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Vapor re-compression propane/propylene splitter

Heat pumpVapor recompressionPolymer-grade propyleneDistillation
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Propylene/propane splitters have a notoriously low relative volatility (~1.1-1.15), so they run at high reflux and benefit from heat pumping: the overhead vapor is compressed and used to reboil the same column at a lower operating pressure (here 12 bar vs. a conventional ~20 bar), cutting the compressor shell cost (Christopher et al., Ind. Eng. Chem. Res. 56, 14557, 2017). The reboiler heat-integration loop itself is not modeled here (that would need a recycle-coupled duty match) — this shows the column plus the overhead compression/condensing train, a bounded simplification.

The flowsheet

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

FEED
feed
dist
btms
COL
COMP
COND
Propylene
Propane

The stream table

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

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