| Loss-in-Weight Screw Feeder | Measures the decrease in hopper weight while one or more screws continuously transfer powder into the process. | Free-flowing, cohesive, and moderately difficult powders when the screw and agitator are correctly selected. | Approximately 0.1 to 5,000 kg/h, depending on screw size, speed, and material density. | Often about ±0.5% to ±1.0% of setpoint after calibration and stable material flow are achieved. | Good continuous control; closed-loop gravimetric operation; suitable for broad capacity ranges; supports recipe changes. | Requires load-cell protection, refill management, and correct screw design; bridging or rat-holing can affect feed stability. | Continuous blending, extrusion, compounding, chemical processing, and food production. |
| Volumetric Screw Feeder | Uses screw displacement and rotational speed to deliver a calculated volume of powder per unit of time. | Relatively consistent, free-flowing powders with stable bulk density. | Approximately 0.1 to 3,000 kg/h, depending on screw geometry and equipment size. | Commonly about ±1% to ±3% of setpoint; actual mass accuracy varies with bulk-density changes. | Simple construction; lower initial cost; easy to operate; effective for steady materials and fixed recipes. | Does not automatically compensate for changes in bulk density, moisture, particle size, or powder aeration. | Batch dosing, packaging lines, and processes where material properties remain consistent. |
| Vibratory Tray Feeder | Uses controlled vibration to move powder along a tray toward an outlet or weighing point. | Free-flowing granules, crystals, pellets, and powders that do not compact easily. | Approximately 1 to 1,500 kg/h, depending on tray width, amplitude, and material flowability. | Typically about ±1% to ±2% in stable applications; lower performance may occur with cohesive powders. | Gentle conveying; low mechanical wear; easy to clean; suitable for fragile particles and sanitary designs. | Can be sensitive to vibration transmission, powder buildup, humidity, and inconsistent flow properties. | Food, pharmaceutical, nutraceutical, and fragile-particle handling applications. |
| Rotary Disc Feeder | A rotating disc carries a controlled layer of powder to a discharge point, where a scraper or doctor blade removes the material. | Free-flowing powders and fine materials that form a stable layer without excessive bridging. | Approximately 0.05 to 500 kg/h, depending on disc diameter, speed, and powder properties. | Often about ±1% to ±2% when powder density and surface behavior remain stable. | Good low-rate control; compact design; relatively gentle product handling; suitable for continuous dosing. | Layer thickness can change with moisture, cohesion, electrostatic charge, and bulk-density variation. | Low-rate dosing, laboratory systems, specialty chemicals, and continuous micro-addition. |
| Gravimetric Batch Weigh Feeder | Dispenses material into a weigh hopper or container until a target mass is reached, then resets for the next batch. | Most powders and granules, provided the hopper and discharge device prevent bridging or segregation. | Approximately 0.01 to 10,000 kg per batch, with cycle time determined by the target weight and feeder size. | Commonly about ±0.1% to ±0.5% of target batch weight under controlled conditions. | Direct mass measurement; strong batch-to-batch traceability; compensates for bulk-density variation. | Provides intermittent rather than continuous flow; may require settling time, anti-bridging equipment, or multiple-speed filling. | Batch formulation, premix preparation, pharmaceutical production, and quality-critical dosing. |
| Pneumatic Powder Feeder | Uses conveying air or gas to transport powder through a pipeline at a controlled rate. | Powders that can be pneumatically conveyed without excessive degradation, segregation, or dust-related risk. | Approximately 1 to 10,000 kg/h, depending on conveying mode, distance, gas velocity, and powder density. | Often about ±1% to ±3%; accuracy depends strongly on conveying stability and upstream metering. | Flexible routing; enclosed transfer; suitable for long distances, elevated points, and difficult layouts. | May cause particle attrition, segregation, static buildup, or filter loading; requires air-quality and dust-control systems. | Pneumatic transfer, enclosed feeding, silo-to-process conveying, and applications with limited floor space. |
| Twin-Screw Feeder | Two intermeshing or closely spaced screws provide positive powder movement and improve hopper discharge. | Cohesive, fine, sticky, or poorly flowing powders, including materials prone to bridging or rat-holing. | Approximately 0.05 to 5,000 kg/h, depending on screw diameter, configuration, and material density. | Often about ±0.5% to ±1.5% after suitable calibration and process stabilization. | Improved powder conditioning and reliable extraction; handles difficult materials better than many single-screw designs. | More complex and costly than basic single-screw systems; may create additional shear or heat for sensitive powders. | Fine chemicals, polymers, minerals, additives, and cohesive formulation ingredients. |
| Micro-Feeder | Uses a small precision screw, disc, belt, or loss-in-weight mechanism to deliver very small quantities at controlled rates. | Fine powders, high-value additives, pigments, catalysts, and ingredients used at low inclusion levels. | Approximately 0.001 to 50 kg/h, depending on feeder design and material flow behavior. | Commonly about ±0.5% to ±2% of setpoint; minimum stable rate is material-dependent. | Accurate low-rate dosing; reduces material waste; supports precise formulation and small recipe additions. | More sensitive to vibration, electrostatic effects, moisture, and inconsistent powder flow; may require specialized calibration. | Low-dose additives, laboratory-scale production, pharmaceuticals, coatings, and specialty formulations. |
| High-Shear or Agitated Feeder | Combines a metering device with an agitator, paddle, or auxiliary screw to maintain powder movement and prevent compaction. | Very cohesive, fluffy, moist, fibrous, or compressible powders that do not discharge reliably from a standard hopper. | Approximately 0.1 to 2,000 kg/h, depending on agitator design and powder characteristics. | Typically about ±1% to ±3%; results depend on preventing compaction and maintaining a consistent hopper condition. | Reduces bridging and rat-holing; improves hopper emptying; useful for challenging powders with poor flowability. | Additional moving parts can increase maintenance, shear, heat generation, and cleaning requirements. | High-cohesion powders, carbon black, pigments, starches, powders with high fines content, and difficult bulk solids. |