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  Cause of extrusion instability

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Author Topic:   Cause of extrusion instability
greg.barnes
Member

Posts: 4
From:Carrollton, GA, USA
Registered: Nov 2005

posted November 23, 2005 08:38 AM     Click Here to See the Profile for greg.barnes   Click Here to Email greg.barnes     Edit/Delete Message   Reply w/Quote
Can extrusion die diameter and tip land length cause surges when extruding natural HDPE? An engineer in our office says that our tooling geometry is causing pressure fluctuations and random OD variations. I do not buy in. HDPE extrudate seems to be like a battleship: once it starts moving it does not want to stop. I think it is more likely that there is something under the extrudate (like moisture) causing the lumps.

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Greg Barnes

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Tom C
Moderator

Posts: 657
From:Brodheadsville, PA USA
Registered: Jun 2001

posted November 23, 2005 09:12 AM     Click Here to See the Profile for Tom C   Click Here to Email Tom C     Edit/Delete Message   Reply w/Quote
With the use of a pressure gauge and a chart recorder you can see any short and long term pressure variations that come from the screw.

From what you are describing it seems as if you are having very short term variations of flow. This can be caused by high shear stress in the die, known as melt fracture and shark skin.

As you mentioned moisutre can cause surface defects, as can entrianed air and unmelted pellets.

Section the defect and look at it under a microscope. This may give you a clue as to the source.

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Best Regards,

Tom Cunningham

Extrusion Technical Services

www.ExtrusionTechnicalServices.com

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greg.barnes
Member

Posts: 4
From:Carrollton, GA, USA
Registered: Nov 2005

posted November 23, 2005 03:56 PM     Click Here to See the Profile for greg.barnes   Click Here to Email greg.barnes     Edit/Delete Message   Reply w/Quote
It does not appear to be sharkskin. I saw that before when a die heater was going bad. The surface in this case is smooth to the touch. The OD will suddenly go up and then drop back down to nominal, apparently at random. The cable jacket kind of looks like a python swallowing a rat. We have not yet been able to section a sample because we always make repairs and send the product on. It does cause delays, however.

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Tom C
Moderator

Posts: 657
From:Brodheadsville, PA USA
Registered: Jun 2001

posted November 24, 2005 09:06 AM     Click Here to See the Profile for Tom C   Click Here to Email Tom C     Edit/Delete Message   Reply w/Quote
Barrier screw or conventional screw?

Mixer on the screw?

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Best Regards,

Tom Cunningham

Extrusion Technical Services

www.ExtrusionTechnicalServices.com

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greg.barnes
Member

Posts: 4
From:Carrollton, GA, USA
Registered: Nov 2005

posted November 28, 2005 08:29 AM     Click Here to See the Profile for greg.barnes   Click Here to Email greg.barnes     Edit/Delete Message   Reply w/Quote
This is a barrier screw and there is no mixer. The OD goes up several millimeters (on a 25 mm tube) within a 2 or 3 cm area.

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Tom C
Moderator

Posts: 657
From:Brodheadsville, PA USA
Registered: Jun 2001

posted November 28, 2005 10:12 AM     Click Here to See the Profile for Tom C   Click Here to Email Tom C     Edit/Delete Message   Reply w/Quote
First you should check some standard stuff before we get into the more exotic.

1) Are your extruder RPMs steady?
2) Is your haul of equipment steady?
3) Is the screw or barrel worn?
4) What is the diameter of the extruder, the RPMs and the output rate? This will help to decide if the screw is operating in normal ranges
5) Is the extruder vented?
6) Did we establish that you have a pressure gauge on the extruder? If so what pressure? Do you see pressure fluctuations?

Sorry for so many requests, but this is what it takes sometimes.

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Best Regards,

Tom Cunningham

Extrusion Technical Services

www.ExtrusionTechnicalServices.com

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louis33
Senior Member

Posts: 140
From:Allentown, PA - USA
Registered: Jun 2001

posted December 05, 2005 12:23 PM     Click Here to See the Profile for louis33     Edit/Delete Message   Reply w/Quote
Seems that you are extruding over a cable. That being the case, moisture will cause that problem or volatiles (out gassing) I suspect that you do not have a true "surge" in output, especially if it is in a very short section. That kind of output variation would be very noticeable on the gages of the machine was it to occur.

Of course, any interruption in the feed rate of the wire versus the feed rate of the material would show up as a "surge" in the product OD. Check the payout and take-up devices if you have not already done so.

Oh, almost forgot, yes, the tooling if it is not sized correctly will cause a similar problem. The Draw Down Balance should be on the positive side. Too high will cause tearing of the melt, too low might put you in a borderline area where slight changes in wire speed cause those short sections of BUMPS.

Sounds like tooling or payout/takeup from where I sit.


[This message has been edited by louis33 (edited December 05, 2005).]

[This message has been edited by louis33 (edited December 05, 2005).]

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greg.barnes
Member

Posts: 4
From:Carrollton, GA, USA
Registered: Nov 2005

posted December 05, 2005 12:58 PM     Click Here to See the Profile for greg.barnes   Click Here to Email greg.barnes     Edit/Delete Message   Reply w/Quote
Thanks, everyone! We measured the head pressure Friday and it was fluctuating a good bit. Then, we did a trial with different tooling and found a combo (with a positive balance if I am calculating it correctly) that reduced the pressure fluctuations at least 50%. Now we are running with the tooling and will see how it works. Interesting enough, this did not happen on every cable. It was about every 15th cable, which was a nuisance. Fortunately, we were able to make repairs 99% of the time.

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mademan5284
Senior Member

Posts: 23
From:Easton, Pa U.S.A.
Registered: Aug 2005

posted December 07, 2005 02:34 PM     Click Here to See the Profile for mademan5284   Click Here to Email mademan5284     Edit/Delete Message   Reply w/Quote
Make sure your tip is not protruding past your die.

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