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Anhydrous ethanol — extractive distillation past the azeotrope (NRTL)

Extractive distillationAzeotropeNRTLAnhydrous ethanol
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Producing fuel-grade anhydrous ethanol from a near-azeotropic ethanol/water feed using ethylene glycol as the extractive entrainer. Ordinary distillation is capped at the 89.4 mol% ethanol azeotrope; the high-boiling glycol raises water's relative volatility so ethanol crosses its azeotrope and leaves the extractive column essentially pure, while a vacuum solvent-recovery column strips the water and recycles the glycol. This is modeled with the NRTL activity package on pinned DECHEMA binaries for every pair (ethanol/water, ethanol/glycol, water/glycol) — the non-ideal, azeotrope-crossing VLE a cubic equation of state structurally cannot reproduce (Peng-Robinson stays trapped at the ~89% azeotrope). Honesty note: NRTL binaries come from the bundled DECHEMA VLE Data Collection (via ChemSep/DWSIM), not fitted here; the solvent-recovery column runs under vacuum to keep the glycol below its decomposition temperature.

The flowsheet

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

FEED
Solvent
feed
dist
btms
ED
Ethanol
feed
dist
btms
SR
Water
Solvent Recovered

The stream table

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

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