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Wide-boiling column Process Flowsheets & Simulations

Explore 2 validated, solved Wide-boiling column simulation flowsheets in MaximaLabs — real components: methanol, dimethyl_ether, water, ethane, propane, n_butane. Open any one directly in your browser.

Solved via: PENG-ROBINSON.

FEED
RX
COOL
feed
dist
btms
Dmecol
feed
dist
btms
Meohcol
DME
Meohr
Water
Akola, India

DME synthesis (methanol dehydration)

Catalytic methanol dehydration (2 CH3OH -> (CH3)2O + H2O, 82% conversion) followed by two atmospheric-pressure columns: DMECOL rejects dimethyl ether overhead (~88% pure — the ternary's relative volatility at this pressure caps a single column's overhead purity there) via the inside-out method (a genuinely wide-boiling ternary — DME boils at -24 C, water at 100 C), then MEOHCOL recovers unconverted methanol (99.9% pure) from the water byproduct (99.3% pure). From the ChemSep casebook (DME_ie101583j).

8 unit ops • PENG-ROBINSON

17 0

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FEED
feed
dist
btms
DEC2
feed
dist
btms
DEC3
feed
dist
btms
DEC4
E C2
E C3
E C4
E C5
Mont Belvieu, Texas, USA

Light-ends fractionation train

A classic three-column light-ends train splitting an ethane/propane/ n-butane/n-pentane feed into four near-pure products: DEC2 (deethanizer, 5 bar) rejects ethane overhead, DEC3 (depropanizer, 5 bar) takes the propane cut, and DEC4 (debutanizer, 2 bar) splits n-butane from n-pentane. A genuinely wide-boiling train — DEC2 and DEC4 both land in the documented successive-substitution residual plateau (converge to a physically correct, sharp separation just above the strict 1e-5 tolerance) rather than a clean converged status, the same class of behavior already accepted for the DME casebook entry. From the ChemSep casebook (light-ends fractionation).

8 unit ops • PENG-ROBINSON

17 0

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