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Reversible Isothermal Expansion

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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 Zero → The Number Zero → Counting to Five → Counting to 10 → Counting to 20 → Counting a Set of Objects Up to 20 → Cardinality: The Last Number Counted → Matching Numerals to Quantities → Subitizing Small Quantities → Addition Within 10 → Number Bonds to 10 → Addition Within 20 → Doubles and Near Doubles → Doubles Facts Within 10 → Near Doubles Facts Within 20 → Mental Math Strategies for Addition → Mental Math: Adding and Subtracting Tens → Addition Within 100 → Repeated Addition as Multiplication → Multiplication as Equal Groups → Multiplication: Arrays → Basic Multiplication Facts (0s, 1s, 2s, 5s, 10s) → Multiplication Facts Within 100 → Division as Equal Sharing → Division as Grouping (Measurement Division) → Division: Grouping (Repeated Subtraction) Model → Division: Fair Sharing Model → Division as Equal Sharing → Division as Grouping → Basic Division Facts → Division Facts Within 100 → Multiplication and Division Fact Families → Relationship Between Multiplication and Division → Division Facts as Inverse of Multiplication → Remainders and Quotients in Division → Division Word Problems → Multi-Step Word Problems → Solving Multi-Step Word Problems → Multiplication Word Problems → Division Word Problems → Introduction to Long Division → Factors and Multiples → Prime and Composite Numbers → Equivalent Fractions → Relating Fractions and Decimals → Decimal Place Value → Integers and the Number Line → Comparing and Ordering Integers → Absolute Value → Adding Integers → Subtracting Integers → Multiplying Integers → Dividing Integers → Unit Rates → Proportions → Percent Concept → Converting Between Fractions, Decimals, and Percents → Operations with Rational Numbers → Two-Step Equations → Solving Multi-Step Equations → Equations with Variables on Both Sides → Angle Pairs: Complementary, Supplementary, and Vertical → Parallel Lines and Transversals → Corresponding Angles → Alternate Interior Angles → Triangle Angle Sum Theorem → Exterior Angle Theorem → Triangle Inequality Theorem → Similar Triangles: AA Similarity → Similar Triangles: SSS and SAS Similarity → Proportions in Similar Triangles → Right Triangle Trigonometry Introduction → Sine, Cosine, and Tangent Ratios → Trigonometric Ratios Review → Radian Measure → Converting Between Degrees and Radians → The Unit Circle → Graphing Sine and Cosine → Graphing Tangent and Reciprocal Trigonometric Functions → Derivatives of Trigonometric Functions → Antiderivatives → Indefinite Integrals → Basic Integration Rules → Riemann Sums → Definite Integral Definition → Double Integrals: Definition and Setup → Iterated Integrals and Fubini's Theorem → Double Integrals over Rectangular Regions → Double Integrals over General Regions → Applications of Double Integrals: Area, Mass, and Moments → Center of Mass → Conservation of Linear Momentum → Elastic Collisions → Inelastic Collisions → Coefficient of Restitution → Collision Analysis and Real-World Applications → Two-Body Collisions in the Center-of-Mass Frame → Reduced Mass and Two-Body Problems → Kinematics in Two Dimensions → Projectile Motion → Circular Motion: Kinematics → Rotational Kinematics → Torque → Moment of Inertia → Rotational Kinetic Energy → The Work-Energy Theorem → Conservation of Mechanical Energy → First Law of Thermodynamics → Thermodynamic Processes and the PV Diagram → Intensive and Extensive Properties → State Variables and Functions → Path Functions versus State Functions → Types of Work: Mechanical PdV and Beyond → Polytropic Processes and the Polytropic Index → P-V Diagram Interpretation and Thermodynamic Processes → Boundary Work and P-V Diagrams → Reversible Adiabatic (Isentropic) Processes → Reversible Isothermal Expansion

Longest path: 118 steps · 667 total prerequisite topics

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