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  Plastic processing forums for extrusion information and advice and for other feed screw applications.
  Extrusion, Single Screw
  Reversion/Orientation

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Author Topic:   Reversion/Orientation
swickham
Senior Member

Posts: 7
From:
Registered: May 2005

posted September 01, 2005 07:12 AM     Click Here to See the Profile for swickham   Click Here to Email swickham     Edit/Delete Message   Reply w/Quote
Please could i have feedback on what parameters affect reversion/orientation inthe production of HDPE sheet.

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Tom C
Moderator

Posts: 592
From:Brodheadsville, PA USA
Registered: Jun 2001

posted September 01, 2005 09:26 AM     Click Here to See the Profile for Tom C   Click Here to Email Tom C     Edit/Delete Message   Reply w/Quote
If you want to orient the product, then stretching the melt and freezing it in place is just about the only method. Typically this is associated with oriented film and monofiliment.

I you want to reduce stress in the product the influential items are:

Rate of cooling the product.
Even cooling of the product.
Draw down.
Stress in the die.
Relaxation in the die.

I have also seen tests recently where a unique screw design produces a "Low Stress Melt" which seems to strongly influence the flow and handling characteristics of the product.

I you would like, email the process details to me and I will run an analysis on Compuplast's sheet die and roll cooling software to see anything shows up. This information will be posted here. Specific geometry is not shown.

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Best Regards,

Tom Cunningham

Extrusion Technical Services

www.ExtrusionTechnicalServices.com

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Steve H
Moderator

Posts: 369
From:New Zealand
Registered: Jun 2001

posted September 09, 2005 03:57 PM     Click Here to See the Profile for Steve H   Click Here to Email Steve H     Edit/Delete Message   Reply w/Quote
The size of the rolling bank of melt between the first two chill rollers could be a factor also, you don't want ot have one for HDPE.

Running temps on your chill rolls could be a factor, try running higher temps.

You could also check the speed differential between your chill rollers and pull rollers, too great difference could be a part of the problem.

Tom mentions drawdown, for HDPE your lipset should be 5-10% over the target gauge, and you want as smaller gap between the die lips and the first nip between the chill rollers.

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Steve Hodgson

If at first you don't succeed, skydiving is not for you.

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