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Screw extruder: Detailed explanation of the core equipment of rubber processing

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