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Depropanizer (NGL fractionation)

Gas processingNGL fractionationDistillationDepropanizer
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The raw NGL recovered by a cold separator is fractionated: a depropanizer column splits it into a C3-and-lighter overhead (propane + a little ethane, the LPG product) and a C4+ bottoms (butanes + natural gasoline). The column is solved with the component-flow Naphtali-Sandholm MESH (method "ns"), which carries every component flow as an unknown so the feed-vs-products material balance is an equation the solver closes by construction — the right tool for a sharp C3/C4 cut, where a reduced-form column would drag the split off and leak a few percent of a component. Peng-Robinson handles the light-hydrocarbon VLE; the built-in sensitivity sweeps the reflux ratio against the reboiler duty (the classic distillation energy trade-off).

The flowsheet

The solved topology — every unit op's real duty, conversion, or split, read straight off a genuine converged solve.

NGL
feed
dist
btms
Deprop
C3prod
C4plus

The stream table

Every stream's flow, temperature, pressure, and composition — real converged numbers, not placeholders.

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