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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
Qc
Qr
ED
Ethanol
feed
dist
btms
Qc
Qr
SR
Water
Solvent Recovered

The stream table

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

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