QUAD/OCTA SCREW EXTRUDER

Technovel Original and Innovative Product
Octa Model "WDR-OT Series"
Quad Model "WDR-QD Series"
  • POINT01
    Best performance in all extruder

    Quad/Octa screw extruder is Technovel new machine that enable kneading that was not possible with twin screw extruder.

  • POINT02
    Solving impossible compounds by multi screw extruder

    "I aim to enhance the blending efficiency."
    "I seek to prolong the residence time."
    "I aspire to optimize the spatial efficiency of equipment installation."
    "I endeavor to reduce torque by shortening the L/D ratio."
    Realizing a compound system in areas unattainable with a twin screw extruder.

Other Features

  • 1
    Improvement of kneading performance
  • 2
    Long time residence
  • 3
    High degassing performance
  • 4
    Volumed feeding system
  • 5
    Maximum dispersibility
  • 6
    Space saving, energy saving

Technical Data

Screw diameter 08, 15, 20, 25, 32, 40, 48, 60, 71, 92
Number of screw QD : Quad screw type
OT : Octa screw type
L / D 15~150
Grade “WDR” series
Screw type NH : Standard depth of screw grove
SH : Deeper screw depth
OT : Other specification
Screw rpm 100~10,000rpm
Multi Screw Extruder QUAD / OCTA | Technovel

Intermeshing Points

More screws mean more intermeshing points

An intermeshing point is where two neighboring screws engage with each other, and the count rises as the number of screws grows.
Each intermeshing point acts as a “redistribution point”: it splits the material flow, transfers part of it to the next screw, and rearranges it.
Kneading proceeds without adding back flow, which disturbs residence time, so strong kneading and a uniform residence time are achieved at the same time.

2 SCREW / TWIN
Intermeshing points 2
4 SCREW / QUAD
Intermeshing points 6
8 SCREW / OCTA
Intermeshing points 14

* The dark points in the diagram mark the intermeshing points. For N screws, the count is 2 × (N − 1): 2 screws give 2, 4 screws give 6, 8 screws give 14.

Free Volume & Heat Transfer Area

3.65 times the volume, 3.3 times the heat transfer area

Taking a twin screw extruder of the same screw diameter as 1, the quad screw has 1.88 times the free volume and 1.75 times the heat transfer area, and the octa screw has 3.65 times the free volume and 3.3 times the heat transfer area.
In a multi screw extruder, the heat transfer area grows almost in proportion to the volume, so temperature control capability is maintained even when the output is increased.
Because of this characteristic, adding screws can also be one of the options for scale up, alongside the conventional approach of enlarging the screw diameter.

4 SCREW / QUAD
vs. twin screw of the same diameter
Free volume
×1.88
Heat transfer area
×1.75
8 SCREW / OCTA
vs. twin screw of the same diameter
Free volume
×3.65
Heat transfer area
×3.3
Reference: Enlarged Twin Screw
When the same volume (×3.65) is obtained by enlarging the screw diameter
Free volume
×3.65
Heat transfer area
approx. ×2.4

* Ratios with a twin screw extruder of the same screw diameter and the same process length taken as 1 (calculated values based on our standard screw geometry)
* When the diameter is enlarged, the heat transfer area increases only with the 2/3 power of the volume (3.652/3 ≈ 2.4)
* A larger screw diameter also means a deeper screw channel, so the heat transfer distance into the molten resin becomes longer
  With a multi screw design, the volume is increased without deepening the channel, which keeps the increase in heat transfer distance small

Applications

Process tasks suited to multi screw extruders

Strong kneading capability, large free volume, good temperature control, and a uniform residence time.
The shear level can be set over a wide range, from intense dispersive kneading to mild kneading, and the large heat transfer area gives better temperature control than a conventional twin screw extruder, so the application range extends to heat sensitive materials.
Here we map these multi screw characteristics by asking “which strength belongs in which process.”

Reactive Processing
Making use of a long and uniform residence time
Reactive Extrusion / Continuous Polymerization Uniform Reaction History / Narrow Residence Time Distribution Grafting / Compatibilization / Dynamic Crosslinking (TPV) Chemical Recycling / Depolymerization / Monomerization Equilibrium Shift by Combined Devolatilization (Condensation / Depolymerization) Reaction Control with Catalysts and Additives
Devolatilization / Degassing / Deodorization
Combining free volume with surface renewal
Multistage Vent Continuous Degassing Removal of Residual Monomer / Solvent Devolatilization of Highly Viscous Systems Enhanced Devolatilization through Surface Renewal
Dispersive Mixing of Highly Viscous and Hard to Disperse Materials
Strong kneading force from many intermeshing points
Very high molecular weight materials such as UHMWPE Super Engineering Plastics (PEEK / PPS / LCP / PEI) Highly Filled Compounds Highly Viscous, Poorly Flowing Materials
Dispersion of Nano and Functional Fillers
Shear set to the task: from high speed dispersion to distributive mixing
Graphene / Graphite Dispersion CNT / Nanocellulose (CNF) Higher Strength and Wear Resistance
Low Temperature, Low Damage Processing
Responsive temperature control from a large heat transfer area
Biomass Plastics (PLA) Cellulose Composites (CNF / Natural Fiber) Low Temperature Kneading of Heat Sensitive Materials Material Recycling / Recycled Compounds
Scale Up
Kneading secured by intermeshing points even at low screw speed, keeping shear down
Scale Up from Twin Screw to Multi Screw for Mass Production Low Screw Speed with the Required Kneading Secured Reduction of Shear Heating Mass Production of Heat and Shear Sensitive Materials