First Law of Thermodynamics for Closed Systems

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first-law energy-balance closed-systems

Core Idea

The first law for a closed system states that energy change equals heat added minus work done by the system: ΔU = Q - W. This energy balance applies to any system undergoing any process and is the foundation for analyzing turbines, compressors, and heat exchangers with fixed mass. Identifying all forms of work (boundary, shaft) and heat transfer is critical to correct application.

How It's Best Learned

Write the first law ΔU = Q - W for various processes (isothermal, isobaric, isochoric) and identify which terms vanish. Practice calculating work for boundary-displacement processes (W = ∫P dV) and recognize that polytropic processes (PVⁿ = const) are common idealizations. Always draw the system boundary clearly and identify work and heat at the boundary.

Common Misconceptions

Explainer

The first law of thermodynamics for a closed system is an energy balance: the change in a system's internal energy equals the heat transferred into the system minus the work done by the system. Written compactly: ΔU = Q − W. This single equation governs steam engines, refrigerators, internal combustion engines, and any other device where a fixed mass of working fluid absorbs or releases energy.

A closed system has fixed mass — no matter crosses the boundary — but energy can cross as heat or work. The system boundary is a conceptual surface you draw around the substance of interest. Heat Q is energy transfer driven by a temperature difference across that boundary; it is positive when flowing in. Work W is energy transfer through mechanical interaction (a moving piston, a rotating shaft); it is positive when the system does work on the surroundings. Getting the sign convention right and drawing a clear boundary before writing any equations prevents most first-law errors.

The most important thing to understand about internal energy U is that it is a state function: it depends only on the thermodynamic state (characterized by properties like temperature and pressure), not on how the system arrived at that state. This means ΔU = U_final − U_initial, full stop — the path does not matter. Contrast this with Q and W individually, which are path-dependent. A slow isothermal compression and a fast irreversible compression between the same two states will have different Q and different W, but the same ΔU. This is why the first law is so powerful: even when you do not know the details of a process, you can compute ΔU from any convenient path.

For boundary work in a simple compressible system, W = ∫P dV. Three process types are especially common: isochoric (constant volume, dV = 0, so W = 0 and ΔU = Q), isobaric (constant pressure, W = PΔV), and isothermal (constant temperature, ΔU = 0 for an ideal gas, so Q = W). The polytropic process PVⁿ = constant generalizes all three: n = 0 is isobaric, n = 1 is isothermal for ideal gases, n = γ is adiabatic (no heat transfer), and n → ∞ is isochoric. Recognizing which process applies tells you immediately which terms in ΔU = Q − W are zero or simplified, making the calculation tractable.

Practice Questions 3 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 EnergyWork-Energy Principle for ParticlesWork-Energy Methods for SystemsWork-Energy Methods for Rigid BodiesPotential Energy and Conservative ForcesConservation of Mechanical Energy in SystemsFirst Law of Thermodynamics for Closed Systems

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