The McCabe-Thiele method is a graphical technique used to determine the number of theoretical stages required for a separation process. In gas stripping, a soluble component is transferred from a liquid solution into a gas stream by repeatedly contacting the two phases. The method uses an equilibrium curve and an operating line to visualize the change in gas- and liquid-phase compositions from one ideal stage to another. It commonly assumes equilibrium stages, constant solute-free gas and liquid flow rates, and steady-state operation.
✅ What it can do:
Estimate the number of ideal equilibrium stages.
Visualize the equilibrium curve and operating line.
Evaluate the effects of stripping-gas flow rate, inlet and outlet compositions, and Murphree efficiency.
Show graphical “stepping” between the equilibrium and operating lines.
Determine stage-by-stage gas- and liquid-phase compositions.
❌ What it cannot do:
Accurately predict the actual number of stages without correcting for stage efficiency.
Reliably handle strongly nonlinear equilibrium relationships or large changes in gas and liquid flow rates.
Account for heat effects, pressure drop, mass-transfer resistance, or hydraulic limitations.
Replace rigorous rate-based simulations used in professional process simulators.
Below is an interactive simulator that allows you to experiment with the McCabe-Thiele method. You can:
Adjust the inlet and outlet gas and liquid compositions.
Modify the stripping-gas flow rate or gas-to-liquid ratio.
Apply Murphree efficiency to represent non-ideal stage behavior.
Choose between a linear equilibrium relationship and a custom equilibrium dataset.
Use it to visualize how design parameters affect stripper performance—great for learning and quick estimation!
Last edited: July 10, 2026