
Buyer-ready package for a 10 TPH Palm Oil Production Line, with biomass boiler (fiber/shell/EFB) and grid power.
- Buyer-ready package for a 10 TPH Palm Oil Production Line in Burundi, with biomass boiler (fiber/shell/EFB) and grid power.
Basis of Design
π Location: Central Africa (landlocked logistics, tropical climate; design for robust water/solids handling and high uptime).
βοΈ Capacity: 10 metric tons FFB/h (Fresh Fruit Bunches per hour; continuous duty).
(Units note used throughout: t = metric ton; h = hour; t/h = tons per hour; mΒ³/h = cubic meters per hour; mΒ³/d = cubic meters per day; kWh = kilowatt-hour; kW = kilowatt; kVA = kilovolt-ampere; USD = United States dollars; ha = hectares.)π Power Scenario: Grid supply (no turbine initially; future-ready).
π₯ Process Steam: Biomass boiler fired mainly with press fiber + shell (optionally EFB (Empty Fruit Bunches)/wood chips as supplement).
π― Quality Targets: CPO (Crude Palm Oil) moisture β€0.25%, impurities β€0.25%; stable clarification for good DOBI (Deterioration of Bleachability Index).
Process & Equipment (Fit-for-Purpose)
π FFB (Fresh Fruit Bunches) Reception & Weighing: Truck tipper, reception hoppers, belt/chain feeders with VFDs (Variable Frequency Drives), weighbridge.
π«§ Sterilization: Horizontal batch sterilizers w/ automatic cycle; steam PRV (Pressure Reducing Valve) station (3β4 barg (bar gauge) process steam), condensate return.
π Threshing: Rotary drum thresher with lifters; EFB (Empty Fruit Bunches) discharge to handling line (mulch/compost/fuel).
π¨ Digestion: Steam-heated digesters (multi-agitator) with temperature/level control.
πͺ Pressing: Twin-screw presses (2 trains for availability) with choke adjustment and dilution injection.
π§½ Primary Oil Screening: Vibratory screens + sand trap tank.
π§ͺ Clarification & Polishing: Decanter centrifuge (or continuous settling) β disc-stack purifier β vacuum dryer β CPO (Crude Palm Oil) buffer/polished tanks.
πΎ FiberβNut Recovery: Depericarper (air), nut conveyors.
π₯₯ Nut Cracking & Kernel Separation: Ripple mill β hydrocyclone/air table β kernel dryer β kernel silo (PK (Palm Kernel) line-ready).
π₯ Boiler Island (Biomass): 20 barg (bar gauge) class water-tube boiler, economizer, multicyclone, ID/FD fans (Induced Draft/Forced Draft), fuel feed (fiber/shell/EFB), deaerator, BW/condensate tanks (Boiler Water/condensate).
π§ Water & Effluent: Raw water treatment (filtration/softening), hot-water system, POME treatment (Palm Oil Mill Effluent; anaerobic + polishing), sludge oil recovery.
β‘ Electrical & Control: Main transformer (630 kVA (kilovolt-ampere) typical), MCCs (Motor Control Centers), PLC/SCADA (Programmable Logic Controller/Supervisory Control and Data Acquisition), instrumentation (flow/level/pressure/temp), safety interlocks & E-stops (Emergency Stops).
π§― HSE & Compliance: HSE (Health, Safety and Environment) fire detection/suppression, guarded drives, platforms/handrails, relief valves, confined-space & pressure-vessel compliance.
Utility Balance (10 TPH β Typical Ranges)
(TPH = tons per hour)
π Throughput & Yield: 10 t/h (tons per hour) FFB β ~2.0β2.3 t/h CPO (20β23% on FFB) + 0.5β0.7 t/h PK after kernel recovery.
π¨ Steam Demand: ~0.7β0.9 t steam/t FFB (metric tons of steam per ton of Fresh Fruit Bunches) β 7β9 t/h average; design boiler 10β12 t/h @ ~20 barg (bar gauge) (PRV (Pressure Reducing Valve) to 3β4 barg (bar gauge) for process), ~15% margin.
β‘ Electrical Load: 12β18 kWh/t FFB (kilowatt-hours per ton) β 120β180 kW average; connected load ~200β250 kW. Transformer ~630 kVA (PF (power factor) & motor starts).
πΏ Water Use: 0.8β1.2 mΒ³/t (cubic meters per ton) β 8β12 mΒ³/h average; peak makeup up to 20 mΒ³/h with cleaning/ETP (Effluent Treatment Plant) needs.
π§ͺ POME (Palm Oil Mill Effluent) Generation: 0.6β0.9 mΒ³/t β 6β9 mΒ³/h to ETP; design daily ~150β220 mΒ³/d with buffer.
πΏ Biomass Fuel: Primarily press fiber + shell; EFB as supplementary fuel. Plan for occasional wood chips during ramp-up/maintenance.
Plot Plan Concept (High-Level)
π§ Zones: (1) FFB handling & sterilizers, (2) threshing/digestion/pressing, (3) clarification & tank farm, (4) kernel plant, (5) boiler & utilities, (6) ETP, (7) maintenance/workshop, (8) admin/lab.
ποΈ Footprint: Process + utilities ~4,000β6,000 mΒ² under roof; full site including roads, laydown, ETP ~1.2β1.5 ha (hectares) (without large anaerobic ponds; add land if lagooning).
π Flow: Gravity-biased layout (sterilizer β thresher β digester β press β clarification) to minimize pumping and improve maintenance access.
Phased CAPEX (USD, Order-of-Magnitude Ranges)
(USD = United States dollars)
(Land excluded; import duties/logistics in/out of Burundi varyβranges reflect that uncertainty.)
π§© Baseline (lean/manual stations, settling + purifier): $4.8β6.2M.
π§ͺ Enhanced (decanter + purifier, robust SCADA (Supervisory Control and Data Acquisition), covered anaerobic digester): $6.8β8.9M.
π¦ Cost Buckets (indicative):
ποΈ Civil & Buildings: $0.9β1.3M
βοΈ Process & Kernel Equipment (FOB (Free On Board)): $2.8β3.6M
π₯ Boiler & Utilities (FOB (Free On Board)): $0.9β1.4M
π’ Freight/Insurance/Import (est. 15β20% CIF (Cost, Insurance and Freight) to site): $0.6β0.9M
β‘ Electrical & Automation: $0.5β0.8M
π§ ETP (Effluent Treatment Plant; anaerobic + polishing): $0.5β0.9M
π· Erection/Commissioning/Training: $0.6β0.9M
π§° Engineering/PM (Project Management)/Contingency (~10%): $0.6β0.8MOPEX Snapshot (Excluding FFB Cost)
π Power (grid): 12β18 kWh/t Γ tariff β ~$2.0β3.5 per t FFB (tariff-dependent).
πΏ Water & Chemicals: $0.5β1.2 per t FFB.
π οΈ Maintenance & Spares: 2β3% of TIC/yr (Total Installed Cost per year) (~$120β220k/yr (thousand per year) at mid-range CAPEX).
π₯ Labor: 35β55 headcount across shifts (operations, lab, maintenance, ETP, logistics, admin) β $4β6 per t FFB (assumption band).
π¦ Biomass Fuel: Net low external cost (fiber/shell internal); budget EFB prep/wood-chip supplement.
π§Ύ All-in (excl. fruit): ~$10β16 per t FFB typical band.
Recommended Spare Parts Package
πͺ Critical 0β6 Months (on site): press worms/cage bars, press gearbox seals, digester bearings/seals, screen decks, purifier/decanter wear parts, pump mechanical seals, valve kits, mission-critical transmitters, VFD (Variable Frequency Drive) spares.
βοΈ 12β24 Months (recommended): full press worm/cage set, ripple-mill liners/beaters, conveyor chains/sprockets, boiler grate/burner spares, instrumentation spares (DP cells (Differential Pressure transmitters), RTDs (Resistance Temperature Detectors)), MCC (Motor Control Center) contactors/relays.
β±οΈ Lead-Time Strategy: classify A (β€2 weeks), B (3β6 weeks), C (8β16 weeks) and hold A/B on site.
Training Plan (Operator-Centric)
π« Week 1β2 (Classroom): process fundamentals, HSE/LOTO (Health, Safety and Environment/Lockout-Tagout), QC (Quality Control) (FFA (Free Fatty Acids)/M&I (Moisture & Impurities)/DOBI (Deterioration of Bleachability Index)), utilities/boiler ops, ETP (Effluent Treatment Plant) basics, SOPs (Standard Operating Procedures) & checklists.
π Week 3β6 (On-the-Job): line walkdowns, start/stop procedures, alarm handling, press torque optimization, decanter/purifier tuning, shift-handovers, lab sampling, sanitation.
π§ͺ Week 7 (Assessment): written + practical evaluations; certification by area (pressing, clarification, kernel, boiler, ETP).
Commissioning Timeline (From Mechanical Completion)
π§° Pre-Comm (pre-commissioning; 2 weeks): loop checks, instrument calibration, motor rotation, flushing/cleaning, boiler hydro (hydrostatic test)/purge.
βοΈ Cold Commissioning (1β2 weeks): dry runs, interlock tests, conveyors/presses jog, water runs on clarification/ETP, electrical load tests.
π₯ Hot Commissioning (1β2 weeks): steam-on, sterilizer cycle tuning, hot oil/clarification stability, purifier balance, boiler/condensate optimization.
π Performance Test (1 week): yield, throughput, product specs (M&I (Moisture & Impurities)), utility KPIs (Key Performance Indicators); punch-list closure and handover.
π Ramp-Up (2β4 weeks): progressive throughput to 10 TPH (tons per hour), operator coaching, energy/water optimization.
Deliverables Youβll Receive
π Engineering Dossier: PFDs (Process Flow Diagrams), P&IDs (Piping & Instrumentation Diagrams), I/O list (Input/Output), data sheets, GA (General Arrangement)/plot plan, utility balance.
π Operating Package: SOPs (Standard Operating Procedures), maintenance plans, critical spares list, QA/QC methods (Quality Assurance/Quality Control), commissioning & SAT protocols (Site Acceptance Test).
β»οΈ Compliance: pressure-vessel files, material certificates, and ETP (Effluent Treatment Plant) mass-balance ready for local permitting.
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