Reversible Isothermal Expansion

College Depth 99 in the knowledge graph I know this Set as goal
Unlocks 54 downstream topics
reversible-processes isothermal work-heat

Core Idea

In a reversible isothermal expansion of an ideal gas, temperature (and internal energy) remain constant, so Q = W = nRT ln(V_f/V_i) = nRT ln(P_i/P_f). The gas does maximum work for a given pressure drop. This process is reversible because the system remains infinitesimally close to equilibrium.

Explainer

You already know that the boundary work done by a gas expanding against a piston is W = ∫P dV, and that an isothermal process holds temperature constant. For an ideal gas, the internal energy depends only on temperature: U = nC_vT. If T is constant, then ΔU = 0, and the first law immediately gives Q = W — all the heat absorbed from the surroundings is converted to work. This is not a perpetual motion trick: the temperature stays constant only because the system continuously draws heat from an external reservoir at temperature T.

The work integral uses the ideal gas law to substitute P = nRT/V at each point along the path: W = ∫_{V_i}^{V_f} (nRT/V) dV = nRT ln(V_f/V_i). Since the gas expands (V_f > V_i), the logarithm is positive and W > 0 — the gas does positive work and absorbs heat. The equivalent form W = nRT ln(P_i/P_f) follows from PV = const at fixed T: if volume doubles, pressure halves, and ln(V_f/V_i) = ln(P_i/P_f). A doubling of volume at 300 K for one mole gives W = (1)(8.314)(300)ln(2) ≈ 1729 J — entirely absorbed from the heat reservoir.

The word reversible means something precise here: the expansion is performed infinitely slowly, with the external pressure kept just infinitesimally below the gas pressure at every moment. This ensures the system passes through a continuous sequence of equilibrium states. Any faster expansion — where the external pressure jumps below the gas pressure and the gas expands into an unresisted space — is irreversible: it produces less work (in the limit of free expansion into a vacuum, zero work) for the same initial and final states. The reversible isothermal path gives the maximum possible work for an isothermal expansion between V_i and V_f, because it extracts work against the largest possible opposing force at every step.

This process appears in two critical places you will encounter soon. First, it is one of the four strokes of the Carnot cycle — the two isothermal steps (one at T_H, one at T_C) are where the engine exchanges heat with its reservoirs, and the reversibility of those strokes is what makes the Carnot engine achieve the maximum possible efficiency. Second, the entropy change ΔS = Q/T = nR ln(V_f/V_i) calculated here generalizes: for any process, reversible or not, ΔS between two equilibrium states is the same, so the reversible isothermal expression gives you a direct way to compute entropy changes for ideal gas expansions.

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 ProcessesPolytropic Processes and the Polytropic IndexP-V Diagram Interpretation and Thermodynamic ProcessesBoundary Work and P-V DiagramsReversible Adiabatic (Isentropic) ProcessesReversible Isothermal Expansion

Longest path: 100 steps · 438 total prerequisite topics

Prerequisites (3)

Leads To (1)