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Extrusion guide TP HFFR

This guide applies to our thermoplastic halogen free flame retardant (HFFR) products including the following grades:

TP519C, TP521, TP536, TP543, TP568, CT08-93, CT09-07, CT09-12

 Equipment
 
   Extruder Ideally 20 to 24 L/D ratio.
     
   Extruder head Ideally with deep flow channels.  A head assembly with a diverter valve is beneficial.
     
   Screw Low compression less than 1.5:1 and ideally 1.2:1.
     
   Extension piece If there is an extension piece connecting the end of the extruder and head then this needs to be heated to 160oC by heater bands or similar.
     
   Tooling Pressure Ring die should be the same size or slightly smaller than the final cable diameter.  Short land length; no longer than 3mm.  The flow path should be as gentle as possible with the adequate separation of the core and ring die. 
     
   Tubing Double taper designs are preferred.  Draw down ratios of no greater than 1.5:1 is recommended.
     
     
 Processing conditions
 
   Drying Generally not necessary unless the material is exposed to the atmosphere for a long period of time.  In this case, it can be dried in a dehumidifying drier.
     
   Temperature profile Ranging from 125 to 160oC from the feed to the end of the extruder with 165oC on the head and 165oC on the die.
     
   Melt temperature Aim for between 160oC and 170oC. 
     
   Colour masterbatches Those from PW Hall are recommended.

 

Troubleshooting guide

  Problem

Cause 

Solution 

     
Poor surface finish             Temperature low   Increase barrel and head temperatures
Use higher shear screw
Melt fracture  

Increase barrel and head temperatures

Use lower draw-down ratio
Reduce extrusion rate
Extrusion O/D too low  Reduce haul off speed
Change to smaller die (run with slight die swell)
Improper filling of the die Use smaller size die 
     

Porosity 

Compound wet  Vacuum dry, replace material 
Colour masterbatch wet Vacuum dry, replace material 
Melt temperature too high (decomposition of fillers)  Reduce barrel temperatures 
Use lower shear screw
Check heating and cooling equipment
     
Surging extrudate Insufficient back pressure in extruder Increase gauze packing
Screw speed too high Reduce screw speed 
Porosity in extrudate See above 
     
Die drool Low moecular weight material exuding during extrusion Use highly polished die/point
Add 1-2% process aid
     
High motor amps Is motor rating sufficient?  Upgrade motor
Incorrect screw design Use lower shear/compression design
Gauze pack too harsh Remove some/all gauzes
Head design restrictive Change head design
Material too stiff Increase temperature profile
Check heater bands/thermocouples
Use higher MFI material
     
High shrinkage Draw-down too high  Reduce draw-down
Vacuum too high Reduce vacuum

 

© AEI Compounds Limited, Great Stonar House, Sandwich Industrial Estate, Sandwich, Kent, CT13 9LY
   
Telephone   +44 (0) 1304 616171                Facsimile   +44 (0) 1304 616170   
Email          sales@aeicompounds.co.uk      Website     www.aeicomppounds.co.uk
        
Whilst this document has been prepared in good faith, AEI Compounds Limited accepts no liability of any kind to any person in respect of its contents or any use made thereof. Neither must it be assumed that any use will not infringe any patent. This document shall not form part of any contract with a customer.