Delint: acid or saw
Acid delinter (H₂SO₄ 8-12% bath, 90-95% lint removal, capacity 2-10 t/h). Saw linter (mechanical, 70-85% removal, capacity 1-5 t/h, no chemical waste). Choose by capex + waste-disposal availability.
Cottonseed pretreatment hard data and module sequence: 1) Cleaning (vibrating screen + magnetic separator + destoner) to impurities <0.1%. 2) Delinting: acid (sulfuric 8-12% bath, 90-95% lint removal, fast) or saw linter (mechanical, 70-85% removal, no chemical). Linter 5-15% of seed → cellulose/cotton-pad market. 3) Dehulling (sheller + air aspirator): hull 35-45% of seed, kernel-rich feed for higher yield (28-35% on kernel vs 14-18% on whole seed). 4) Cooking 110-130°C × 30-60 min → moisture 8-12% → 6-8%, gossypol gland rupture. 5) Grinding/stirring 1-3 mm uniform feed to barrel.
Module specifications
Acid delinter (H₂SO₄ 8-12% bath, 90-95% lint removal, capacity 2-10 t/h). Saw linter (mechanical, 70-85% removal, capacity 1-5 t/h, no chemical waste). Choose by capex + waste-disposal availability.
Vibrating screen (40-100 mesh) + magnetic separator + destoner (gravity table). Capacity matches line throughput 1-10 t/h. Output: clean delinted seed, impurities <0.1%, stones <0.05%.
Sheller (drum or roll) + air aspirator separates hull (35-45% of seed) from kernel. Kernel-rich feed → 28-35% yield (vs 14-18% on whole seed). Hulls collected for ruminant feed/fuel/board.
Steam-jacketed cooker 110-130°C × 30-60 min (moisture 8-12% → 6-8%, gossypol gland rupture) + roll/hammer mill 1-3 mm + stirring tank for uniform feed to press barrel.
Common errors
Project boundary
Cottonseed Delinting + Dehulling | Linter 5-15%, Hull 35-45%, Acid vs Saw Linter should not be quoted from an equipment name alone. Check feed lots, target oil, post-press handling, and packing rhythm in one scope before deciding which Cottonseed Oil Press modules stay. Cottonseed is almost always 300/325 hot press + cook + mandatory refining (gossypol).
When feed condition, moisture, impurities, batch weight, and product position are unclear, press tonnage and filter area become guesswork. Factory systems share 60 MPa and 2.2 kW motors; hot pure press is 30–40 min/barrel and cold pure press is ~2 h/barrel — cycle time matters more than brochure tonnage.
Factory model check
Pin models to published factory specs before tonnage talk.
Hot 300/325: 300–325 ton, 60 MPa system, standard barrel Ø390×800 mm / max 100 kg, pure press 30–40 min/barrel, ~1.5 h for 2 barrels with loading, 2.2 kW motor. Cold 355/400/426/480/500: 370–630 ton, integrated frame, same 100 kg standard barrel, pure press ~2 h/barrel, ~4.5 h for 2 barrels with loading; optional Ø300 high-pressure barrel max 60 kg. Residual oil target ~≤5% (peanut hot often 6–8% measured).
Equipment check
Once the route is clear, write the interfaces: how preparation feeds the press, how oil leaves the press, how filtration connects to tanks, and how packing receives finished oil.
Record feed form, daily volume, moisture, and sorting needs so pretreatment is not left to operators.
Gossypol 0.5–2.5% makes alkali + bleach + deodorize mandatory. Leave piping and sample points for refining in the first layout.
Prepare space, power (often 380V/50Hz/3ph), labor, target package, local rules, and acceptance method before quotation.
Acid delinter (H₂SO₄ 8-12% bath): 90-95% lint removal, capacity 2-10 t/h, fast and complete. But requires acid handling + neutralization + waste-water treatment, raising capex 30-50% on the delinting section. Saw linter (mechanical): 70-85% removal, capacity 1-5 t/h, no chemical waste, lower capex. Choose acid for >50 t/d mills with waste infrastructure; saw linter for 10-30 t/d gin-side lines or where chemical handling is impractical.
Dehulling raises kernel-feed yield from 14-18% (whole seed) to 28-35% (kernel-only), nearly doubling oil output per ton of input. Cake protein rises from 23-28% (with hulls) to 41-44% (decorticated meal, premium ruminant feed price). Crude oil also lighter (less hull pigment), simplifying refining. Hulls 35-45% by weight sold separately as feed/fuel/board feedstock. Dehulling adds sheller + aspirator (~$15-30k capex for 30 t/d) but recovers in 6-12 months on yield + cake-protein premium.
Related guides
Compare hydraulic batch press vs continuous screw (expeller) for cottonseed: oil quality, cold-press ability, capacity, residual oil, labor, and when each route wins. Use this before you request a quote.
Size cottonseed hydraulic capacity with real cycles: hot pure press 30-40 min/barrel (~1.5 h for 2 barrels with loading); cold ~2 h pure / ~4.5 h for 2 barrels. Example math for 1–5 t/day small mills.
RFQ checklist for cottonseed hydraulic oil press projects: seed form, kg/shift, hot/cold, filtration, cake path, power, country, and photos. Incomplete inquiries get catalog replies — complete packs get model counts and line scope.
2026 factory price bands for cottonseed hydraulic presses: hot 300/325 about US$2000-5000, cold 355 about US$4000-7000, large cold 400–500 about US$8000-15000+. What drives the quote and how to compare offers.
Send feed condition, target output, post-press destination, and site constraints — we reply with a workable scope.