Peanut · 325 hot / 355–500 cold · yield 45–55%

Most peanut projects don't fail on press tonnage — they fail on feed, route, and aflatoxin control

Before comparing a 300-ton against a 500-ton hydraulic press, lock three things: feed form (pods or kernels), route (hot 80-100°C or cold ≤60°C), and aflatoxin discipline (B1 <20 μg/kg). This guide walks the full peanut line on real parameters.

A peanut hydraulic oil press process guide built on real numbers: kernel oil 44-56%, hot press 80-100°C (yield 40-48%), cold press ≤60°C (yield 35-42%), aflatoxin B1 <20 μg/kg, batch 100 kg/barrel, 200-300 mesh filtration.

Feed condition

Pods, shelled kernels, and graded kernels carry different preparation, cleaning, and handling assumptions.

Pressing route

Hot pressing needs a clear roasting window and loading rhythm; lower-temperature positioning needs cleaner kernels and tighter post-press handling.

Post-press handoff

Crude oil may move to pneumatic filtration, settling, buffer storage, or later refining, while cake handling should be planned beside the press.

Feed prep video00:19

Peanut shelling and cleaning before pressing

Use this clip to confirm whether shelling and cleaning belong in the current phase before sizing the press room.

Peanut pressing process routeProcess path

Feed, pressing, filtration, and peanut cake in one route

Keep pods or kernels, hot or lower-temperature route, crude-oil filtration, and cake flow on one project path.

Decide first

Pick the route before the machine — here's the quick read

The hot route and cold route are not two settings on one machine. They use different press classes, run different cycle times, and serve different markets. Choose the lane first.

Bulk edible oil → Hot route

Roast 160-180°C, press 80-100°C on a 300-325 ton hydraulic press. Oil yield 40-48%, residual oil 6-8%, cycle 30-40 min per 100 kg barrel. Highest throughput per hour.

Premium bottled brand → Cold route

Press at ≤60°C on a 355-500 ton hydraulic press. Oil yield 35-42%, residual oil 8-10%, cycle 60-90 min per barrel. Unrefined smoke point ~160°C — premium positioning, lower throughput.

Still have pods? → Shelling first

Shells are 30-40% of pod weight and contain no oil. Hydraulic pressing works only on shelled kernels. If you start from pods, shelling and a shell-disposal plan must be in scope.

Step by step

The peanut line from raw material to filtered crude oil

Step 1

1 · Shell, clean, and grade

Remove stones, metal, and stalks. Shell pods (shell 30-40% of weight). Grade kernels by size for uniform pressing. Reject moldy or damaged kernels — aflatoxin concentrates in damaged tissue.

Step 2

2 · Set moisture to 5-8%

Optimal pressing moisture is 5-8%. Above 10% causes low yield and mold risk; below 4% causes excessive friction and brittle cake. Test moisture every batch.

Step 3

3 · Roast (hot) or warm gently (cold)

Hot route: roast 160-180°C in flat-bottomed woks or drum roasters until moisture drops to 3-5% and color turns golden. Cold route: warm ≤60°C or crush at ambient. Record roast temperature per batch.

Step 4

4 · Load the hydraulic press by a fixed rule

Standard barrel 390 × 800 mm holds ~100 kg; model 325 uses 14 partitions. Hot cycle 30-40 min, cold cycle 60-90 min. System pressure 60 MPa, 2.2 kW motor — the same hydraulics across the range; only frame strength and pressure stability differ.

Step 5

5 · Filter crude oil immediately

Plate-frame filtration at 200-300 mesh right after pressing. Crude oil clarity target: sediment ≤0.1%, moisture ≤0.2%. Filtering warm oil promptly avoids sediment settling and flavor drift.

Key parameters

Real peanut numbers to size the line

Every figure below comes from the production spec, not a generic catalog. Use them to sanity-check any quote.

44-56%
Kernel oil content
Shelled kernels; shell is 30-40% of pod weight and oil-free.
40-48%
Hot-press oil yield
Press 80-100°C, residual oil in cake 6-8%.
35-42%
Cold-press oil yield
Press ≤60°C, residual oil 8-10%, premium route.
100 kg
Batch per barrel
Barrel 390 × 800 mm; hot cycle 30-40 min, cold 60-90 min.
45-50%
Cake protein
Feed ingredient or defatted food-grade flour (60-80 mesh).
<20 μg/kg
Aflatoxin B1 limit
EU <20 μg/kg, US FDA <20 ppb. Test every batch.

Avoid rework

Mistakes the press gets blamed for — but that belong upstream

Real line

Hot peanut roasting and hydraulic pressing rhythm

Watch the roast-to-press handoff and barrel loading rhythm that decides real hourly output.

  • Skipping aflatoxin testing: one contaminated batch can destroy an entire export shipment. Color sorter or manual picking is not optional for food-grade oil.
  • Mixed kernel size and drifting moisture: the press is blamed for low yield that actually comes from inconsistent feed.
  • Using cold-press claims for hot-route oil: hot-pressed oil is fragrant and practical, but it is not cold-pressed — mislabeling risks brand and compliance problems.
  • Sizing only the press: shelling, roasting, filtration, and cake handling must match its throughput, or the press sits idle waiting on a bottleneck elsewhere.

Strong front-end preparation and aflatoxin control remove most arguments about machine size that are really feedstock problems.

Why hydraulic

Why a hydraulic press suits peanut oil — and what stays constant across the range

Peanut kernels are soft, high-oil (44-56%) seeds that release oil readily under steady pressure, which is exactly what a hydraulic press delivers: a slow, even squeeze that protects flavor instead of the high-shear heat of a screw press. Across the peanut oil line team range — model 300, 325, 355, and up to 500 — the hydraulic system is the same: 60 MPa system pressure driven by a 2.2 kW motor, mechanical high- and low-pressure relief valves (not solenoid valves), carbon-steel partition plates between cakes (not filter cloth), and twin pressure gauges whose needles should always read together. What changes between models is frame strength and pressure stability, not the core hydraulics. That is why the model choice follows the route, not the other way around: a 300-325 ton frame is matched to the faster, lower-pressure hot cycle (30-40 min, 80-100°C), while a 355-500 ton frame absorbs the higher mechanical stress of the cold cycle (60-90 min, ≤60°C) without deforming over years of use. A correctly sized press keeps its frame true, holds pressure steady, presses out more oil, and lasts longer — the four things that actually decide cost per ton of oil. Picking a bigger model than the route needs wastes capital; picking a smaller one than the cold route demands shortens its life.

Project boundary

What to confirm before scoping Peanut Oil Press Process Guide: Hot vs Cold Route, Yields, and Real Parameters

Peanut Oil Press Process Guide: Hot vs Cold Route, Yields, and Real Parameters 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 Peanut Oil Press modules stay. Listed on the factory hot-press page — discuss 300/325 first.

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

When discussing Peanut Oil Press Process Guide: Hot vs Cold Route, Yields, and Real Parameters, pin models to published factory specs — not tonnage alone.

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).

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
  • 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.
  • Listed on the factory hot-press page — discuss 300/325 first.

Equipment check

project scope needs to land in equipment interfaces

After Peanut Oil Press Process Guide: Hot vs Cold Route, Yields, and Real Parameters 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.

Filtration, tanks, and peanut cake

Define pneumatic/plate-frame filtration, tanks, retained samples, and cake offtake before press count. Factory hot lines often use multi-layer paper filters.

Delivery data

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

Questions to confirm next

Clear these up first

Yes. Shells are 30-40% of pod weight and contain no oil. Hydraulic pressing works only on shelled kernels. If you start from pods, shelling must be in scope, and the 30-40% shell by-product needs a fuel, fiberboard, or disposal plan sized to match press throughput.

Send this page's requirement to the factory

Bring feed condition, target output, and site constraints, and we will continue from what this page covers.