MaximaLabs
Back to gallery

Acetic acid Process Flowsheets & Simulations

Explore 3 validated, solved Acetic acid simulation flowsheets in MaximaLabs — real components: methanol, carbon_monoxide, acetic_acid, water, diisobutyl_ketone. Open any one directly in your browser.

Solved via: PENG-ROBINSON, NRTL-ASSOCIATE.

MEOH FEED
CO FEED
MIX
RX
Flash
CO VENT
feed
dist
btms
COL
Methanol Recycle
Acetic ACID Product
Acetic acid plant, Texas City, Texas, USA

Acetic acid via methanol carbonylation (Cativa process)

Methanol carbonylated with CO to acetic acid over the iridium-based Cativa catalyst (BP Chemicals), which runs at higher selectivity and lower water content than the older Monsanto rhodium process. The homogeneous catalyst itself isn't a flowing component in this model -- only the carbonylation stoichiometry and downstream light-ends recovery are represented. Unreacted CO is flashed off and a column strips residual methanol from the acetic acid product.

9 unit ops • PENG-ROBINSON

17 0

View & open
FEED
Solvent
feed
dist
btms
ED
Water Product
feed
dist
btms
SR
Acetic ACID Product
Solvent Recovered
Terephthalic acid plant, Map Ta Phut, Thailand

Dilute acetic acid recovery by extractive distillation

Recovering acetic acid from a dilute aqueous stream (e.g. cellulose acetate or terephthalic acid plant wastewater) using diisobutyl ketone (DIBK) as an extractive entrainer. Because acetic acid and water form no azeotrope but have a relative volatility that flattens toward 1 as the mixture concentrates, straight distillation needs an impractically tall column and heavy reboil duty; the entrainer raises water's relative volatility so the extractive column takes water overhead in far fewer stages, and a second column then strips the entrainer from the acid bottoms for recycle.

7 unit ops • PENG-ROBINSON

17 0

View & open
FEED
feed
dist
btms
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%) to a 99.8% acetic-acid bottoms product 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. Honesty note: acetic acid and water are close-boiling with no azeotrope, so the water distillate is only ~87% water (the acid product is the concentrated, high-purity stream); a sharper water cut needs more stages / reflux than this screening case uses.

4 unit ops • NRTL-ASSOCIATE

18 0

View & open

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