1. Function and classification of screw extruder
Screw extruder is a key automatic feeding equipment in the rubber industry, mainly used to produce various rubber semi-finished and finished products. According to the different feeding methods, it can be divided into two categories:
Cold feed screw extruder
Features: Directly feed room temperature rubber compound
Advantages: Eliminate the preheating process and save energy by 20-30%
Typical applications: automotive sealing strips, rubber pipes, wires and cables coating
Hot feed screw extruder
Features: Feed the rubber compound preheated by the open rubber mixer (60-80℃)
Advantages: High output, suitable for high viscosity rubber compound
Typical applications: tire treads, rubber tracks, large industrial products
Industry data: In the production of rubber products, about 65% of extrusion operations use cold feed models, and 35% use hot feed models
2. Working principle of screw extruder
The screw extruder completes rubber processing through a three-stage process of mechanical conveying → plasticizing and mixing → pressurized extrusion:
Feeding section (accounting for 30% of the screw length)
Cold feeding model: adopt deep screw groove design (h/D=0.25-0.3) to enhance the material gripping ability
Hot feeding model: shallow screw groove design (h/D=0.15-0.2) to improve the conveying efficiency
Compression plasticizing section (accounting for 50%)
Temperature control:
Cold feeding: 90-120℃ (heating by barrel + shearing)
Hot feeding: 100-130℃ (maintaining pre-plasticized state)
Special design:
Pin type mixing section (dispersion efficiency increased by 40%)
Barrier type screw (output increased by 15-20%)
Extrusion molding section (accounting for 20%)
Die head pressure: usually 5-15MPa (high hardness rubber can reach 25MPa)
Die design:
Expansion rate compensation (rubber extrusion expansion rate is about 30-80%)
Flow channel convergence angle (15-30° to optimize flow)
3. Comparison of technical advantages
Performance indicators |
Cold feed extruder |
Hot feed extruder |
Energy consumption |
0.3-0.5kWh/kg |
0.4-0.7kWh/kg |
Production capacity |
Medium-low (50-500kg/h) |
High (300-2000kg/h) |
Adaptability of rubber materials |
Wide (Mooney viscosity 40-120) |
Narrow (Mooney viscosity 40-80) |
Equipment investment |
High (strong drive required) |
Low |
Product precision |
±0.5mm |
±1.0mm |
Special advantages:
- Cold feed models can achieve co-extrusion of colored rubber compounds (such as two-color sealing strips)
- Hot feed models are more suitable for highly filled formulas (such as rubber compounds containing 50% carbon black)
4. Solutions to common problems
Fault phenomenon |
Possible causes |
Handling measures |
Extrusion fluctuation |
Uneven feeding |
Check feeder speed stability |
Surface roughness |
Temperature is too low |
Increase barrel temperature by 5-10℃ |
Scorch phenomenon |
Local overheating |
Clean screw glue and check cooling system |
Production reduction |
Screw wear |
Measure screw outer diameter and repair or replace |