Seed-to-cake separation
Incoming seed silos → delint area → dehull aspirator (hulls go to separate silo) → cook + grind area → press hall (hot cake discharge to cooler/bagger). No crossing flows.
Industrial-scale cottonseed mill (50-100 t/d) integrates seed storage (silo 1500-5000 t for off-season feed), continuous delinting + dehulling, multi-press hot-pressing (5-10× 325 ton hydraulic, or screw press hybrid for higher continuous throughput), crude-oil buffer tanks (50-150 m³), and on-site NBD refining train 30-80 t/d (degum + neutralize + bleach + deodorize at 240-260°C). Yield 14-18% whole seed = 7-18 t crude oil/day. Output: refined edible cottonseed oil (free gossypol <0.045%) + decorticated meal (protein 41-44%) + hulls (feed/fuel) + linters (cellulose).
50-100 t/d module set
Layout rules
Incoming seed silos → delint area → dehull aspirator (hulls go to separate silo) → cook + grind area → press hall (hot cake discharge to cooler/bagger). No crossing flows.
Stagger press cycles 5-10 min apart so loading, oil collection, cake discharge happen continuously. Total floor 200-400 m² press hall, 5 m height clearance.
Crude-oil pumps + sample point + buffer tank between press and refining. Refining train footprint 100-200 m², stainless 304/316 contact, dedicated venting for deodorizer 240-260°C vapors.
Project boundary
50-100 t/d Cottonseed Mill | 5-10× Press, Refining + Hull Sale, Capex $300-600k 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.
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.