
Turnkey Peanut Production Plant Project (1 TPH Capacity)
- 🌍 Comprehensive Turnkey Proposal – 1 TPH Peanut Oil Production Plant
Scope: Turnkey delivery—from engineering and procurement to installation, commissioning, training, warranties, and performance guarantees—converting raw in-shell peanuts into refined, bottled edible oil and saleable by-products.
Capacity: 1 TPH raw peanuts → 0.40–0.45 TPH refined oil (typical oil yield 40–45%), 0.50–0.55 TPH press cake.
Economics (indicative): CAPEX (Capital Expenditure) $255k–$370k; OPEX (Operating Expenditure, ex-peanuts) $90–$147 per ton of peanuts; ROI (Return on Investment) 25–35%+; payback 2.5–4 years, driven by oil price, peanut cost, and cake valuation.
Edge: Automated controls (PLC = Programmable Logic Controller, SCADA = Supervisory Control And Data Acquisition), energy-efficient drive systems (VFD = Variable Frequency Drive), rigorous QA/QC, and ESG-positive by-product valorization.
1.0 Detailed Process Flow & Equipment Specification
Design philosophy: continuous, closed-loop, hygienic; minimal human intervention; maximum yield and uptime.
1.1 Raw Material Pre-Cleaning & Storage
Equipment: Vibratory sieve with aspiration hood; magnetic trap; receiving hopper; bag/tote dump.
Purpose: Remove stones, metal fragments, dust, and FM (Foreign Materials) to protect downstream assets.
Storage: Dry, ventilated, rodent-proof room; RH < 65%, temperature < 25 °C; FIFO racking.
KPIs: foreign matter < 0.2%; breakage < 1% during handling.
1.2 Shelling (Decortication)
Equipment: Automated cascading sheller with adjustable rubber rollers; aspiration columns; vibratory graders.
Outputs: Kernels, husk, middlings (recycle to sheller).
By-product use: Husk → biomass boiler fuel or pelletizing.
KPIs: shelling efficiency >98%; kernel breakage <2%.
1.3 Kernel Roasting
Equipment: Indirectly heated rotary drum roaster; PID temperature control via PLC; moisture probe at discharge.
Set-points: 110–130 °C, residence 20–35 min; discharge moisture 3–4%.
Benefits: promotes Maillard flavor, coagulates proteins, lowers press power/viscosity → higher oil yield.
1.4 Peeling (Testa Removal)
Equipment: Abrasive peeler; product cooler; cyclone + aspiration.
Target: >95% testa removal; skins collected for animal feed premix or fuel.
1.5 Oil Pressing (Mechanical Extraction)
Equipment: Heavy-duty continuous screw press/expeller with pre-heater, choke cone, wear-resistant cage/screw, torque monitoring.
Operating window: barrel temp 90–110 °C, pressure up to 850–1100 bar (localized), feed moisture 3–4%.
Outputs: Crude peanut oil (to hot tank) + press cake (~50–55% of input).
Option: Second-stage press for +1–2% oil recovery; or low-capex mini solvent extractor add-on (hexane) for premium yield (requires ATEX compliance—see §10).
1.6 Crude Oil Clarification & Filtration
Train: Vibrating scalper screen → heated balance tank → plate & frame filter press (food-grade cloth) or pressure leaf filter (upgrade).
Goal: solids < 100 ppm before refining; free moisture < 0.1%.
1.7 Refining (Semi-Automatic Batch)
Degumming: water/acid hydration to remove phospholipids.
Neutralization (Chemical) or Deacidification (Physical) depending on FFA (Free Fatty Acids) baseline.
Bleaching: activated earth under vacuum; dosage 0.5–1.5% (oil quality dependent).
Deodorization: high-vacuum steam stripping 210–240 °C; vacuum < 3 mbar; residence 30–90 min.
Cooling & polishing filter to final storage.
Refined Oil Specs (targets): FFA ≤0.1% as oleic, Peroxide Value ≤5 meq O₂/kg, Moisture & volatiles ≤0.1%, Insolubles ≤0.05%, color Lovibond ≤1.5R 20Y (or Gardner equivalent).
1.8 Filling & Packaging
Equipment: 4-head piston or mass-flow filler, rinser, capper, labeler, date coder; conveyors; checkweigher; case pack (manual/auto).
Formats: 200 mL–5 L PET/HDPE/glass; nitrogen flush optional for shelf-life.
Throughput example: with 1 TPH peanuts and 42% yield → ~420 kg/h oil ≈ ~460 L/h (ρ≈0.91 kg/L).
1 L SKU: ~460 bph single lane; scalable to 900–1,200 bph with starwheel or 8-head filler.
2.0 Utility Consumption, Sizing & Daily Loads (per ton of peanuts)
Utility Range Notes & Typical Sizing Electricity 55–70 kWh/t Installed connected load ~90–120 kW (press 30–40 kW, drives, pumps, fans). Daily at 10 t/day → 550–700 kWh Process Water 0.8–1.5 m³/t For refining washes + boiler make-up. Day load at 10 t/day → 8–15 m³ Thermal Energy 900–1,200 MJ/t Thermal oil heater 350–500 kW or steam boiler 0.2–0.3 t/h @ 8–10 bar Compressed Air 5–10 Nm³/t Screw compressor 3–5.5 kW, receiver 500–1,000 L, dryer to -20 °C PDP CIP (Clean-In-Place) skids: 3× 1,000 L tanks (caustic, hot water, rinse) with return pump and heat exchanger.
3.0 Plant Layout & Facility Requirements
Covered area: ~500–600 m²; clear height > 5.5 m; flow left-to-right to avoid cross-contamination.
Zone 1 – Raw & Packaging Store (150 m²): receiving, pre-cleaning, racking (FM control).
Zone 2 – Processing Hall (200 m²): sheller, roaster, peeler, press; epoxy floor, trench drains, high-volume ventilation.
Zone 3 – Refining & Filling Suite (100 m²): temperature-controlled, positive pressure, smooth wall finishes; segregated from roasting smells.
Zone 4 – Utilities (50 m²): boiler/thermal oil skid, MCC/electricals, compressor, water treatment, vacuum system.
Zone 5 – Finished Goods & Dispatch (100 m²): pallet racks, shaded dock; FIFO.
Hygiene: GMP zoning, pest control program, allergen management, HACCP plan with CCPs (Critical Control Points) at metal detection and deodorization.
4.0 CAPEX (USD, order-of-magnitude)
Phase Description Estimate Scope 1 Pre-Project & Design $20–30k Site survey, P&IDs (Piping & Instrumentation Diagrams), GA (General Arrangement) drawings, project controls 2 Equipment & Installation $200–280k All machines, structures, piping, electricals, PLC/SCADA, commissioning 3 Contingencies & Working Capital $35–60k 12–15% contingency; first fills (chemicals, filter media); 1–2 months operating float Total Estimated CAPEX $255–370k Firm fixed price after data-book validation Exclusions typically: taxes/duties, land/building, major civil works beyond foundations, grid upgrades, local approvals.
5.0 OPEX Snapshot (per ton of peanuts, excl. peanut cost)
Cost Center USD/t Notes Utilities 15–22 Power, fuel, water Labor (3-shift) 20–30 2–3 ops/shift + supervisor Maintenance & Spares 10–15 Preventive program, lubricants Packaging 25–50 Bottle, cap, label, carton Chemicals & Consumables 8–12 Bleaching earth, caustic, citric, filter cloths Admin/QA/QC 12–18 Lab, insurance, overhead Total 90–147 Excludes peanuts Per-liter lens: at 42% yield and 0.91 kg/L → ~2.38 t peanuts → 1,000 L oil; OPEX (ex-peanuts) ~$214–$350 per 1,000 L.
6.0 Mass Balance Example (typical)
Feed: 1,000 kg peanuts at 8% moisture →
Refined oil: 420 kg (~462 L)
Press cake: 540 kg (48–50% protein basis; valuable feed)
Losses & process rejects: ~40 kg (fines, gums, moisture, volatiles)
Neutralization chemistry (illustrative): For crude oil FFA 1.5% as oleic → NaOH 12–16 °Bé dose ≈ 7–9 kg/ton oil, producing soapstock (settled & recovered).
7.0 Product & QA/QC Specifications
Refined peanut oil: FFA ≤ 0.1%, PV (Peroxide Value) ≤ 5 meq O₂/kg, moisture ≤ 0.1%, insolubles ≤ 0.05%.
Microbiological: typically not growth-supportive; monitor plate counts in filling zone.
Shelf life: 12–18 months in sealed, light-protected packaging; nitrogen flush recommended.
Compliance: Codex/ISO edible oil specs; food-contact MOC (Materials of Construction) certificates.
8.0 Staffing & Organization (indicative)
Operations: 2–3 operators/shift × 3 shifts.
Maintenance: 1 electro-mechanic + part-time instrumentation tech.
QA/QC & Warehouse: 1 lab tech, 1 storekeeper.
Supervision: 1 production supervisor.
Total: 10–14 persons.9.0 Automation & Digitalization
PLC/SCADA with recipe management, alarm historian, batch records.
Energy meters on major consumers (press, heater, deodorizer).
OEE (Overall Equipment Effectiveness) dashboard; e-SOPs and e-maintenance (CMMS) optional.
10.0 EHS, Compliance & Risk
ATEX (explosive atmospheres) zoning if solvent add-on is adopted; otherwise standard hot-work precautions.
Fire safety: fryer/roaster hoods, flame arrestors, Class K extinguishers.
Ergonomics: guarded nip points, interlocks, LOTO (Lockout-Tagout).
Effluent: small ETP (Effluent Treatment Plant) 1–2 m³/h with oil trap and DAF (Dissolved Air Flotation) for wash waters.
Food safety: HACCP with CCPs at metal detection, filtration integrity, and deodorizer vacuum.
Key risks & mitigations:
Peanut price volatility: forward contracts, seasonal storage, quality bonuses/penalties.
Oil price swings: product mix (retail/bulk/food service), hedging options.
Yield slippage: strict moisture control at roaster, press settings, refining losses audit.
Unplanned downtime: critical spares (see §11), predictive maintenance.
11.0 Spares & Maintenance Strategy
Critical mechanical: press worms/cages, bearings, seals, V-belts, gear reducers.
Electrical/instrumentation: motors, VFDs, PLC I/O modules, sensors (T/P/level), HMI.
Consumables: filter cloth/paper, bleaching earth, caustic/citric, gaskets, lubricants.
Coverage: 6–12 months minimum; MTBF tracking; quarterly preventive shutdown.
12.0 Project Schedule & Commissioning
Overall schedule (from PO = purchase order): 14–18 weeks to SAT (Site Acceptance Test).
On-site commissioning: 4–5 weeks to first saleable oil.Week-by-week commissioning (typical):
W1: Mechanical completion, IO check, dry runs (IQ = Installation Qualification).
W2: Utilities proving, interlocks, water-oiling tests (OQ = Operational Qualification).
W3–W4: Hot runs with peanuts, refining tuning, first pass to spec.
W5: PQ = Performance Qualification at 1 TPH; 24-h reliability run; handover & operator certification.
13.0 Deliverables
Engineering: P&IDs, GA layouts, data sheets, cable/pipe lists, cause-and-effect/interlock matrix.
Quality & Operations: SOPs, HACCP plan templates, CIP procedures, sanitation master schedule.
Documentation: manuals, spare lists, MSDS (Material Safety Data Sheets) for chemicals, calibration certificates.
Commercial: 12-month equipment warranty; performance guarantee at 1 TPH within stated specs; training certificates.
14.0 Options & Upgrades
Second-stage press or small solvent extractor (hexane) for additional 4–6% oil recovery (requires ATEX & solvent recovery).
Polishing centrifuge post-bleach for ultra-low particulates.
Mass-flow filler upgrade to 8–12 heads; robotic case packing.
Solar thermal/biomass integration for roasting/steam; heat-recovery to process water.
QA lab kit: rapid FFA/PV meters, bench centrifuge, moisture analyzer.
Next Steps – Your Customized Business Case
Request the detailed financial model (Excel) to input local peanut prices, tariffs (power/water/fuel), labor, packaging, and selling prices—auto-generates ROI, NPV, IRR, payback.
Receive a site-specific technical layout adapted to your plot, utilities, and SKU strategy.
Book a confidential consultation with our project engineers to finalize scope, delivery plan, and guarantees.
Ready to move from concept to commercial oil in weeks—not years?
Contact us today to secure a firm quotation, tailored model, and execution schedule with locked delivery slots.
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