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Duhem–Margules equation

A binary-mixture thermodynamic constraint equating composition-scaled changes in the components’ equilibrium partial vapor pressures.

Version
v2 · 2026-09-19 · History
Domain-specific #
4279
Domain group
Natural Sciences
Origin domain
Chemistry & Materials Science
Subdomain
Solution Thermodynamics → Chemistry & Materials Science

Core Idea

For a binary liquid mixture in equilibrium with an ideal-gas vapor at fixed temperature, the equation follows from Gibbs–Duhem and relates each component’s logarithmic partial-pressure derivative to its liquid mole-fraction derivative. The Gibbs–Duhem constraint couples the two chemical-potential changes; ideal-gas vapor chemical potentials convert that coupling into partial-pressure slopes. The abstraction is therefore identified by a declared carrier, a transformation or constraint over that carrier, and an invariant that tells an analyst whether the named structure is genuinely present.

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Two Liquids, One Rule

When you mix two liquids, like water and alcohol, little bits of each float up into the air above them. If you add more of one liquid, the amounts floating up change. The Duhem–Margules equation is a rule saying those two changes are tied together: you can't change one without the other changing in a matching way.

The Linked Vapor Pressure Rule

When two liquids are mixed, like water and alcohol, some of each evaporates into the air above, and each one pushes with its own vapor pressure. The Duhem-Margules equation, which works at a fixed temperature, is a rule that ties these together. If you change the mix a little, the way one liquid's vapor pressure changes is linked to how the other's changes, adjusted for how much of each liquid is in the mix. So you can't change one liquid's vapor pressure without affecting the other's in a matching way.

Coupled Partial-Pressure Slopes

The Duhem–Margules equation applies to a mixture of two liquids in equilibrium with the vapor above it, at fixed temperature, when the vapor behaves like an ideal gas. It comes from the Gibbs–Duhem equation, which says the chemical potentials of the components in a mixture can't all change independently. For an ideal-gas vapor, chemical potential depends on the logarithm of partial pressure, so the constraint becomes a relation between partial pressures: x₁ times the slope of ln p₁ with respect to x₁ equals x₂ times the slope of ln p₂ with respect to x₂, where x₁ and x₂ are the liquid mole fractions that add to one. In practice it's used to check the consistency of vapor–liquid data, and it holds only under its stated conditions.

 

The Duhem-Margules equation relates the partial vapor pressures of the two components of a binary liquid mixture in equilibrium with its vapor at fixed temperature. It states that x1 (d ln p1 / d x1) = x2 (d ln p2 / d x2), where x1 and x2 are liquid mole fractions (summing to one) and p1 and p2 are partial pressures. The derivation starts from the Gibbs-Duhem relation, which at fixed temperature and pressure constrains the chemical-potential changes of the two components, x1 d mu1 + x2 d mu2 = 0, coupling them. Treating the vapor as an ideal gas, each component's chemical potential equals that of its vapor, which varies as RT ln p_i, so the coupling of chemical potentials becomes a coupling of logarithmic partial-pressure slopes. The result is a consistency condition on vapor-liquid equilibrium data. Its validity depends on the stated conditions: fixed temperature and pressure in the Gibbs-Duhem step, mole fractions summing to one, and the ideal vapor convention.

Scope of Application

Duhem–Margules equation belongs to solution thermodynamics and is useful where the analyst can specify the typed solution thermodynamics carrier, defining objects and relations, parameters, conventions, evidence, boundary cases, and comparison targets, then evaluate temperature and pressure are fixed, liquid mole fractions sum to one, vapor behavior follows the stated ideal convention, and the two scaled logarithmic slopes agree. The scope is broad within that domain but bounded by the need for temperature and pressure are fixed, liquid mole fractions sum to one, vapor behavior follows the stated ideal convention, and the two scaled logarithmic slopes agree. Conceptual equilibrium-thermodynamics identity only; no chemical preparation, operating condition, or laboratory procedure is provided.

Clarity

The abstraction clarifies a crowded vocabulary by making temperature and pressure are fixed, liquid mole fractions sum to one, vapor behavior follows the stated ideal convention, and the two scaled logarithmic slopes agree the center of the account. A claim should name the carrier, the governing operation or relation, the applicable assumptions, and the recognition test. A bare label is insufficient because the name Duhem–Margules equation can be used for a formal identity, an implementation, or a neighboring result unless carrier and convention are stated.

Manages Complexity

Without the abstraction, an analyst must reason directly over many local details: the carrier roles, admissibility assumptions, competing conventions, derived invariants, boundary cases, and proof or validation obligations specific to Duhem–Margules equation. Duhem–Margules equation compresses them into the roles in the structural signature. That compression permits comparison across instances without erasing the variables that determine validity. It also exposes which details may be varied safely and which are constitutive.

Abstract Reasoning

  1. Identify the carrier. State what the elements, states, objects, or observations are: the typed solution thermodynamics carrier, defining objects and relations, parameters, conventions, evidence, boundary cases, and comparison targets. Reject examples whose alleged carrier belongs to a different problem.
  2. Lock the constitutive rule. Express temperature and pressure are fixed, liquid mole fractions sum to one, vapor behavior follows the stated ideal convention, and the two scaled logarithmic slopes agree independently of one notation or implementation.

Knowledge Transfer

Knowledge transfers strongly among subfields of solution thermodynamics because they reuse the typed solution thermodynamics carrier, defining objects and relations, parameters, conventions, evidence, boundary cases, and comparison targets, The Gibbs–Duhem constraint couples the two chemical-potential changes; ideal-gas vapor chemical potentials convert that coupling into partial-pressure slopes., and type the carrier, state every parameter and convention in the definition, test that temperature and pressure are fixed, liquid mole fractions sum to one, vapor behavior follows the stated ideal convention, and the two scaled logarithmic slopes agree, compare the nearest accepted identity, and report counterexamples, uncertainty, and limiting cases.

Relationships to Other Abstractions

Local relationship map for Duhem–Margules equationParents appear above the current abstraction, mutual partners to the right, and children below. Node labels state whether each abstraction is prime or domain-specific; colors identify relation types.Duhem–MargulesequationDOMAINPrime abstraction: Coupling — is a kind ofCouplingPRIME

Current abstraction Duhem–Margules equation Domain-specific

Parents (1) — outgoing typed relations

  • Duhem–Margules equation is a kind of Coupling Prime

    What makes it its own entry: the domain-specific identity determined by temperature and pressure are fixed, liquid mole fractions sum to one, vapor behavior follows the stated ideal convention, and the two scaled logarithmic slopes agree.

Hierarchy path (1) — routes to 1 parentless root

  • Duhem–Margules equation → is a kind of Coupling

Neighborhood in Abstraction Space

Duhem–Margules equation sits in a crowded region of the domain-specific corpus (27th percentile for distinctiveness): several abstractions share nearly its structure, so a description that fits it tends to fit its neighbors too.

Family — Thermodynamic States & Processes (32 abstractions)

Nearest neighbors

Computed from structural-signature embeddings · 2026-10-25