Ethanol–Water · NRTL · 101.325 kPaEthanol–water interactive vapour–liquid equilibrium

Move the parameters on the left and every phase diagram, excess property and column design is recomputed instantly. Model: modified Raoult's law + NRTL; validation data: Kamihama et al. (2012), 21 points.

Azeotrope (NRTL, current pressure)
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Deviation from experiment (101.3 kPa, 21 points)
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Heat of mixing ΔHmix (Tref)
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Minimum reflux Rmin (specification on the column tab)
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T–x–y diagram

y–x diagram

Separation is possible above the diagonal; where the curve crosses the diagonal is the azeotrope

Close-up near the azeotrope

x1 = 0.65–1; error bars are the expanded experimental uncertainty

Relative volatility α12

Along the bubble line, log scale; at α12 = 1 no further separation is possible

Method: the bubble temperature of each liquid composition is solved with the Illinois method; the excess enthalpy comes from numerical differentiation of GE/RT (Gibbs–Helmholtz); McCabe–Thiele assumes constant molar overflow, a saturated-liquid feed of 100 kmol/h and a total condenser; the reboiler duty uses the heat of vaporization of water, 40.65 kJ/mol. Code and report: github.com/Shuruyue/Ethanol-Water-VLE.