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Physics HL · Chapter 9: The Gas Laws

9.3 Equation of State and Gas Transformations

Unify empirical gas laws into $PV = nRT$ and apply process-specific relationships with disciplined variable control.

Estimated time: 32 minutes

From Empirical Laws to a Single Unified Law

Boyle's law gives P1/VP \propto 1/V at fixed nn and TT. Charles' law gives VTV \propto T at fixed nn and PP. Gay-Lussac's law gives PTP \propto T at fixed nn and VV. These are not separate universes; they are constrained slices through one higher-dimensional state surface.

A good mental model is to treat gas state as a point in (P,V,T,n)(P, V, T, n) space. Each named law freezes two variables and examines how one responds to another. The equation of state stitches those projections into one compact expression that remains valid whenever ideal assumptions hold.

Equation of State in Mole and Particle Form

PV=nRT,PV=NkBT,P1V1T1=P2V2T2 (fixed n)PV = nRT,\qquad PV = Nk_B T,\qquad \frac{P_1V_1}{T_1}=\frac{P_2V_2}{T_2}\text{ (fixed }n\text{)}

Use nRT form when quantity is given in moles and Nk_B T form when particle count is explicit.

RR and kBk_B are linked by R=NAkBR = N_A k_B, so the two forms encode the same physics at different counting scales. The first is convenient for laboratory mass/mole data. The second emphasizes microscopic particle-energy interpretation and is often cleaner in kinetic-theory derivations.

Remember that the ratio formula P1V1T1=P2V2T2\frac{P_1V_1}{T_1} = \frac{P_2V_2}{T_2} is not an independent law. It is an algebraic consequence of PV=nRTPV = nRT under fixed nn. This matters because if nn changes (for example valve opening, leaks, or injected gas), the ratio form is no longer valid unless you include the amount change explicitly.

Process Maps and Multi-Step Problem Solving

  • List known and unknown values with units first (PP, VV, TT, nn).
  • Convert all temperatures to kelvin before substitution.
  • Decide whether nn is constant; if not, avoid fixed-nn ratio shortcuts.
  • For multi-step paths, solve each process stage separately and pass final state forward.
  • Do a trend check: compressed gas at fixed TT should have higher PP, not lower.

The process-map approach is especially useful when problems mix constraints. A gas may first be heated at fixed volume, then expanded at fixed temperature. Solving each leg separately with clear state labels prevents equation misuse and mirrors how real thermodynamic cycles are analyzed.

Another reliability check is dimensional sanity. If you use SI pressure (Pa\text{Pa}) and SI volume (m3\text{m}^3), then nRTnRT naturally produces joules on the right and pascal-cubic-meter on the left, which are equivalent. If units do not reconcile cleanly, a conversion is missing.

Simulation: Switching Between Boyle, Charles, and Gay-Lussac Views

Toggle process modes and verify that each special law is a constrained slice of PV=nRTPV = nRT.

Ideal Gas Law Lab

Active law interpretation

Charles mode keeps n and P fixed, so volume scales linearly with kelvin temperature (V/T = constant).

Container micro-view (animated gas particles + piston)

Volume: 17.38 LPressure: 190.9 kPaTemperature: 420.0 K

P-V map with isotherms

V (L)P (kPa)

State diagnostics

P

190.9 kPa

1.88 atm

T

420.0 K

146.9 deg C

V

17.38 L

0.0174 m^3

Pressure index12%
Thermal index46%
Volume fraction40%

Microscopic metrics

RMS speed c_rms: 572.2 m s^-1

Mean molecular kinetic energy: 8.698e-21 J

Density estimate: 1.749 kg m^-3

Monatomic internal energy estimate: 4975.9 J

Model validity note

Ideal-model range: this state is in a typical low-density, moderate-temperature regime where PV = nRT is usually reliable.

Try this workflow: hold n fixed, then switch between Boyle/Charles/Gay-Lussac modes and verify each ratio form before returning to full-state PV = nRT checks.

Test Yourself

An ideal gas has n=0.25moln = 0.25\,\text{mol}, T=300KT = 300\,\text{K}, and V=6.20×103m3V = 6.20 \times 10^{-3}\,\text{m}^3. Enter the pressure in pascals.

Hint: Use PV=nRTPV = nRT with R=8.31J mol1K1R = 8.31\,\text{J mol}^{-1}\text{K}^{-1}.