Process Engineering

Solvent Extraction of Soybean, Sunflower, and Canola Oils: Hexane Desolventising and Residue Limits

Step-by-step engineering analysis of continuous counter-current hexane extraction in oilseed processing: flake preparation, miscella distillation, and meal desolventising.

Author: Kiki's Technical Team•Published: 2026-10-09•5 min read
Edible Oil Solvent Extraction with Commercial n-Hexane
Continuous solvent extraction of vegetable oilseeds using high-purity commercial n-hexane in East African edible oil refinery plants.

Quick Answer — Solvent Extraction of Soybean, Sunflower, and Canola Oils: Hexane Desolventising and Residue Limits

Hexane solvent extraction recovers over 99% of vegetable oil from prepared oilseed flakes via counter-current washing, producing miscella that is vacuum-stripped to leave less than 1 ppm residual solvent in refined oil, while the meal is toasted in a DTDC tower for animal feed.

Solvent extraction in oilseed processing is the solid-liquid separation technique using non-polar hexane to dissolve neutral triglycerides from prepared seeds.

Key Facts

  • •Reduces residual meal oil from 8% down to less than 1.0%.
  • •Miscella contains 25% to 30% oil before falling film distillation.
  • •Refined cooking oil residual hexane strictly capped at < 1.0 ppm.
  • •Supplied to leading edible oil crushers in Kenya by KIKI'S.

Primary Use Cases

Soybean oil and high-protein meal productionSunflower seed oil commercial extractionCanola and cottonseed lipid processing

In East Africa's edible oil refining sector (processing sunflower, soybean, canola, and cottonseed in Nakuru, Nairobi, and Jinja), mechanical expeller pressing leaves 6% to 10% residual oil trapped within the press cake. Continuous solvent extraction using commercial n-hexane extracts over 99% of available lipids, reducing residual meal oil to under 1.0%.

The Extraction Cycle: Flaking, Percolation, and Miscella

Efficient solvent extraction relies on meticulous seed preparation and counter-current fluid mechanics:

  • Conditioning and Flaking: Cleaned seeds are cracked, heated to 60°C, and passed through smooth flaking rolls to create thin flakes (0.25 mm to 0.35 mm thick). Flaking ruptures cellular membranes, creating short diffusion pathways for the solvent.
  • Counter-Current Extraction: In rotary or belt extractors, fresh hexane washes the most exhausted meal, while concentrated miscella (hexane-oil mixture, 25% to 30% oil) percolates through incoming fresh flakes.
  • Miscella Evaporation: The liquid miscella is pumped through multi-stage falling film evaporators and a final vacuum stripping column where direct steam strips volatile hexane, yielding crude degummed vegetable oil.

Desolventiser-Toaster (DT) Operation and Meal Quality

Hexane-laden wet meal leaving the extractor contains approximately 30% solvent by weight. This meal enters the Desolventiser-Toaster (DTDC):

  • Indirect and Direct Steam Heating: Trays heated by steam evaporate volatile hexane. Direct sparge steam condenses into the meal, raising its moisture to 18-20% and driving out residual hydrocarbon traces.
  • Anti-Nutritional Factor Inactivation: In soybean processing, thermal toasting deactivates urease enzymes and trypsin inhibitors, rendering soybean meal digestible and safe for commercial livestock feed millers.

Residue Standards and Food Safety Compliance

Regulatory standards harmonised under KeBS and Codex Alimentarius mandate that refined edible vegetable oils contain less than 1.0 mg/kg (1 ppm) residual hexane. Properly calibrated solvent recovery systems routinely achieve residues below 0.1 ppm.

KIKI'S supplies oil millers with technical extraction grade n-Hexane possessing verified low boiling limits (<70°C) and non-volatile residues under 10 ppm, ensuring zero off-odours in refined oil.

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