Gibbs Free Energy

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Core Idea

Gibbs free energy G = H − TS = U + PV − TS is the natural thermodynamic potential at constant T and P. Equilibrium occurs at minimum G; phase transitions occur when Gibbs energies of competing phases are equal. It governs chemical reactions and phase behavior under constant pressure.

Explainer

You already know the Helmholtz free energy F = U − TS, which is the natural thermodynamic potential when you control temperature and volume. But most chemistry and much of physics happens at fixed temperature *and* fixed pressure — think of reactions open to the atmosphere, or water boiling at sea level. For those conditions, you need a different potential. The Gibbs free energy G = H − TS = U + PV − TS is constructed by adding the PV term to Helmholtz, turning the natural variables from (T, V) to (T, P). The shift is a Legendre transform — the same mathematical trick that converts the Lagrangian to the Hamiltonian in mechanics, swapping a variable for its conjugate.

The physical meaning of G follows directly. For a process at constant T and P, the second law requires that the total entropy of system plus surroundings increases. Working through this constraint, you find that spontaneous processes at constant T and P must have dG ≤ 0. The system relaxes toward the state of minimum Gibbs free energy. Equilibrium occurs when dG = 0 — no more free energy can be extracted. This is the condition that chemical reactions and phase transitions satisfy at equilibrium.

Phase transitions become transparent in the Gibbs framework. At the melting point of ice, for example, both liquid water and solid ice are present simultaneously. This is only possible if their Gibbs free energies are equal: G_liquid(T_m, P) = G_solid(T_m, P). Below T_m the solid has lower G and is stable; above T_m the liquid wins. The transition temperature is exactly where the two G curves cross. For a first-order transition, the crossing has a kink — the first derivative of G (which gives entropy S = −(∂G/∂T)_P and volume V = (∂G/∂P)_T) is discontinuous, producing latent heat and a volume jump. For a second-order transition, G is continuous through the crossing but curves in a way that changes the second derivatives (heat capacity, compressibility), with no latent heat.

The decomposition G = H − TS captures the competition between energy and entropy. A reaction that releases enthalpy (exothermic, ΔH < 0) tends to lower G, making it spontaneous. A reaction that produces more disorder (ΔS > 0) also lowers G, especially at high temperature where the TS term dominates. This competition explains why some endothermic reactions still proceed spontaneously at high enough temperature — entropy wins — and why others that release heat are still suppressed at high temperature because they reduce entropy. The formula ΔG = ΔH − TΔS quantifies the tug-of-war between enthalpy and entropy that governs equilibrium in chemistry, materials science, and biology.

Practice Questions 5 questions

Prerequisite Chain

Counting to 10Counting to 20Understanding ZeroThe Number ZeroCounting to FiveOne-to-One CorrespondenceCombining Small Groups Within 5Addition Within 10Addition Within 20Two-Digit Addition Without RegroupingTwo-Digit Addition with RegroupingAddition Within 100Repeated Addition as MultiplicationMultiplication Facts Within 100Division as Equal SharingDivision as Grouping (Measurement Division)Division: Grouping (Repeated Subtraction) ModelDivision: Fair Sharing ModelDivision as Equal SharingDivision as GroupingBasic Division FactsDivision Facts Within 100Two-Digit by One-Digit DivisionDivision with RemaindersRemainders and Quotients in DivisionDivision Word ProblemsIntroduction to Long DivisionFactors and MultiplesPrime and Composite NumbersEquivalent FractionsRelating Fractions and DecimalsDecimal Place ValueReading and Writing DecimalsComparing and Ordering DecimalsAdding and Subtracting DecimalsMultiplying DecimalsDividing DecimalsDividing FractionsMixed Number ArithmeticOrder of OperationsInteger Order of OperationsVariable ExpressionsCombining Like TermsOne-Step EquationsTwo-Step EquationsSolving Multi-Step EquationsEquations with Variables on Both SidesAngle Pairs: Complementary, Supplementary, and VerticalParallel Lines and TransversalsCorresponding AnglesAlternate Interior AnglesTriangle Angle Sum TheoremExterior Angle TheoremTriangle Inequality TheoremSimilar Triangles: AA SimilaritySimilar Triangles: SSS and SAS SimilarityProportions in Similar TrianglesRight Triangle Trigonometry IntroductionTrigonometric Ratios ReviewRadian MeasureConverting Between Degrees and RadiansThe Unit CircleGraphing Sine and CosineGraphing Tangent and Reciprocal Trigonometric FunctionsDerivatives of Trigonometric FunctionsAntiderivativesIterated Integrals and Fubini's TheoremDouble Integrals in Cartesian CoordinatesDouble Integrals over Rectangular RegionsDouble Integrals in Polar CoordinatesDouble Integrals: Definition and SetupIterated Integrals and Fubini's TheoremDouble Integrals over Rectangular RegionsDouble Integrals over General RegionsApplications of Double Integrals: Area, Mass, and MomentsCenter of MassConservation of Linear MomentumElastic CollisionsInelastic CollisionsCoefficient of RestitutionCollision Analysis and Real-World ApplicationsTwo-Body Collisions in the Center-of-Mass FrameReduced Mass and Two-Body ProblemsKinematics in Two DimensionsProjectile MotionCircular Motion: KinematicsRotational KinematicsTorqueMoment of InertiaRotational Kinetic EnergyThe Work-Energy TheoremConservation of Mechanical EnergyFirst Law of ThermodynamicsThermodynamic Processes and the PV DiagramIsobaric and Isochoric ProcessesHeat EnginesThermal Efficiency of Heat EnginesRefrigerators and Heat PumpsSecond Law of ThermodynamicsEntropyMicrostates and MacrostatesEnsemble Theory FundamentalsCanonical Ensemble (NVT)Partition Function: Definition and PropertiesHelmholtz Free EnergyGibbs Free Energy

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