| Primary Function | Continuous conveying of bulk solids | The conveyor transfers loose material through a trough or enclosed tube by rotating a helical screw flight around a central shaft. |
| Main Operating Principle | Rotational motion converted into axial material flow | As the screw rotates, the flight pushes material forward. Friction between the material and the conveyor surfaces helps prevent the bulk solid from simply rotating with the screw. |
| Core Components | Screw flight, shaft, trough or tube, drive, bearings, inlet, and discharge | Each component supports material containment, controlled rotation, alignment, loading, or discharge. |
| Screw Flight | Helical ribbon wrapped around a shaft | The flight provides the pushing surface. Its diameter, pitch, thickness, and profile influence capacity, power demand, and material handling behavior. |
| Shaft Arrangement | Shafted or shaftless | Shafted designs are widely used for conventional dry bulk solids. Shaftless designs can handle certain sticky, stringy, or difficult materials with fewer internal obstructions. |
| Conveyor Enclosure | U-trough, tubular housing, or covered trough | An enclosed housing limits dust release, protects the product from contamination, and improves safety in dusty or weather-sensitive applications. |
| Common Flight Types | Standard, variable-pitch, tapered, ribbon, cut-flight, and paddle | Flight geometry can regulate feed rate, improve mixing, reduce buildup, support aeration, or accommodate materials with different flow characteristics. |
| Typical Materials | Powders, granules, pellets, flakes, chips, and moist solids | Examples include grain, flour, cement, lime, ash, fertilizer, plastic pellets, wood chips, food ingredients, and wastewater screenings. |
| Material Flowability | Free-flowing, sluggish, cohesive, abrasive, or sticky | Flowability affects filling, power requirements, possible bridging at the inlet, and the choice of flight profile and conveyor speed. |
| Bulk Density | Material-specific; commonly expressed in kg/m³ or lb/ft³ | Bulk density is required to convert volumetric conveying capacity into mass flow and influences torque and drive sizing. |
| Particle Size | Fine powder to coarse particles, depending on equipment design | Particle size affects the required clearance, risk of segregation, wear rate, and the possibility of particle damage. |
| Screw Diameter | Selected according to capacity, material, and installation limits | A larger diameter generally provides greater volumetric capacity at a comparable fill level and speed, but it also increases equipment size and power demand. |
| Flight Pitch | Often close to the screw diameter for standard conveying; reduced pitches are also used | Pitch determines how far material tends to advance per revolution. Shorter pitches can improve control and increase the residence time. |
| Rotational Speed | Application-dependent; many industrial units operate at low to moderate speeds | Increasing speed can raise capacity, but excessive speed may increase wear, dust, particle degradation, and material centrifuging. |
| Loading or Fill Level | Common design ranges include partial loading rather than a completely full trough | Controlled fill prevents excessive torque and allows the screw to move material consistently without overloading the drive. |
| Conveying Direction | Horizontal, inclined, or vertical | The screw can move material horizontally and upward. Inclined and vertical conveying generally require special design and reduce effective capacity. |
| Incline Effect | Capacity typically decreases as the angle increases | Material tends to slide backward between flights at higher inclines. The exact reduction depends on material properties, pitch, speed, and fill level. |
| Throughput Basis | Volumetric rate or mass rate | Capacity is influenced by screw diameter, pitch, rotational speed, loading efficiency, conveyor angle, and bulk density. |
| Drive System | Electric motor with gearbox or geared motor | The drive supplies the torque required to overcome material resistance, friction, startup load, elevation, and any plugging tendency. |
| Metering Capability | Good when speed and inlet loading are controlled | Variable-speed drives and controlled feed gates allow the screw conveyor to function as a feeder as well as a transporter. |
| Mixing Function | Possible with suitable flight or shaft arrangements | Paddles, multiple inlets, variable pitch, or counteracting flight sections can promote blending while material travels through the conveyor. |
| Heating or Cooling | Available in jacketed or specially designed units | A jacket around the trough or tube can transfer heat to or from the material during conveying and processing. |
| Advantages | Compact layout, enclosed transfer, controlled flow, and flexible installation | The compact form suits short or moderately long routes and can combine conveying, feeding, mixing, and controlled discharge. |
| Limitations | Potential wear, power demand, buildup, and particle degradation | A screw conveyor may be unsuitable for highly fragile products, very long distances, extremely abrasive materials, or materials that readily compact without specialized design. |
| Maintenance Points | Bearings, seals, flights, liners, drive, and alignment | Regular inspection helps identify wear, material buildup, abnormal noise, overheating, loose connections, and changes in power consumption. |
| Safety Considerations | Guarding, lockout/tagout, covers, and controlled access | The rotating screw presents entanglement and crushing hazards. Access covers should remain secured, and power must be isolated before maintenance. |
| Best Selection Inputs | Material properties, required capacity, route, incline, temperature, and duty cycle | Accurate equipment selection requires both process data and mechanical information so the conveyor can achieve the target flow without excessive wear or overload. |