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NGL recovery Process Flowsheets & Simulations

Explore 3 validated, solved NGL recovery simulation flowsheets in MaximaLabs — real components: methane, ethane, propane, co2, n_butane, n2. Open any one directly in your browser.

Solved via: PENG-ROBINSON, GERG-2008.

Fast convergence
GAS
COMP
COOL
DRUM
Salesgas
NGL
Permian Basin, Texas, USA

Associated gas conditioning

Field gas is compressed, cooled, and flashed to knock out NGL/condensate — the sales-gas vs. liquids split every midstream gathering plant runs (Peng-Robinson).

6 unit ops • PENG-ROBINSON

17 0

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⭐ Featured
FEED
Chill
feed
dist
btms
Demeth
Residue GAS
NGL Product
NGL recovery plant, Permian Basin, Texas, USA

Deep ethane recovery with propane-refrigerated feed chilling

Associated gas is chilled by an external propane refrigeration package before a demethanizer recovers ethane and heavier as NGL bottoms from a methane-rich residue gas overhead — the cryogenic-chilling role Ortloff's CCS/GSP processes play ahead of the turboexpander in a real deep-ethane-recovery plant. The mechanical refrigeration loop itself (compressor/condenser/valve) isn't separately modeled here; the chiller's duty is represented directly as the feed's cooled outlet temperature (the same honest-simplification pattern used for LNG cold-box examples elsewhere in this library).

5 unit ops • PENG-ROBINSON

17 0

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NG
Chill
JT
SEP
Sales GAS
NGL
Gas processing plant, Permian Basin, Texas, USA

Cryogenic NGL recovery (GERG-2008 EoS)

A natural-gas dew-point-control / NGL knockout run on the GERG-2008 reference equation of state -- the multiparameter Helmholtz model the LNG and custody-transfer industries use because cubic EoS (Peng-Robinson/SRK) are off by several percent on cryogenic natural-gas density. Rich pipeline gas is chilled, let down across a Joule-Thomson valve into the two-phase region, and flashed cold to drop out an NGL liquid (propane/butane-rich) from the methane sales gas. The value is accuracy: on this flowsheet GERG predicts an NGL liquid density ~10% different from Peng-Robinson at cryogenic conditions -- enough to change vessel and exchanger sizing. Implemented via CoolProp's multiparameter Helmholtz mixture model (GERG-2008 binary reducing/departure functions), a validated implementation -- not a hand-transcription of GERG's thousands of coefficients. Scope: natural-gas / light-hydrocarbon components only (every species must be a CoolProp fluid); see flowsim/solver/thermo/gerg.py.

6 unit ops • GERG-2008

20 1

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