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NGL fractionation Process Flowsheets & Simulations

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

Solved via: PENG-ROBINSON.

FEED
feed
dist
btms
Demeth
Sales GAS
feed
dist
btms
Deeth
Ethane
feed
dist
btms
Deprop
Propane Product
feed
dist
btms
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
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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⭐ Featured
FEED
DWC
C2
C3
C4
Mont Belvieu NGL fractionation complex, Texas, USA

NGL fractionation: single-shell Petlyuk dividing-wall column

A natural-gas-liquids cut (ethane / propane / n-butane) split into three on-spec products by ONE thermally-coupled dividing-wall column instead of two columns in series. This uses the native Petlyuk unit op: a prefractionator whose reflux and boilup are supplied by the main column (the single condenser + single reboiler), solved by an outer Wegstein loop that converges the bidirectional vapor/liquid coupling to self-consistency — the coupling legacy sequential-modular solvers approximate with two connected columns whose recycle fails to converge. Honesty note: the vapor-split and liquid-split ratios are specified inputs (not solved from tray hydraulics), and this is an outer-loop coupling of two rigorous MESH sub-solves, not a single monolithic Petlyuk MESH.

5 unit ops • PENG-ROBINSON

18 0

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