Small fish feed plant in Indonesia

fish feed plant project

The first enquiry arrived on May 24, 2018, requesting a quotation and video for a fish pellet machine at 1–2 T/H. That request established the starting interest, rather than the final floating-feed capacity. Subsequent discussions expanded the project to include poultry feed and defined a smaller extrusion branch suited to the combined business plan.

Making feed on the farm requires more than replacing purchased bags with a machine. The owner needs qualified ingredients, workable recipes, accurate weighing and a system for identifying finished lots. For a mixed poultry and fish business, preparation also has to prevent an unsuitable coarse poultry mash from being sent directly to the extruder.

The contract was signed on November 3, 2022, covering a 1–2 T/H poultry feed production line together with a 500 kg/h floating fish-feed unit. The two capacities remain separate throughout the layout and operating brief. The contract date records the agreed purchase; it does not establish a commissioning date or measured production performance.

separate route duties

equipment contract

location

project type

The poultry branch presses conditioned mash through a ring die. The fish branch uses extrusion followed by drying, cooling and grading. A single preparation area can serve both, but it must have enough batch time and correctly routed holding capacity. Concurrent operation is possible only after checking those shared duties; adding the two outlet ratings does not prove a continuous combined factory rate.

Project boundaryDefined duty
First enquiryMay 24, 2018
Contract signedNovember 3, 2022
Poultry route1–2 T/H reference duty
Floating fish-feed route500 kg/h; output basis requires confirmation
Common preparationScheduled grinding and mixing
Finished productsSeparate recipes and release checks

The poultry recipe brief includes corn, rice bran, soybean meal and copra meal, with palm kernel cake considered only where the formulator accepts its nutrient and fibre contribution. These materials differ in bulk density, grind behaviour and storage condition. Receiving checks and actual analyses guide their use; availability alone does not establish a suitable inclusion rate.

The fish-feed brief uses finely prepared corn, selected bran, soybean meal, qualified fish meal and controlled oil additions, with premixes and other small ingredients weighed separately. Oil applied before extrusion and oil applied after drying have different effects. Excess oil in the extrusion mix can limit expansion, so the formula and addition point must be agreed together.

Deliveries through an Indonesian supplier may include both domestic and imported ingredients. The purchase specification therefore follows the ingredient and lot, rather than assuming one origin or one nutrient value. Bran freshness, meal condition and fish-meal quality matter to both physical processing and formulation. Supplier changes should trigger a recipe and processing review before a new lot is released.

Input groupControl before production
Corn and branCondition and recipe-specific particle size
Protein mealsIdentity, analysis and supplier qualification
Copra or palm kernel materialFormula-specific fibre and inclusion limits
Fish mealQualified quality and intended diet
OilControlled quantity and addition point
PremixesAccurate weighing and mixing sequence

The small scale fish feed plant uses a common preparation concept followed by distinct processing branches. Weighing, grinding and mixing are scheduled to deliver the correct mash to each destination. Fish-feed mash requires its own agreed particle specification; a poultry grinding setting should not be adopted automatically for extrusion.

Weighing → Cleaning → Recipe-specific grinding → Mixing → Route selection → Poultry conditioning and pelleting OR Fish extrusion and drying → Cooling → Grading → Packing

The route selector is an operating control, not simply a tee in the conveyor. Batch identity, holding-bin destination and cleaning procedures need to agree before mash is discharged. When recipes share equipment, carryover is considered during production sequencing, with residual material returned only to a compatible feed batch.

StagePoultry routeFish route
GrindingAgreed poultry particle specificationFiner recipe-specific preparation
FormingSteam conditioning and ring-die pressingExtrusion with controlled moisture
DryingNo separate dryer assumedRequired after wet extrusion
CoolingBefore crumbling or packingAfter drying; before packing
SizingIntact pellets or screened crumbsSelected die size and grading
Return materialCompatible poultry batches onlyAssessed compatible fish batches only

Poultry pellets, poultry crumbs and floating fish pellets are separate product briefs. Crumbling poultry feed does not make it a suitable juvenile fish diet. Likewise, changing an extrusion die does not by itself qualify a recipe for ornamental fish. Each additional product needs a nutritional specification, a practical processing trial and an agreed release standard.

Product briefFormCheck before release
Poultry grower feedIntact pelletsRecipe, durability and fines
Chick feedScreened poultry crumbsAppropriate diet and crumb fraction
Floating fish feedExtruded pelletsSize, floatability and water stability
Additional fish gradesTrial-qualified productsNutrition and extrusion suitability

Equipment duties without an invented model list

The poultry press and floating-feed extruder perform different jobs. The poultry feed pellet machine must be matched to the intended poultry pellet size and formula, while the floating fish feed extruder machine must be matched to the fish recipe, die and dried-product duty. The contracted equipment categories are described below without assigning an unconfirmed model or motor power.

Equipment groupSizing responsibility
Cleaning and hammer millingMaterial quality and particle specification
Batch mixingFull cycle and route schedule
Poultry pellet press1–2 T/H recipe-specific duty
Fish-feed extruder500 kg/h basis and product specification
Fish-feed dryerWet load and water removal
Cooling equipmentRoute-specific heat and moisture load
Crumbler with bypassPoultry grade and screened yield
Screens and packingSeparate product identity and handling

For this combined package, the feed mill equipment must be checked as a connected system. A press rating alone cannot establish bagged output. Shared preparation, transfers, dryer evaporation, cooling and bag handling can each restrict production. The technical schedule should identify those interfaces before dimensions, electrical loads or operating shifts are committed.

At the upper poultry reference duty, two tonnes of poultry feed require preparation for that route during each hour of continuous operation. A further 500 kg/h fish branch increases the shared demand only if both operate together. Sequential production reduces the instantaneous shared load, but the poultry and fish quantities then compete for available production time.

A holding bin can allow the extruder to continue while the mixer changes recipe, provided the bin contains the correct fish mash. Its usable quantity sets the bridging time. For example, 250 kg of usable mash supports a 500 kg/h draw for 30 minutes. This is a scheduling illustration, not a confirmed installed bin size or proof of simultaneous rated output.

The table gives planning arithmetic for this small fish feed plant in Indonesia. It excludes changeovers, start-up material, cleaning and downtime. Fish bag counts use dried, cooled and accepted feed, not wet extrudate. These boundaries keep production planning connected to the material that can actually be packed.

Planning basisCalculated requirement
Poultry: 1 T/H in 25 kg bags40 bags/hour
Poultry: 2 T/H in 25 kg bags80 bags/hour
Fish: 0.5 T/H in 25 kg bags20 bags/hour
Both upper targets together100 bags/hour; subject to shared capacity
250 kg buffer at 500 kg/h draw30 minutes; usable quantity only

For the 500 kg/h branch, the specification needs to state whether the quoted rate refers to mash, wet extrudate or finished feed. The project brief names the branch capacity but does not supply a performance-test basis. The engineering example below uses 500 kg/h of finished fish feed at 10% moisture to show the dryer calculation; it is not a certified output record.

With 25% moisture at the dryer inlet, 500 kg/h of finished feed at 10% moisture contains 450 kg/h of dry solids. Keeping those solids constant requires 600 kg/h of wet extrudate and removal of 100 kg/h of water. The inlet moisture is an illustrative assumption. Actual dryer selection needs measured inlet condition, recipe, air conditions and the agreed product endpoint.

Illustrative fish-feed balanceFlow
Wet dryer inlet at 25% moisture600 kg/h
Dry solids entering and leaving450 kg/h
Water entering dryer150 kg/h
Water in finished feed50 kg/h
Water evaporated100 kg/h
Finished feed at 10% moisture500 kg/h

After drying, fish feed must cool sufficiently for packing without condensation. In a warm, humid location, the available intake air and the finished-feed condition should be assessed together. A fixed storage-life promise cannot be derived from the country name, a dryer setting or a cooler alone. Moisture, water activity where appropriate, package condition and storage practice inform release.

A useful enquiry for a compact feed plant states the poultry and fish quantities separately, along with the intended fish pellet sizes, main ingredients and daily production window. It also identifies available power, water, heat services and building access. These details determine whether shared preparation is practical or whether particular duties need dedicated equipment.

Before accepting a small scale feed mill production arrangement, confirm the recipe-specific grinding requirement, batch schedule, extrusion output basis and dryer duty. Specify how rejected sizes and start-up material will be collected and assessed. Packing should accept only identified, cooled product; a nominal machine rate is not a substitute for an agreed finished-feed test.

RICHI can develop a small fish feed plant in Indonesia around the buyer’s actual product mix. Send the poultry and floating-feed targets separately, together with the raw-material list and available services, so the proposal can connect equipment selection, process routing and a realistic operating schedule.

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