Hydraulic pressing: 200-325 ton press, 80-100 kg/barrel, 30-45 min cycle, yield 12-16% of bean weight, residual cake oil 6-8%, no solvent. Best for non-GMO, organic, specialty, pilot, regional <50 t/d. Solvent extraction (hexane): continuous, throughput 100-3000+ t/d, yield 18-22% (>95% of oil recovered), residual oil <1%, requires DT-DC + solvent recovery + flammable-area design. Capex 5-10× hydraulic. Hybrid: hydraulic pre-press + solvent extraction is standard for high-oil seeds (>30%), not used for soybean (oil only 18-22%).
200-325 ton press, 80-100 kg/barrel, 30-45 min/cycle, yield 12-16%, residual cake oil 6-8%, no solvent. Capex $50-150k for 5-30 t/d. Best for non-GMO/organic/specialty, label-friendly.
Continuous extractor + DT (desolventizer-toaster) + solvent recovery, hexane working solvent. Yield 18-22% (recovery >95%), residual oil <1%. Capex $1-10M for 100-3000 t/d. Mainstream commodity soy oil.
Below ~50 t/d: hydraulic dominates (small capex, batch control, no flammable area). Above ~100 t/d: solvent extraction wins on per-ton cost. Between 50-100 t/d: mechanical screw press + solvent extractor common compromise.
Hard-data comparison
Hydraulic: yield 12-16% bean weight (60-80% of total bean oil 18-22%), residual cake oil 6-8%. Solvent: yield 18-22% (recovery >95%), residual oil <1%. Solvent extracts 4-6 pt more oil per bean.
Hydraulic 5-30 t/d: $50-150k capex, no solvent, electricity + steam only. Solvent 100 t/d: $1-3M capex, hexane consumption 1-2 kg/t, fire/explosion area design (zone 1/2), continuous operation.
Hydraulic: 'mechanically pressed', non-GMO/organic-friendly, specialty retail, soybean meal protein 44% (with hull) or 48-50% (dehulled). Solvent: commodity refined oil + soybean meal 44% (most US/Brazil mainstream).
Decision criteria
Common errors
Keep the engineering path moving
Share feed condition, pretreatment depth, shift output, post-press destination, and utility limits. We use that to narrow the scope to the pressing section, clarification loop, and real factory boundary.