Moisture at intake
Sample across the lot; the top of the bag is not representative. Accept 6-8% for copra; send wetter lots back to the dryer before they enter storage.
Drying targets
Wet kernel at 45-50% moisture is not press feed. The dry route only becomes real when drying lands in a window the press can hold shift after shift.
Drying stages
Fresh kernel starts to ferment within hours in tropical heat, so drying is a same-day task, not a weekend job. Run it in two stages: a fast first stage that strips surface and free water, then a slower finishing stage so the center dries through without case-hardening the outside. For anything positioned as virgin, the whole chain stays at or below 60°C - one hot stage ends that positioning even if the press itself runs cold.
Intake checks
Bought-in copra is the biggest quality variable on the dry route. Whatever the trading paper says, the number that matters is measured at your own intake and again at the press infeed.
Sample across the lot; the top of the bag is not representative. Accept 6-8% for copra; send wetter lots back to the dryer before they enter storage.
Smoke-dried or moldy copra carries taint and color straight into the crude oil and raises refining loss. Grade it out of the edible route at the gate.
Copra accepted at 6-8% can drift past 9% after weeks in humid storage. Re-check before pressing and run first-in-first-out staging.
Capacity match
Drying shrinks the weight the press actually sees: 100 kg of wet kernel at 45-50% moisture becomes roughly 55-60 kg of press-ready meat. On the factory's coconut complete-line reference, the desiccated coconut dryer handles about 5 t/day (~350 kg wet feed per hour), which keeps one Model 128 screw section at ~160 kg/h fed with a workable buffer. Downstream, the S600 refining reference of ~500 kg per 24 hours defines how much crude oil the plant can actually finish each day.
Storage control
Project boundary
Copra Moisture and Drying Targets Before Pressing 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 Coconut Oil Press modules stay. Coconut may be VCO on 355–500 cold, or a complete multi-product line (325 milk + 128 screw + refine).
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.
Complete lines include water/milk (325CG-A), desiccated dryer, screw 128, and S600 refine. VCO keeps the full chain ≤60°C with warm-fill jars.
Prepare space, power (often 380V/50Hz/3ph), labor, target package, local rules, and acceptance method before quotation.
Dried coconut meat presses well at 10-12% when used soon after drying; trade copra for the dry route is accepted at 6-8%. After pressing, settling and filtration should bring oil moisture below 0.1% for stable storage.
Not on the dry route - it emulsifies and the cake will not release. Direct fresh processing belongs to the wet VCO route, where a hydraulic milk press (Model 325CG-A reference, ~80% milk extraction) presses milk first and oil is separated afterwards. That is a different equipment scope.
Not necessarily, but the hourly balance must hold: a ~5 t/day dryer roughly keeps one 160 kg/h screw section fed. If a dryer already exists on site, send its photos, heat source, and real hourly output with the project brief.
Related guides
Compare hydraulic batch press vs continuous screw (expeller) for coconut: oil quality, cold-press ability, capacity, residual oil, labor, and when each route wins. Use this before you request a quote.
Size coconut 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 coconut 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 coconut 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.
Intake moisture readings, drying method and heat source, daily wet-kernel volume, and storage room photos decide the dryer-press pairing and the quote boundary.