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Renewable diesel & SAF: HEFA hydrotreating train

SAFHEFARenewable dieselHydrotreatingHydrodeoxygenation
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The HEFA (Hydroprocessed Esters and Fatty Acids) pathway to sustainable aviation fuel and renewable diesel from fats/oils/greases: a triglyceride feed (triolein) plus a large hydrogen excess is hydrodeoxygenated (HDO) to n-paraffins + propane + water, the paraffins are hydrocracked/isomerized toward the jet range, the H2-rich recycle gas and the HDO process water are knocked out, the light ends are stabilized, and a two-column fractionation splits the product into light naphtha, a jet-range SAF cut, and renewable-diesel bottoms. Honesty notes: the databank carries no lauric/oleic assay, so the FOG feed is modeled as triolein hydrodeoxygenating to n-octadecane (real HDO stoichiometry: triolein + 15 H2 -> 3 n-C18 + propane + 6 H2O); the hydrocracking lump (n-C18 -> n-C12 + n-C6) is illustrative, not a fitted kinetic network; and the n-/iso-paraffin distinction that actually sets the jet freeze-point spec is NOT resolved (the databank carries n-paraffins, not the specific branched isomers) — the train computes real material/energy balances and a real fractionation, not a validated freeze-point. A 3-phase water knockout is modeled as a component separator (the real unit gravity-decants the sour water).

The flowsheet

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

OIL
H2feed
MIX
HDO
HC
Hpsep
Recycle H2
Water KO
SOUR Water
Letdown
Lpsep
Offgas
feed
dist
btms
NAPH COL
Naphtha
feed
dist
btms
JET COL
SAF JET
Renewable Diesel

The stream table

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

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