Gas Mixture Thermodynamics and Dalton's Law

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mixtures daltons-law partial-pressure mole-fraction

Core Idea

For ideal gases, Dalton's law states total pressure P = Σ P_i (partial pressures), and mole fraction x_i = P_i/P. Mixture properties are molar averages: M_mix = Σ x_i*M_i, R_mix = R_u/M_mix, c_p,mix = Σ x_i*c_p,i. For real gases this becomes complex; mixing rules depend on the equation of state. Combustion, HVAC, and gas separation all rely on mixture thermodynamics.

Explainer

Your prerequisite on partial pressures established the central fact about ideal gas mixtures: each component behaves as if it were alone in the container, occupying the full volume at the temperature of the mixture. Dalton's law formalizes this as P_total = Σ P_i, where each partial pressure P_i = x_i × P_total is the pressure that component i would exert if it alone occupied the volume at the same temperature. The mole fraction x_i = n_i/n_total is the key composition variable — it is simultaneously the volume fraction and the partial-pressure fraction for ideal gases.

The mixture properties you need for thermodynamic calculations follow from treating the mixture as a single pure substance with molar-averaged properties. The mixture molecular weight M_mix = Σ x_i M_i is a straightforward molar average — heavier components pull it up, lighter ones pull it down. From M_mix you get the specific gas constant R_mix = R_u / M_mix (where R_u = 8.314 J/mol·K is the universal gas constant), which you can plug directly into the ideal gas law PV = m R_mix T to work in mass-based units. Similarly, the mixture heat capacity c_p,mix = Σ x_i c_p,i lets you compute enthalpy changes for the mixture just as you would for a pure gas. All of this works because ideal gas components do not interact — mixing them does not change their individual enthalpies, internal energies, or entropies beyond the entropy of mixing (which matters for chemical equilibrium but not for energy balances in most engineering calculations).

A practical example anchors the arithmetic. Dry air is approximately 21% O₂ and 79% N₂ by mole. The mixture molecular weight is M_air = 0.21×32 + 0.79×28 = 6.72 + 22.12 = 28.84 g/mol, giving R_air = 8314/28.84 ≈ 287 J/(kg·K) — the familiar specific gas constant for air. The partial pressure of O₂ at sea level (101.3 kPa) is 0.21 × 101.3 = 21.3 kPa. This is why oxygen partial pressure matters for aviation physiology and why altitude affects combustion — as you climb, P_total falls and with it P_O₂, reducing oxygen availability even though the mole fraction stays the same.

For real gas mixtures, the ideal treatment breaks down because intermolecular forces between unlike species differ from forces between like species, producing volume and enthalpy changes on mixing. Real gas equations of state like van der Waals or Peng-Robinson require mixing rules for their parameters — empirical or theoretically motivated formulas for the cross-interaction parameters a_ij (attraction) and b_ij (size). These are more involved and depend on the specific gas pair. For engineering work at moderate pressures (combustion products below ~10 bar, HVAC systems at atmospheric conditions), the ideal mixture treatment is accurate to within a few percent and is almost universally used. Real-gas corrections become important in natural gas pipelines at high pressure, supercritical processes, and precision measurements where small departures from ideality matter.

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 PropertiesThe Canonical Partition Function and Thermodynamic DerivationFree Energy and Thermodynamic Relations from Partition FunctionsPhase Transitions and Equilibrium Phase DiagramsSpontaneous Symmetry BreakingOrder Parameters and Phase TransitionsMean Field Theory and Self-ConsistencyVan der Waals Equation from Statistical MechanicsCritical Point and Supercritical Fluid BehaviorReal Gas Thermodynamics and Equations of StateCompressibility Factor and Generalized CorrelationsIdeal and Real Gas BehaviorGas Mixture Thermodynamics and Dalton's Law

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