PhysicsTHERM

Thermodynamics & Kinetic Theory of Gases

Apply concepts from Thermodynamics & Kinetic Theory of Gases to problem-solving. Focus on numerical practice and real-world applications.

2-3 Qs/year55 minPhase 2 · APPLICATION

Concept Core

Thermodynamics governs energy exchange between systems and their surroundings. The Zeroth Law establishes the concept of temperature: if system A is in thermal equilibrium with B, and B with C, then A is in thermal equilibrium with C.
The First Law is the energy conservation statement: Q = Δ\Delta-U + W, where Q is the heat absorbed by the system (J), Δ\Delta-U is the change in internal energy (J), and W is the work done by the system (J). All have dimensional formula [M1  L2  T2M^{1} \; L^{2} \; T^{-2}]. Sign convention (NEET standard): Q > 0 (heat absorbed), Q < 0 (heat released); W > 0 (expansion), W < 0 (compression); Δ\Delta-U > 0 (temperature rise).

Four thermodynamic processes define special conditions.
In an isothermal process (T = constant), Δ\Delta-U = 0 for an ideal gas, so Q = W = nRT ln(V2V1\frac{V_{2}}{V_{1}}), where n is moles, R = 8.314 J mol1  K1mol^{-1} \; K^{-1}, and PV = constant.
In an adiabatic process (Q = 0), W = -Δ\Delta-U = nC_v Δ\Delta-T = (P1  V1P_{1} \; V_{1} - P2  V2P_{2} \; V_{2})/(γ\gamma - 1); the governing relations are PV^γ\gamma = constant, TV^(γ\gamma-1) = constant. Adiabatic expansion cools the gas; compression heats it.
In an isochoric process (V = constant), W = 0, so Q = Δ\Delta-U = nC_v Δ\Delta-T; P/T = constant.
In an isobaric process (P = constant), W = P Δ\Delta-V = nR Δ\Delta-T, Q = nC_p Δ\Delta-T; V/T = constant. Work done in any process equals the area under the PV curve.

The Second Law has two equivalent statements. Kelvin-Planck: no engine can convert all absorbed heat into work (100% efficiency is impossible). Clausius: heat cannot spontaneously flow from cold to hot without external work.
The Carnot engine operates between a hot reservoir at T1T_{1} (K) and a cold reservoir at T2T_{2} (K) with maximum efficiency: η\eta = 1 - T2T1\frac{T_{2}}{T_{1}} = W/Q1Q_{1} = (Q1Q_{1} - Q2Q_{2})/Q1Q_{1}. Temperatures must be in kelvin; using Celsius gives wrong answers.
A refrigerator has COP = Q2Q_{2}/W = T2T_{2}/(T1T_{1} - T2T_{2}).

The kinetic theory of gases connects microscopic molecular motion to macroscopic properties.
The ideal gas equation PV = nRT = Nk_B T, where kBk_{B} = 1.38 x 102310^{-23} J/K is the Boltzmann constant.
Kinetic pressure: P = 13\frac{1}{3} ρ  vrms2\rho \; v_{rms}^{2} [M1  L1  T2M^{1} \; L^{-1} \; T^{-2}] (Pa).
Molecular speeds: vrmsv_{rms} = 3RT/M\sqrt{3RT/M} [M0  L1  T1M^{0} \; L^{1} \; T^{-1}] (m/s), vavgv_{avg} = 8RT/(πM\sqrt{8RT/(\pi M}), vmpv_{mp} = 2RT/M\sqrt{2RT/M}.
The ratio vmpv_{mp} : vavgv_{avg} : vrmsv_{rms} = 2\sqrt{2} : 8/π\sqrt{8/\pi} : 3\sqrt{3} = 1 : 1.128 : 1.224. The ordering vmpv_{mp} < vavgv_{avg} < vrmsv_{rms} is always maintained — most probable speed is the smallest.

Degrees of freedom (f): monoatomic gases (He, Ne, Ar) have f = 3 (translational only), diatomic (H2H_{2}, O2O_{2}, N2N_{2}) have f = 5 (3 translational + 2 rotational), polyatomic (CO2\text{CO}_{2}, H2OH_{2O}) have f = 6 (3 translational + 3 rotational).
By the law of equipartition, energy per degree of freedom = 12\frac{1}{2} kBk_{B} T per molecule = 12\frac{1}{2} RT per mole.
Internal energy U = (f/2)nRT.
Specific heats: CvC_{v} = (f/2)R, CpC_{p} = CvC_{v} + R = ((f+2)/2)R, and γ\gamma = CpCv\frac{C_{p}}{C_{v}} = (f+2)/f.
For monoatomic: CvC_{v} = 3R/2, CpC_{p} = 5R/2, γ\gamma = 53\frac{5}{3} = 1.67.
For diatomic: CvC_{v} = 5R/2, CpC_{p} = 7R/2, γ\gamma = 75\frac{7}{5} = 1.4.
For polyatomic: CvC_{v} = 3R, CpC_{p} = 4R, γ\gamma = 43\frac{4}{3} = 1.33.

Solved Numerical 1: Isothermal expansion at T = 300 K, n = 2 mol, V1V_{1} = 2 L, V2V_{2} = 6 L (R = 8.314 J mol1  K1mol^{-1} \; K^{-1}).
W = nRT ln(V2V1\frac{V_{2}}{V_{1}}) = 2 x 8.314 x 300 x ln(62\frac{6}{2}) = 2 x 8.314 x 300 x ln(3) = 4988.4 x 1.0986 = 5480 J.
Since isothermal: Δ\Delta-U = 0, Q = W = 5480 J.

Solved Numerical 2: Carnot engine: ThotT_{hot} = 527 degrees C = 527 + 273 = 800 K, TcoldT_{cold} = 127 degrees C = 127 + 273 = 400 K.
Efficiency: η\eta = 1 - T2T1\frac{T_{2}}{T_{1}} = 1 - 400800\frac{400}{800} = 0.5 = 50%.
If Q1Q_{1} = 2000 J: W = η  Q1\eta \; Q_{1} = 0.5 x 2000 = 1000 J.
Q2Q_{2} = Q1Q_{1} - W = 2000 - 1000 = 1000 J.
Dimensional check: all quantities in [J] = [M1  L2  T2M^{1} \; L^{2} \; T^{-2}].

Solved Numerical 3: Oxygen (M = 32 x 10310^{-3} kg/mol) at T = 300 K (R = 8.314 J mol1  K1mol^{-1} \; K^{-1}).
vrmsv_{rms} = 3RT/M\sqrt{3RT/M} = 3x8.314x300/0.032\sqrt{3 x 8.314 x 300 / 0.032} = 7481.3/0.032\sqrt{7481.3 / 0.032} = 233,790\sqrt{233,790} = 483.5 m/s.
vavgv_{avg} = 8RT/(πM\sqrt{8RT/(\pi M}) = 8x8.314x300/(πx0.032\sqrt{8 x 8.314 x 300 / (\pi x 0.032}) = 19,954/0.10053\sqrt{19,954 / 0.10053} = 198,480\sqrt{198,480} = 445.5 m/s.
vmpv_{mp} = 2RT/M\sqrt{2RT/M} = 2x8.314x300/0.032\sqrt{2 x 8.314 x 300 / 0.032} = 155,888\sqrt{155,888} = 394.8 m/s. Ratio check: 394.8 : 445.5 : 483.5 = 1 : 1.128 : 1.225.

The key testable concept is the distinction between thermodynamic processes (especially that Q = 0 in adiabatic does NOT mean Δ\Delta-U = 0 or T = constant) and the correct application of Carnot efficiency using kelvin temperatures.

Key Testable Concept

The key testable concept is the distinction between thermodynamic processes (especially that Q = 0 in adiabatic does NOT mean Delta-U = 0 or T = constant) and the correct application of Carnot efficiency using kelvin temperatures.

Comparison Tables

A) Thermodynamic Processes

ProcessConstant QuantityQWΔ\Delta-UKey EquationPV Curve Shape
Isothermal (T = const)TemperaturenRT ln(V2V1\frac{V_{2}}{V_{1}})nRT ln(V2V1\frac{V_{2}}{V_{1}})0PV = constRectangular hyperbola
Adiabatic (Q = 0)No heat exchange0-Δ\Delta-U = nC_v(T1T_{1}-T2T_{2})nC_v(T2T_{2}-T1T_{1})PV^γ\gamma = constSteeper than isothermal
Isochoric (V = const)VolumenC_v Δ\Delta-T0nC_v Δ\Delta-TP/T = constVertical line
Isobaric (P = const)PressurenC_p Δ\Delta-TP Δ\Delta-V = nR Δ\Delta-TnC_v Δ\Delta-TV/T = constHorizontal line

B) Carnot Engine vs Refrigerator

ParameterHeat EngineRefrigeratorFormula
PurposeConverts heat to workTransfers heat from cold to hot
Energy inputHeat Q1Q_{1} from hot reservoirWork W from external source
Efficiency / COPη\eta = W/Q1Q_{1} = 1 - T2T1\frac{T_{2}}{T_{1}}COP = Q2Q_{2}/W = T2T_{2}/(T1T_{1} - T2T_{2})η\eta < 1 always; COP can be > 1
OutputMechanical work WHeat Q1Q_{1} = Q2Q_{2} + W to hot reservoir
Ideal limitη\eta = 1 only if T2T_{2} = 0 K (impossible)COP = infinity if T1T_{1} = T2T_{2} (no work needed)

C) Molecular Speeds

Speed TypeFormulaPhysical MeaningRatio Factor
Most probable (vmpv_{mp})2RT/M\sqrt{2RT/M}Speed with maximum number of molecules1 (= 2\sqrt{2})
Mean / average (vavgv_{avg})8RT/(πM\sqrt{8RT/(\pi M})Arithmetic mean of all molecular speeds1.128 (= 8/π\sqrt{8/\pi})
RMS (vrmsv_{rms})3RT/M\sqrt{3RT/M}Root mean square; used in pressure formula1.224 (= 3\sqrt{3})
Ordervmpv_{mp} < vavgv_{avg} < vrmsv_{rms}Always: most probable is the smallest

D) Gas Type Properties

Gas Typef (DOF)CvC_{v}CpC_{p}γ\gamma = CpCv\frac{C_{p}}{C_{v}}Examples
Monoatomic33R/2 = 12.47 J/(mol K)5R/2 = 20.79 J/(mol K)53\frac{5}{3} = 1.67He, Ne, Ar
Diatomic55R/2 = 20.79 J/(mol K)7R/2 = 29.10 J/(mol K)75\frac{7}{5} = 1.40H2H_{2}, O2O_{2}, N2N_{2}
Polyatomic (nonlinear)63R = 24.94 J/(mol K)4R = 33.26 J/(mol K)43\frac{4}{3} = 1.33CO2\text{CO}_{2}, H2OH_{2O}

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