothermal compressibility)โ€”both measurable
  • Why it matters: This equation explains why CP>CVC_P > C_V for all substances and quantifies the difference

Joule-Thomson Coefficient

  • The coefficient ฮผJT=(โˆ‚Tโˆ‚P)H\mu_{JT} = \left(\frac{\partial T}{\partial P}\right)_H describes temperature change during throttling
  • Maxwell relations help express this in terms of CPC_P, VV, and ฮฑ\alpha: ฮผJT=VCP(Tฮฑโˆ’1)\mu_{JT} = \frac{V}{C_P}(T\alpha - 1)
  • Physical insight: Predicts whether a gas cools or warms upon expansionโ€”critical for refrigeration and gas liquefaction

Compare: Entropy calculations vs. heat capacity derivationsโ€”both use Maxwell relations, but entropy problems typically need a single relation applied directly, while heat capacity problems often require combining multiple relations with chain rules. FRQs on CPโˆ’CVC_P - C_V are common; practice the full derivation.


Special Systems and Phase Transitions

Maxwell relations become particularly powerful when applied to specific systems or phase boundaries. They reveal universal behavior that transcends the details of any particular substance.

Ideal Gas Verification

  • Test the relations: For an ideal gas with PV=nRTPV = nRT, verify that (โˆ‚Pโˆ‚T)V=nRV\left(\frac{\partial P}{\partial T}\right)_V = \frac{nR}{V} and (โˆ‚Sโˆ‚V)T=nRV\left(\frac{\partial S}{\partial V}\right)_T = \frac{nR}{V}
  • Physical meaning: Entropy increases with volume at constant temperature because more microstates become accessible
  • Exam strategy: Ideal gas problems are excellent for checking your Maxwell relation workโ€”if the relation doesn't hold, you made an error

Clapeyron Equation and Phase Boundaries

  • Phase equilibrium requires dGฮฑ=dGฮฒdG^\alpha = dG^\beta along the coexistence curve
  • The Clapeyron equation dPdT=ฮ”Sฮ”V=ฮ”HTฮ”V\frac{dP}{dT} = \frac{\Delta S}{\Delta V} = \frac{\Delta H}{T\Delta V} follows from Maxwell-type reasoning
  • Applications: Predicts how melting points change with pressure, explains why ice skating works, describes vapor pressure curves

Critical Point Behavior

  • Near the critical point, (โˆ‚Pโˆ‚V)Tโ†’0\left(\frac{\partial P}{\partial V}\right)_T \to 0 and (โˆ‚2Pโˆ‚V2)Tโ†’0\left(\frac{\partial^2 P}{\partial V^2}\right)_T \to 0
  • Maxwell relations predict diverging response functions like ฮบT\kappa_T and CPC_P at criticality
  • Significance: Universal behavior near critical pointsโ€”all fluids behave similarly regardless of chemical identity

Compare: Ideal gas vs. real gas applicationsโ€”ideal gases provide clean verification of Maxwell relations, while real gases reveal their predictive power. The van der Waals equation with Maxwell relations predicts liquid-vapor coexistence and critical behavior that ideal gas equations cannot capture.


Quick Reference Table

ConceptBest Examples
Thermodynamic potential โ†’ Maxwell relationUโ†’(โˆ‚Tโˆ‚V)S=โˆ’(โˆ‚Pโˆ‚S)VU \to \left(\frac{\partial T}{\partial V}\right)_S = -\left(\frac{\partial P}{\partial S}\right)_V; Gโ†’(โˆ‚Sโˆ‚P)T=โˆ’(โˆ‚Vโˆ‚T)PG \to \left(\frac{\partial S}{\partial P}\right)_T = -\left(\frac{\partial V}{\partial T}\right)_P
Converting unmeasurable to measurable(โˆ‚Sโˆ‚V)Tโ†’(โˆ‚Pโˆ‚T)V\left(\frac{\partial S}{\partial V}\right)_T \to \left(\frac{\partial P}{\partial T}\right)_V; (โˆ‚Sโˆ‚P)Tโ†’โˆ’(โˆ‚Vโˆ‚T)P\left(\frac{\partial S}{\partial P}\right)_T \to -\left(\frac{\partial V}{\partial T}\right)_P
Natural variable pairsU(S,V)U(S,V), H(S,P)H(S,P), A(T,V)A(T,V), G(T,P)G(T,P)
Heat capacity relationshipsCPโˆ’CV=TVฮฑ2/ฮบTC_P - C_V = TV\alpha^2/\kappa_T; Joule-Thomson coefficient
Phase transition applicationsClapeyron equation; critical point analysis
Mathematical foundationExact differentials; Schwarz's theorem; state function symmetry
Experimental connectionsThermal expansion ฮฑ\alpha; compressibility ฮบT\kappa_T; equation of state derivatives
Ideal gas verification(โˆ‚Pโˆ‚T)V=nR/V\left(\frac{\partial P}{\partial T}\right)_V = nR/V matches (โˆ‚Sโˆ‚V)T\left(\frac{\partial S}{\partial V}\right)_T

Self-Check Questions

  1. Starting from dG=โˆ’SdT+VdPdG = -SdT + VdP, derive the Maxwell relation (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 and explain why this relation is useful for calculating entropy changes at constant temperature.

  2. Which two thermodynamic potentials have temperature as a natural variable, and how do you decide which one to use for a given problem?

  3. Compare and contrast the Maxwell relations derived from U(S,V)U(S,V) and H(S,P)H(S,P)โ€”what physical situations favor each one?

  4. An FRQ asks you to express (โˆ‚Sโˆ‚V)T\left(\frac{\partial S}{\partial V}\right)_T in terms of measurable quantities for a van der Waals gas. Which Maxwell relation do you use, and what equation of state derivative do you need?

  5. Explain why Maxwell relations cannot be applied to heat (qq) or work (ww), and identify what mathematical property distinguishes state functions from path functions in this context.