Sawmill Residue Pellet Plant in Bosnia and Herzegovina

Sawmill Residue Pellet Plant in Bosnia and Herzegovina

This sawmill residue pellet plant in Bosnia and Herzegovina was developed for a sawmill operator that wanted to convert its own wet sawdust and nearby clean wood residues into a saleable fuel product instead of continuing to move low-value by-products off site. The completed project targets 45000 T/A of wood pellets. Its commercial line is rated at 9–10 T/H, with three MZLH768 pellet mills providing additional nominal pelletizing reserve above the normal finished-line output.

The annual schedule uses two 8-hour shifts and about 315 operating days, giving roughly 5040 scheduled production hours. Producing 45000 tonnes over that calendar requires an average finished output of about 8.9 T/H, so the line can meet the annual target without assuming that every hour runs at its maximum nameplate capacity. Maintenance, die work and cleaning are planned around the sawmill’s residue flow, with production campaigns adjusted when incoming moisture or customer orders change.

The project is integrated with an existing sawmill compound in central Bosnia rather than built as a remote greenfield pellet factory. Roads, loaders and part of the storage infrastructure are reused, while the pellet section separates wet raw-material handling from dry finished-product storage.

The design also reflects Bosnia and Herzegovina’s continental and mountain climate: covered storage prevents rain and snow pickup, but winter cold is not treated as a drying method. Moisture is measured and removed by the dryer whenever the feed remains above the pelletizing window.

Total completed project investment is USD 680,000. The equipment supply portion accounts for about USD 425,000, while the balance covers building adaptation, electrical works, foundations, installation, dust and fire-control integration, utility connections and commissioning.

This distinction keeps the case consistent with the real scope of a 9–10 T/H project that includes wet-residue drying, three pellet mills, mechanical cooling and finished-product handling rather than presenting the machine package alone as the cost of the entire factory.

capacity

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project type

Bosnia and Herzegovina gives this project a credible industrial residue base because forestry and wood processing are established parts of the national economy. Recent investment-promotion data put forests and forest land at about 3.23 million hectares, around 63% of national territory, with wood stock of roughly 435 million m³.

The same source reports a long-standing export-oriented wood industry, so the project is tied to an existing sawmill and wood-processing chain rather than a speculative plan to harvest trees solely for pellet production.

The country’s wood industry exported about KM 1.62 billion in 2024, with Germany, Croatia, Serbia and Italy among the sector’s leading markets. Those figures describe the broader wood industry rather than guaranteeing pellet sales, but they support the logic of locating a residue-upgrading project close to existing processors and regional transport routes. Pellet contracts still depend on product certification, buyer specification, freight and seasonal heating demand.

Project DriverDesign or Commercial Effect
Existing sawmill residue streamProvides a base load of sawdust before external purchasing is considered
Nearby wood processorsSupply chips and clean offcuts when the client’s own residue is insufficient
Export-oriented wood sectorMakes traceability, documentation and cross-border logistics familiar to local operators
Continental and mountain climateRequires covered storage and winter operating measures but does not eliminate drying duty
Regional road accessSupports domestic and neighboring-market deliveries without depending on one distant export route

For the sawmill residue pellet plant in Bosnia and Herzegovina, the commercial priority is to convert a predictable by-product stream into a tested pellet specification. The customer therefore manages raw-material moisture, electricity, dryer fuel, wear parts, packing and freight on a dry-finished-ton basis. This prevents wet sawdust from appearing artificially cheap and allows each domestic or cross-border sales contract to be evaluated on the real cost of usable pellets.

The raw-material plan retains the client’s 60000 T/A residue basis but separates material form and moisture because the three streams do not enter the line in the same condition. About 50000 T/A is wet sawdust generated by the client’s own sawmill. Around 5000 T/A of chips and 5000 T/A of clean solid-wood offcuts are sourced from nearby processors. Painted, preservative-treated, demolition and adhesive-rich engineered-wood residues are excluded from the fuel feedstock.

Raw MaterialAnnual QuantityTypical MoisturePrimary Preparation
Sawmill sawdust50000 T/AAbout 28–32%Screening, moisture control and drying; fine fractions can bypass coarse crushing
Wood chips5000 T/AAbout 30–45%Size check, grinding and drying as required
Clean solid-wood offcuts5000 T/AAbout 25–40%Chipping, grinding and drying
Total as-received feedstock60000 T/AWeighted average near 30%Supports the 45000 T/A finished-pellet target after water removal and normal dry-matter loss

The mass balance closes only when moisture is handled correctly. Sixty thousand tonnes of material at an average 30% moisture contains about 42000 tonnes of dry wood solids. Forty-five thousand tonnes of finished pellets at 10% moisture contains about 40500 tonnes of dry solids.

The difference allows roughly 1500 tonnes of dry-material loss through screening, dust, bark rejection and normal process losses, while about 13500 tonnes of water must be removed before finished product leaves the plant.

Across roughly 5040 scheduled production hours, the average water-removal requirement is about 2.7 T/H. That is why the project needs a real industrial dryer rather than the earlier assumption that covered storage or winter freezing can replace thermal drying. Storage is used to protect material and smooth supplier delivery.

The dryer and its biomass hot-air furnace are sized around actual evaporation duty, with lower burner load when material arrives drier and higher duty after wet-weather deliveries.

  • Every incoming lot is checked for moisture, visible contamination and material form before it is routed to storage or preparation.
  • Fine sawdust bypasses the coarse chipper; only oversize chips and clean offcuts are reduced by coarse crushing.
  • Magnetic separation is placed ahead of sensitive size-reduction and pelletizing equipment to remove ferrous contamination.
  • Bark-rich, painted, treated or otherwise unsuitable material is rejected or managed separately instead of being blended into saleable pellets.

The existing sawmill property provides about 7500 m² of usable project area. Rather than describing the entire property as one enclosed building, the pellet project uses roughly 3300 m² of covered production and storage space, with the balance retained for truck movement, outdoor utility areas, fire access and sawmill operations. Wet raw material and finished pellets are physically separated so moisture, dust and loader traffic from the receiving side do not interfere with dry-product storage.

ZoneApprox. Covered AreaUse
Wet raw-material storage1000 m²Sawdust, chips and clean offcuts with short-term buffer capacity
Preparation drying and pelletizing1200 m²Chipping, grinding, dryer, dry buffer, three pellet mills, cooling and screening
Finished-product storage and packing700 m²Bagged pellets, big bags and dispatch staging
Maintenance electrical and utility rooms200 m²Electrical distribution, spare parts, tools and controls
Office laboratory and staff area200 m²Administration, sampling, quality checks and staff facilities
Total covered areaApprox. 3300 m²Within an existing sawmill compound of about 7500 m²

The building has a concrete floor and enough clear height for elevators, bins, ducting and cooling equipment. Winter design focuses on protected conveyors, enclosed electrical equipment and reliable access around snow or freezing conditions; summer operation needs ventilation and dust management. The raw-material store is not intended to hold several months of annual consumption.

Because the owner’s sawmill supplies material continuously, storage is sized as an operating buffer, while external suppliers deliver against planned weekly requirements.

Different wood forms take different routes, but the whole process remains one coordinated line: receiving and inspection → magnetic separation → selective chipping → hammer milling → moisture measurement → rotary drying when required → dry-material buffering → pelletizing → counterflow cooling → screening → packing and storage.

This route avoids sending fine sawdust through unnecessary coarse equipment while still bringing chips and offcuts into the particle-size range needed for uniform drying and stable pellet formation.

Clean offcuts and oversize chips enter the wood chipper only when their dimensions exceed the hammer mill feed limit. Prepared chips, coarse sawdust and other material requiring further reduction then pass through the wood pellet hammer mill. Fine sawdust can bypass the chipper and, when already within specification, may also bypass intensive grinding.

The objective is generally a controlled fibrous particle distribution around 3–5 mm rather than forcing every tonne through identical size-reduction energy.

Material above the commissioned moisture limit enters the wood chip dryer. A biomass hot-air furnace uses approved low-grade clean wood residues such as bark and non-product sawmill fuel rather than consuming high-value finished pellets as the default heat source. Dryer control is based on inlet moisture, outlet moisture and fire-safety limits. For an average 30% inlet and about 10–12% dry feed, the line needs roughly 2.5–3 T/H of average water evaporation and enough reserve for wetter batches.

Dried material is buffered before pelletizing so short changes in the dryer or grinder do not immediately destabilize all three pellet mills. The mills are operated in parallel and can be sequenced according to feedstock condition and maintenance needs. Fresh pellets then enter mechanical cooling, not floor cooling. Counterflow cooling reduces temperature before screening, limits condensation risk in storage and allows fines to be removed before bagging or bulk dispatch.

  1. Inspect and segregate sawdust, chips and offcuts by moisture, contamination and size.
  2. Chip only oversize clean wood, then grind the fractions that need finer particle preparation.
  3. Measure moisture and send wet prepared material through the rotary dryer; route suitably dry material through the controlled bypass where the line design allows it.
  4. Feed dry material to the three parallel pellet mills through a stable buffer and controlled distribution system.
  5. Cool, screen and recycle qualified clean fines before finished pellets enter bagging, big-bag or bulk storage.

Three MZLH768 units form the pelletizing core. Each machine is configured at 315 kW with a typical wood-pellet capacity of about 3–4 T/H on properly prepared feedstock. The three-machine nominal window is therefore about 9–12 T/H, while the complete project is operated as a 9–10 T/H commercial line after allowance for dryer behavior, raw-material variation and downstream handling.

This gives the operator enough reserve to maintain annual output without advertising a theoretical pellet-mill sum as guaranteed finished-line throughput.

EquipmentQtyKey Design BasisFunction
Wood chipper machine155–75 kW classReduces clean oversize offcuts and large chips
Hammer mill190–110 kW classProduces the controlled particle size required for drying and pelletizing
Rotary dryer and biomass hot-air furnace1 setApprox. 2.5–3 T/H average water evaporation dutyReduces variable wet residue to the pelletizing moisture window
MZLH768 Wood pellet mill3315 kW each; 3–4 T/H eachParallel production of 8 mm fuel pellets
Counterflow cooler1Sized above 10 T/HMechanical cooling before screening and storage
Pellet screener19–10 T/H finished-line basisRemoves fines and oversize after cooling
Dust and aspiration system1 systemMultiple controlled pickup pointsControls chipper, hammer mill, transfer and pellet-area dust
Packing system1 setRetail bags plus big-bag capabilityWeighs and packs finished pellets
Conveying and electrical control1 setProject-matchedConnects wet preparation, drying, dry buffering and finished-product handling

The three machines are not three identical isolated lines. Material distribution, dry buffering, cooling and screening are shared so operators can stop one wood pellet extruder machine for planned maintenance while the remaining units continue at reduced output. This arrangement is more useful to a sawmill owner than forcing one very large pelletizer to carry the entire annual duty and gives the project a practical route for die service, roller work and raw-material trials.

Total project investment is USD 680,000, including the approximately USD 425,000 equipment supply package and the additional project costs required for installation in the existing sawmill compound. The total includes building and foundation work, electrical integration, dryer heat-source installation, fire and dust-control measures, internal material handling and commissioning. Keeping both figures separate prevents the equipment contract from being mistaken for the finished project cost.

Electrical design is dominated by the three pellet mills. Their combined main-motor load is 945 kW before the hammer mill, chipper, dryer drives and fans, cooler, dust collection, conveyors, screen and packing equipment are added.

The connected load therefore falls roughly in the 1.3–1.5 MW class, with final transformer and protection sizing based on the simultaneous-load calculation, motor-starting method and local utility connection. Bosnia and Herzegovina’s network nominal frequency is 50 Hz, so motors and controls are specified accordingly.

UtilityPlanning BasisEngineering Note
ElectricityApprox. 4–5 GWh/yearActual use depends on pellet-mill loading, drying hours and the percentage of material requiring size reduction
Dryer heatBiomass hot-air furnace sized to evaporation dutyFuel demand depends on inlet moisture, fuel moisture and furnace efficiency
WaterLow process demandMainly domestic use, cleaning, fire protection and limited utility needs
Compressed airProject-specificFor pneumatic gates, controls and packing equipment where fitted

An annual electricity figure cannot be calculated by multiplying every connected motor by every scheduled hour because the chipper, hammer mill, dryer and pellet mills do not all remain at full load continuously. A planning range of 4–5 GWh corresponds to roughly 90–110 kWh per tonne of finished pellets, which is credible for a line with heavy pelletizing and substantial drying support.

The customer verifies the actual specific consumption after commissioning and uses the contracted local electricity tariff rather than a fixed web-page EUR/kWh assumption.

Dryer energy is tracked separately because moisture dominates the heat balance. At the project’s average mass balance, about 13500 tonnes of water are removed annually. If incoming sawdust becomes wetter, thermal fuel consumption rises even when finished tonnage does not change. This is why feedstock contracts record moisture and why the operator does not treat a wet tonne of residue as economically equivalent to a dry tonne.

The line uses a lean two-shift operating team rather than the five-person total assumed in the draft. Around 7–8 production personnel per active shift cover receiving and loader work, line operation, pelletizing, packing and warehouse duties. Maintenance and quality functions can be shared with the existing sawmill, giving roughly 16–18 direct roles around the pellet operation without duplicating every support position.

The standard commercial product is an 8 mm fuel pellet made from clean sawmill residues. The project does not claim ENplus certification simply because the pellets are intended for European buyers. Certification is a separate audited scheme covering product requirements, traceability, handling and company procedures.

If the producer pursues ENplus A2, the official specification requires 6 ± 1 mm or 8 ± 1 mm diameter, 3.15–40 mm length, moisture no higher than 10%, ash no higher than 1.20% on a dry basis, mechanical durability of at least 97.5% and bulk density of 600–750 kg/m³.

Finished Product ParameterProject TargetVerification Basis
Diameter8 mm nominalRing-die specification and finished-product measurement
LengthWithin buyer or certification limitCutter setting and sampling
MoistureTypically ≤10% for certification-oriented productMoisture test after cooling and before release
Mechanical durabilityBuyer or certification requirementLaboratory test using the agreed method
AshDepends on clean-wood blend; ≤1.20% required for ENplus A2Representative laboratory analysis
Bulk densityMeasured by lot; 600–750 kg/m³ if targeting ENplus classesLaboratory or standardized bulk-density test
Net calorific valueDeclared from test; ≥4.6 kWh/kg if targeting ENplusRepresentative fuel analysis

Actual product claims are based on laboratory results from the sawmill’s wood mix, not assumed species values. Bark content and contamination have a direct effect on ash, while moisture and fines influence storage and combustion behavior. The customer can sell through domestic distributors, industrial users or cross-border contracts, but each route requires its own packaging, delivery and quality documentation.

Retail-sized bags, 500–1000 kg big bags and bulk dispatch are all technically possible within the same finished-product section.

The broader wood industry in Bosnia and Herzegovina is strongly export-oriented, but this page does not convert general wood-export statistics into guaranteed pellet demand. Germany, Croatia, Serbia and Italy are among the important markets for the country’s wood sector, while actual pellet sales depend on contract pricing, certification status and freight.

The wood pellet production line is therefore designed first around reliable 45000 T/A production and product consistency, leaving the sales team to choose the best domestic or regional channel.

Environmental control is centered on combustible wood dust, dryer exhaust, noise, fire risk and material storage. Local aspiration is installed at chipping, grinding, dry transfer, pelletizing and screening points. The dryer and biomass furnace use spark control, cyclone separation and filtration selected for the actual gas temperature and permit requirements.

Instead of stating that Bosnian law requires three identical 18 m stacks, the final exhaust arrangement and stack heights are set by the applicable environmental permit, emission limits and site dispersion assessment.

The plant has no continuous process-water discharge from pellet production. Domestic wastewater and stormwater are handled separately, while the yard and raw-material areas are graded so runoff does not enter finished-pellet storage. Housekeeping is part of fire prevention because settled wood dust can become an ignition and explosion hazard.

Magnets, temperature monitoring, accessible fire points and separation of wet raw material from hot drying and pelletizing equipment are included in operating procedures.

Bosnia and Herzegovina has entity-level environmental permitting procedures, so the applicable authority depends on the project location and scope. The case does not copy an emission concentration, chimney height or permit threshold from another plant. Where production capacity, combustion equipment or later expansion triggers additional environmental assessment or permit conditions, those requirements are addressed through the project’s current local approval process.

The project is built around mixed sawmill residues, so RICHI’s engineering scope starts with the water balance and material form rather than only the number of pellet mills. The biomass wood pellet machine section can only perform consistently when wet sawdust, chips and offcuts arrive at a stable particle size and moisture.

Layout work therefore coordinates raw-material routes, dryer residence time, dry buffers, cooler capacity, dust pickup points, maintenance clearances and finished-product traffic before equipment installation begins.

Commissioning is carried out with the customer’s actual wood residues. Operators check moisture before and after drying, hammer-mill screen performance, dry-buffer behavior, pellet-mill amperage, die and roller condition, cooler airflow, fines return and packing accuracy. The three pellet mills are balanced as a system rather than tuned independently to three different output targets.

Training also covers spark and fire response, dust housekeeping, lubrication, wear-part inspection and safe isolation procedures.

The sawmill residue pellet plant in Bosnia and Herzegovina also retains practical expansion options without designing an oversized first-stage plant. If future sawmill throughput rises, the owner can first extend operating hours, storage and drying duty before considering more pelletizing capacity.

If raw-material moisture falls because more kiln-dried residues enter the blend, the dryer load and specific energy use decline. This makes the plant responsive to the sawmill’s real residue profile instead of locking the business into one theoretical moisture assumption.

For a similar biomass pellet project, the information that changes the design most is annual residue volume, moisture by season, percentage of sawdust versus chips and offcuts, bark and contamination level, required pellet specification, site power, building dimensions, storage days and sales format. Those inputs determine dryer size, grinding duty, pellet-mill quantity, cooler selection, electrical load and the finished project investment.

The economics of this sawmill residue pellet plant in Bosnia and Herzegovina come from vertical integration rather than from assuming that raw material is free. The owner’s sawdust already exists as a by-product, but it still carries handling, storage, drying and opportunity costs. Purchased chips and offcuts must be evaluated on a moisture-adjusted basis.

The business gains value when a controlled 45000 T/A fuel product sells for enough to cover those costs plus electricity, thermal energy, labor, wear parts, packing, maintenance and freight.

This is also why the project uses a full industrial process instead of a simplified seasonal line. A 60000 T/A wet-input balance requires substantial water removal, three parallel pellet mills need mechanical cooling and screening, and export-oriented customers require repeatable product testing.

The Wood pellet processing plant therefore combines residue-specific preprocessing with commercial downstream handling rather than relying on natural air drying and floor cooling to carry a 9–10 T/H factory.

Customers planning a comparable plant should provide monthly sawdust volume, moisture range, chip and offcut percentage, wood species, bark content, target pellet class, building layout, electricity conditions and intended packing. With those data, RICHI can calculate the mass balance, dryer evaporation duty, equipment configuration, power demand, storage requirement and investment scope before the project is frozen.

That is more useful than copying a standard capacity package from a dry-sawdust project into a wet sawmill-residue site.

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RICHI Machinery is one of the world’s leading suppliers of technology and services for the animal feed, aqua feed and pet food industries, also the largest pellet production line manufacturer in China.

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In the past three decades, we have expanded our business to a wide range of areas, including animal feed mill equipment, aqua feed equipment, pet feed equipment, biomass pellet equipment, fertilizer equipment, cat litter equipment, municipal solid waste pellets equipment, etc.

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