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Solvent recovery Process Flowsheets & Simulations

Explore 2 validated, solved Solvent recovery simulation flowsheets in MaximaLabs — real components: acetone, water, isopropanol, sulfolane. Open any one directly in your browser.

Solved via: NRTL.

FEED
feed
dist
btms
COL
Acetone
Water
Reference model (ChemSep)

Acetone–water distillation

A 12-stage column recovers acetone overhead from a dilute aqueous solvent-recovery feed — a common industrial acetone/solvent-recycling duty.

4 unit ops • NRTL

17 0

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Waste FEED
Sulfolane FEED
feed
dist
btms
Extcol
IPA Product
feed
dist
btms
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. Honesty note: the brief's original entrainer, DMSO, doesn't have a pinned NRTL isopropanol binary in this codebase's databank (only DMSO-water is pinned), so this uses sulfolane instead — a real, industrially-standard extractive/physical solvent with a genuine pinned NRTL isopropanol binary. At this stage count and solvent-to-feed ratio the entrainer effect is real but modest (overhead reaches ~82 mol% IPA, up from the 68% feed) — a sharper, near-anhydrous cut would need more stages/reflux or a higher solvent ratio than what this session verified converges reliably.

7 unit ops • NRTL

18 0

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