(P + a/V²)(V − b) = RT introduces molecular size (excluded volume b) and attractive forces (a parameter) to ideal gas law, predicting real gas behavior near condensation. Higher virial coefficients and compressibility factors Z extend this to even better accuracy. These corrections explain why gases liquefy and why critical phenomena (critical point, law of rectilinear diameters) occur.
Calculate compressibility factors for CO₂ near critical point using van der Waals vs. ideal gas law; measure or look up a and b parameters from literature; plot isotherms and identify critical behavior; relate a to intermolecular attractions and b to molecular size.
You already know from your introduction to real gases that the ideal gas law, PV = nRT, breaks down when molecules are close together — at high pressures and low temperatures. The van der Waals equation was your first correction: (P + a/V²)(V − b) = RT (per mole). Now we dig deeper into what these corrections actually mean physically and where the equation succeeds and fails. The parameter b represents the excluded volume — the space physically occupied by the molecules themselves. Think of it this way: if you have a box of tennis balls, the gas molecules can only move in the space between the balls, not through them. This makes the effective volume smaller than the container volume, so V becomes V − b. The parameter a captures the average attractive force between molecules: in a real gas, molecules pulling on each other slightly reduce the pressure compared to what you'd expect from ideal behavior, so the measured pressure is P_ideal − a/V².
The most revealing way to see where the van der Waals equation works and fails is through the compressibility factor Z = PV/(nRT). For an ideal gas, Z = 1 everywhere. For a real gas, Z deviates: at moderate pressures, attractive forces dominate and Z < 1 (the gas is more compressible than ideal), while at very high pressures, excluded volume dominates and Z > 1 (the gas resists compression more than ideal). If you plot van der Waals isotherms (P vs. V at constant T), something dramatic happens below the critical temperature: the isotherms develop an S-shaped wiggle, predicting that pressure would decrease as volume decreases — a physically impossible region. This unphysical loop (called the van der Waals loop) is replaced in reality by a horizontal tie line representing the liquid-gas phase transition, determined by the Maxwell equal-area construction.
The critical point is where the van der Waals equation makes its most elegant prediction. At the critical temperature and pressure, the distinction between liquid and gas vanishes. The van der Waals equation predicts critical constants in terms of a and b: T_c = 8a/(27Rb), P_c = a/(27b²), V_c = 3b. This gives a universal critical compressibility factor Z_c = P_cV_c/(RT_c) = 3/8 = 0.375 for all gases — a prediction of the law of corresponding states, which says that all gases behave similarly when expressed in reduced variables (P/P_c, V/V_c, T/T_c). Real gases have Z_c values ranging from about 0.23 to 0.29, so the van der Waals prediction is qualitatively right but quantitatively off.
For higher accuracy, you need more sophisticated equations of state. The virial expansion Z = 1 + B'/V + C'/V² + … systematically adds correction terms, where each virial coefficient captures interactions between pairs, triples, and higher-order clusters of molecules. The second virial coefficient B' is directly related to the intermolecular potential energy function — connecting macroscopic gas behavior to the microscopic forces you studied in your prerequisite on intermolecular potentials. The van der Waals equation can be recast as a truncated virial expansion, revealing that it captures pairwise interactions but neglects higher-order terms. For engineering applications, more flexible equations like the Redlich-Kwong, Peng-Robinson, or multi-parameter correlations provide the quantitative accuracy that van der Waals sacrifices for conceptual clarity.