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Reversible Isothermal Expansion

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Boundary Work and P-V DiagramsIsothermal Processes+1 moreEntropy Definition and Calculation
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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

Understanding ZeroThe Number ZeroCounting to FiveCounting to 10Counting to 20Counting a Set of Objects Up to 20Cardinality: The Last Number CountedMatching Numerals to QuantitiesSubitizing Small QuantitiesAddition Within 10Number Bonds to 10Addition Within 20Doubles and Near DoublesDoubles Facts Within 10Near Doubles Facts Within 20Mental Math Strategies for AdditionMental Math: Adding and Subtracting TensAddition Within 100Repeated Addition as MultiplicationMultiplication as Equal GroupsMultiplication: ArraysBasic Multiplication Facts (0s, 1s, 2s, 5s, 10s)Multiplication 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 100Multiplication and Division Fact FamiliesRelationship Between Multiplication and DivisionDivision Facts as Inverse of MultiplicationRemainders and Quotients in DivisionDivision Word ProblemsMulti-Step Word ProblemsSolving Multi-Step Word ProblemsMultiplication Word ProblemsDivision Word ProblemsIntroduction to Long DivisionFactors and MultiplesPrime and Composite NumbersEquivalent FractionsRelating Fractions and DecimalsDecimal Place ValueIntegers and the Number LineComparing and Ordering IntegersAbsolute ValueAdding IntegersSubtracting IntegersMultiplying IntegersDividing IntegersUnit RatesProportionsPercent ConceptConverting Between Fractions, Decimals, and PercentsOperations with Rational NumbersTwo-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 IntroductionSine, Cosine, and Tangent RatiosTrigonometric Ratios ReviewRadian MeasureConverting Between Degrees and RadiansThe Unit CircleGraphing Sine and CosineGraphing Tangent and Reciprocal Trigonometric FunctionsDerivatives of Trigonometric FunctionsAntiderivativesIndefinite IntegralsBasic Integration RulesRiemann SumsDefinite Integral DefinitionDouble 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 DiagramIntensive and Extensive PropertiesState Variables and FunctionsPath Functions versus State FunctionsTypes of Work: Mechanical PdV and BeyondPolytropic Processes and the Polytropic IndexP-V Diagram Interpretation and Thermodynamic ProcessesBoundary Work and P-V DiagramsReversible Adiabatic (Isentropic) ProcessesReversible Isothermal Expansion

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