Drying targets

Coconut pressing starts with a moisture number, not a machine

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

From 45-50% wet kernel to a window the press can hold

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.

  • Two press-ready windows exist: dried coconut meat at 10-12% for pressing soon after drying, and trade copra at 6-8% for the classic dry route.
  • Cool the dried meat before bagging; warm meat sweats inside the bag and climbs straight back above the window.
  • Uneven lots press unevenly - blend or re-dry mixed-moisture batches instead of averaging them on paper.

Intake checks

Accept copra with a meter, not with the seller's certificate

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.

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.

Smoke and mold

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.

Storage drift

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

Match dryer output to press rhythm before quoting either

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.

~350 kg/h
Dryer wet-feed rate
Desiccated coconut dryer reference, about 5 t/day.
~160 kg/h
Model 128 screw press
About 40% oil yield on dried coconut meat.
100 kg
Hydraulic barrel batch
Ø390×800 mm barrel, ~2 h per barrel cold, ~4.5 h for two.
~500 kg/24h
S600 refining reference
Crude-to-finished capacity that caps the daily plan.
Send drying and capacity data →

Storage control

Hold the window between dryer and press

  • Stack dried meat and copra off the floor, away from wash water, drains, and the wet residue exit.
  • Keep a moisture meter at the press infeed as well as the dryer outlet - the storage room is part of the process.
  • Old copra darkens the crude oil and raises refining loss, so date every lot and press the oldest first.
  • Log intake moisture, re-check moisture, and press date per lot; that record settles most oil-color disputes later.

Project boundary

What to confirm before scoping Copra Moisture and Drying Targets Before Pressing

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.

  • Confirm whether feed is whole seed, kernels, pretreated material, or an existing semi-finished stream.
  • Confirm whether the target is crude oil, filtered oil, bottled oil, drum ingredient oil, or a refining handoff.
  • Hot cycle reference: pure press 30-40 min/barrel, ~1.5 h for 2 barrels with loading; cold pure press ~2 h/barrel, ~4.5 h for 2 barrels.
  • Confirm batch rhythm, labor, changeover, retained samples, power (often 380V/50Hz/3ph), and site install conditions.

Factory model check

Match hot / cold models to factory hard data

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).

  • Standard barrel Ø390×800 mm, max ~100 kg crushed feed; optional Ø300 high-pressure barrel max ~60 kg.
  • Cylinder material 27SiMn; cold frames are integrated molded steel; hot frames are typically H-type channel steel.
  • Coconut may be VCO on 355–500 cold, or a complete multi-product line (325 milk + 128 screw + refine).
60 MPa
System pressure
High-low dual pump, ~60 MPa continuous
2.2 kW
Motor power
380V / 50Hz / 3 phase
300/325
Hot series
Pure press 30–40 min/barrel · ~1.5 h for 2 barrels
355–500
Cold series
370–630 ton · pure press ~2 h/barrel · ~4.5 h for 2 barrels

Equipment check

Preparation needs to land in equipment interfaces

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.

Front-end input

Record feed form, daily volume, moisture, and sorting needs so pretreatment is not left to operators.

Milk, drying, and refine interfaces

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.

Delivery data

Prepare space, power (often 380V/50Hz/3ph), labor, target package, local rules, and acceptance method before quotation.

Prepare pre-pricing data →

Questions on this page

What moisture should coconut feed reach before pressing?

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.

Can fresh kernel at 45-50% moisture be pressed directly?

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.

Does the dryer have to come from the same supplier as the press?

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

Keep planning your coconut project

Send measured moisture with your copra photos

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.

Shandong Shengshi Hecheng Machinery Co., Ltd.
No. 5888, Yineng Street, Development Zone, Qingzhou, 262500, Weifang, Shandong, China
+86 199 0636 5856
gavin@hydraulic-oil-press.com