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Distillation train Process Flowsheets & Simulations

Explore 3 validated, solved Distillation train simulation flowsheets in MaximaLabs — real components: methane, ethane, propane, n_butane, n_pentane, benzene. Open any one directly in your browser.

Solved via: PENG-ROBINSON.

FEED
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Demeth
Sales GAS
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Deeth
Ethane
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Deprop
Propane Product
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Debut
Butane Product
Pentane PLUS
Gas plant, Permian Basin, Texas, USA

Natural gas fractionation train

A four-column NGL fractionation train — demethanizer, deethanizer, depropanizer, debutanizer — recovering pipeline-spec sales gas plus ethane, propane, and butane products from wellhead-pressure raw natural gas, after Luyben (Ind. Eng. Chem. Res. 2013, 52, 10741).

10 unit ops • PENG-ROBINSON

17 0

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FEED
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BENZ
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TOLU
B
T
X
Aromatics complex, Ulsan, South Korea

BTX aromatics train

Benzene / toluene / p-xylene split in a two-column train — 99+% purity on all three products. From the ChemSep casebook (CScasebook_BTX).

6 unit ops • PENG-ROBINSON

18 0

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FEED
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dist
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DEC2
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DEC3
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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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