MaximaLabs
All examples
Simulation gallery

Ethanol-water column at 6 atm (SRK + MHV1)

DistillationGᴱ mixing ruleMHV1AzeotropeHigh pressure
See it live
Open this exact flowsheet in the workspace, already solved — tweak a spec and re-run.
Launch interactive model

The ethanol-water column everyone knows, run at 6 atm on the Gᴱ-mixing-rule package: Soave-Redlich-Kwong whose mixture energy parameter comes from NRTL's excess Gibbs energy through the MHV1 rule (Michelsen 1990) instead of a kij — the package built for polar, hydrogen-bonding mixtures at pressure, where a γ-φ activity model is past its ~10 bar ceiling and a plain cubic with van der Waals mixing has no hydrogen bonding at all. A 10 mol% ethanol feed through 16 stages at a reflux ratio of 2.5 gives a 66.7 mol% distillate and an ethanol-free bottoms, 2.6 MW on the reboiler. Read it against NRTL, which at 6 atm is still inside its own range: the two packages put the pressure-shifted azeotrope in different places — 0.88 mol fraction ethanol here, 0.84 on NRTL at 6 atm (0.97 against 0.89 at 1 atm) — so this card shows where the MHV1 rule sits, not a number to prefer over the fitted binary at low pressure. The cut is kept well short of the azeotrope on purpose: at a distillate ratio of 0.12 the profile pinched against it and the column reported exactly that. Each solve is about a minute, because every stage K-value is a Gᴱ mixing-rule evaluation.

The flowsheet

The solved topology — every unit op's real duty, conversion, or split, read straight off a genuine converged solve.

FEED
feed
dist
btms
Qc
Qr
COL
Distillate
Bottoms

The stream table

Every stream's flow, temperature, pressure, and composition — real converged numbers, not placeholders.

See it live
Open this exact flowsheet in the workspace, already solved — tweak a spec and re-run.
Launch interactive model

Stop fighting legacy software. Build your first flowsheet in 60 seconds.