| Steam Cooker | Indirect heating with steam through a jacket or internal heating surfaces | Coagulates fish proteins and releases part of the oil and moisture before pressing | Fresh or chilled whole fish, trimmings, and fish offal | Heating temperature, residence time, steam pressure, and feed consistency | Uniform cooking supports efficient separation and helps limit excessive protein damage | Good heat control; suitable for continuous operation; relatively low direct contact with the product | Requires a reliable steam supply and additional boiler-room infrastructure | Medium- to large-scale plants seeking consistent cooking conditions |
| Direct-Fired or Hot-Air Cooker | Direct contact with hot combustion gases or heated air | Rapidly heats and partially dries the raw material while beginning protein coagulation | Fish raw material with moderate moisture and plants with limited steam capacity | Gas temperature, airflow, residence time, and combustion control | Fast heating is possible, but poor control can cause localized overheating or oxidation | Quick start-up; does not require a steam boiler; compact in some layouts | Greater risk of uneven heating and possible contamination if combustion gases contact the product directly | Small or specialized operations where steam generation is impractical |
| Screw Press | Mechanical dewatering by continuous compression and shearing | Separates press liquor, containing water and oil, from the cooked fish solids | Properly cooked fish and fish offal | Press speed, compression ratio, screen condition, and cooked-material temperature | Effective pressing reduces the moisture load on the dryer and supports higher meal recovery | Continuous operation; robust design; lower thermal demand after pressing | Performance depends strongly on cooking quality; excessive pressure can increase fines and wear | Standard continuous fish meal lines requiring mechanical dewatering |
| Decanter Centrifuge | High-speed centrifugal separation of solids, water, and oil-containing liquid phases | Clarifies press liquor and recovers suspended solids before oil separation | Press liquor and liquid streams containing fine fish solids | Bowl speed, differential speed, feed rate, and solids concentration | Can improve recovery of fine solids and reduce suspended material in downstream liquid streams | Compact; continuous; effective for fine particles that are difficult to settle by gravity | Higher capital and maintenance requirements; power consumption is significant | Plants processing high volumes or raw materials that generate fine suspended solids |
| Disc-Stack Centrifuge | High-speed centrifugal clarification and liquid-liquid separation | Separates fish oil from stickwater and fine suspended solids after pressing | Clarified press liquor or liquid containing recoverable fish oil | Feed temperature, flow rate, bowl speed, interface setting, and solids loading | Produces cleaner oil and can improve recovery of valuable liquid fractions | High separation efficiency; continuous operation; suitable for compact process layouts | Requires careful feed conditioning and regular cleaning; sensitive to excessive solids | Facilities prioritizing fish-oil recovery and liquid-stream clarification |
| Tube-Bundle Dryer | Indirect convective drying through heated tubes and controlled airflow | Removes moisture from pressed fish cake to produce stable fish meal | Pressed fish cake with reduced but still substantial moisture | Drying-air temperature, airflow, residence time, feed layer thickness, and exhaust humidity | Indirect heating helps reduce direct oxidation and allows better control of final moisture | Good product protection; suitable for continuous production; relatively low direct contact with combustion gases | Higher equipment cost and more complex heat-transfer surfaces than simple direct dryers | Quality-focused plants producing consistent meal for feed applications |
| Disc Dryer | Indirect conductive drying using heated rotating discs | Dries fish cake through contact with heated surfaces while mixing the product | Pressed fish cake and other sticky, cohesive rendered materials | Disc temperature, rotor speed, feed rate, vacuum or airflow, and product residence time | Controlled indirect drying can help preserve protein quality and reduce surface scorching | Efficient heat transfer; handles relatively sticky material; generally enclosed | Moving parts require maintenance; overloading may reduce drying uniformity | Plants handling cohesive fish cake and requiring controlled indirect drying |
| Direct Rotary Dryer | Direct contact between hot air and tumbling fish meal or fish cake | Rapidly reduces moisture after pressing | Pressed fish cake or partially dried fish meal | Hot-air temperature, drum speed, airflow, fill level, and residence time | High temperatures or excessive residence time may darken the meal and reduce heat-sensitive quality | High throughput; straightforward continuous operation; relatively simple mechanical design | Greater risk of oxidation, overheating, dust generation, and odor emissions without proper control | High-throughput operations where drying capacity and simple process flow are priorities |
| Hammer Mill | Impact milling with rotating hammers and a perforated screen | Reduces dried fish meal to a more uniform particle size | Fully dried fish meal with low residual moisture | Rotor speed, screen opening, feed rate, and meal temperature | Improves particle-size consistency for blending, conveying, and feed formulation | High capacity; adjustable particle size; widely applicable to dry meal | Creates noise and dust; excessive heat or overgrinding can increase energy use | General-purpose size reduction after drying and before storage or packaging |
| Pin Mill | Fine grinding through high-speed impact between pins or discs | Produces a finer and more uniform fish meal powder | Dry, free-flowing fish meal requiring fine particle size | Rotor speed, feed rate, clearance, and product temperature | Can provide a fine, homogeneous meal, but heat generation must be controlled | Suitable for fine grinding; compact; adjustable operating conditions | Less suitable for damp or fibrous feed; higher wear and energy demand at very fine sizes | Specialized applications requiring fine, uniform fish meal particles |
| Vibrating or Rotary Screen | Mechanical classification by particle size | Removes oversized particles and separates meal fractions before packing | Ground and cooled fish meal | Screen aperture, vibration or rotation speed, feed rate, and screen cleanliness | Improves uniformity and helps prevent oversized particles from entering the final product | Simple operation; low thermal impact; useful for quality control | Screens can blind when meal contains excess moisture or oil; requires routine cleaning | Final classification after grinding and before storage or packaging |