Oleochemicals Process Flowsheets & Simulations
Explore 4 validated, solved Oleochemicals simulation flowsheets in MaximaLabs — real components: triolein_ooo, tripalmitin_ppp, methanol, methyl_oleate, methyl_palmitate, glycerol. Open any one directly in your browser.
Solved via: PENG-ROBINSON.
Biodiesel: alkali-catalysed transesterification with methanol recovery
Continuous base-catalysed (NaOH/methoxide) transesterification of a refined vegetable oil to fatty acid methyl esters — the classic FAME biodiesel process. The oil is modeled as a 70/30 triolein/tripalmitin blend (the C₁₈:1 and C₁₆:0 triglycerides that dominate soy, canola and rendered-fat feedstocks); each is transesterified with methanol at a 6:1 molar ratio and 60 C in a two-reactor cascade at 97% conversion per stage, the standard industrial staging that drives the equilibrium toward the esters. Excess methanol is then vacuum-flashed overhead for recycle, and the wash/settling step splits the heavy glycerol phase from the ester product. The FAME product comes out at 96.9 wt% ester content — just over the EN 14214 minimum of 96.5 wt% — and the crude glycerin at ~85 wt% glycerol, typical of the crude co-product that goes on to a glycerin refining column.
8 unit ops • PENG-ROBINSON
117 0
View & openFat splitting: fatty acids from palm kernel oil
Continuous high-pressure countercurrent fat splitting (Colgate-Emery process): triglyceride oil hydrolyzed with excess water at ~260 C / 55 bar to free fatty acids plus glycerol. The databank has no lauric/myristic acid or their triglycerides (palm kernel oil's actual dominant fatty acids), so the feed is modeled as tripalmitin/triolein hydrolyzing to palmitic/oleic acid instead — the same reaction chemistry and process conditions, a different (available) fatty-acid slate. The real unit gravity-settles the fatty-acid and glycerol-water phases downstream; that decanting step is not modeled here (scope note), so the product stream is the full reactor effluent.
6 unit ops • PENG-ROBINSON
223 0
View & openFatty alcohols from methyl ester hydrogenolysis
High-pressure hydrogenolysis of a fatty acid methyl ester over a copper-chromite catalyst to the corresponding fatty alcohol plus methanol byproduct, the route used by natural-fatty-alcohol producers such as Oxiteno. Modeled with methyl palmitate as the ester feed (the C₁₆ member of the coconut/palm-kernel-derived ester slate these plants actually run); a flash removes unreacted hydrogen for recycle and a partial-condenser column recovers methanol overhead from the crude fatty alcohol. The column runs a vapor distillate because the flash liquid still carries dissolved hydrogen, and its distillate rate is set to the feed's light-component fraction — ask for more overhead than there is light material and the column can only meet the spec by dragging fatty alcohol up with it.
9 unit ops • PENG-ROBINSON
225 0
View & openFatty-ester vacuum fractionation
Biodiesel methyl esters (C₁₆ / C₁₈) split at 0.05 bar — vacuum keeps the bottoms under 515 K; near-total C₁₆ recovery overhead and ~98% C₁₈ in the bottoms (the two components' relative volatility caps bottoms purity there — more stages/reflux do not push it further). From the ChemSep casebook (Fatty_Acids, as methyl esters).
4 unit ops • PENG-ROBINSON
221 0
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