MaximaLabs
Back to gallery

NRTL Process Flowsheets & Simulations

Explore 3 validated, solved NRTL simulation flowsheets in MaximaLabs — real components: isopropanol, water, sulfolane, acetic_acid, ethanol, ethylene_glycol. Open any one directly in your browser.

Solved via: NRTL, NRTL-ASSOCIATE.

Waste FEED
Sulfolane FEED
feed
dist
btms
Qc
Qr
Extcol
IPA Product
feed
dist
btms
Qc
Qr
Stripper
Water OVHD
Sulfolane Recovered
Puerto Rico (pharmaceutical manufacturing corridor)

Waste solvent recovery — extractive distillation (IPA/water)

A pharmaceutical waste isopropanol/water stream (near the ~68 mol% IPA azeotrope) is fed to an extractive column with a high-boiling entrainer feeding in a few stages above it; a second column strips the entrainer back out of the bottoms for reuse.

7 unit ops • NRTL

230 0

View & open
FEED
feed
dist
btms
Qc
Qr
COL
Water
ACID
Terephthalic-acid / cellulose-acetate plant, Map Ta Phut, Thailand

Acetic acid recovery — NRTL with vapor-phase dimerization

Concentrating dilute aqueous acetic acid (30 mol%) by distillation, modeled with the NRTL activity package and chemical-theory vapor-phase association (acetic acid dimerizes, 2 A → A2, in the vapor). This is the physics a cubic equation of state gets wrong: the pinned NRTL acetic-acid/water binary (DECHEMA) plus the cited dimerization constants (Nagy et al., Molecules 2020) give the real bubble curve and latent heat, so the close-boiling acid/water pair actually separates and converges where Peng-Robinson does not.

4 unit ops • NRTL-ASSOCIATE

228 0

View & open
FEED
Solvent
feed
dist
btms
Qc
Qr
ED
Ethanol
feed
dist
btms
Qc
Qr
SR
Water
Solvent Recovered
Fuel-ethanol dehydration unit, Pekin, Illinois, USA

Anhydrous ethanol — extractive distillation past the azeotrope (NRTL)

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).

7 unit ops • NRTL

228 0

View & open

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