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  Material out of vent

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Author Topic:   Material out of vent
wiseguynj
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Posts: 1
From:
Registered: Jun 2001

posted June 05, 2001 01:14 PM     Click Here to See the Profile for wiseguynj   Click Here to Email wiseguynj     Edit/Delete Message   Reply w/Quote
Running a 4/2" 32:1 DS with RRVC powder have material coming out of the vent, it has never happened before, have any idea what is going on?

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admin2
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Posts: 15
From:fl
Registered: Jun 2001

posted June 05, 2001 03:08 PM     Click Here to See the Profile for admin2   Click Here to Email admin2     Edit/Delete Message   Reply w/Quote
Should really check discharge pressure, screw speed, screw profile and zone settings. Typically, vent flow can be reduced with clean screens (you aren't running with any on RPVC are you?), higher screw speeds or lower barrel discharge zone settings. The fact that it occured suddenly reeks of contamination and high discharge pressures...

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louis33
Senior Member

Posts: 146
From:Allentown, PA - USA
Registered: Jun 2001

posted June 06, 2001 09:05 PM     Click Here to See the Profile for louis33     Edit/Delete Message   Reply w/Quote
quote:
Originally posted by wiseguynj:
Running a 4/2" 32:1 DS with RRVC powder have material coming out of the vent, it has never happened before, have any idea what is going on?

The simple answer is a higher pressure in the discharge section of the screw. The complicated answer depends on what you find caused that!

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2beeps
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Posts: 111
From:Silver City, NM, USA
Registered: Jun 2001

posted July 01, 2001 06:32 PM     Click Here to See the Profile for 2beeps   Click Here to Email 2beeps     Edit/Delete Message   Reply w/Quote
Hi wiseguynj,

A few more thoughts to throw "in the hopper"
In running RPVC, depending on die opening (i.e thin or thick walled pipe), and orifice opening in adapter,I'd first want to know my exit melt temperature.If it's on the high side of 400F, NEXT string-up would call for a larger orifice insert. I would first play with screw oil temp.--increasing to equal or slightly above metering zone temp., to try to reduce melt viscosity and lower front end and head pressures, allowing faster flow through head and die, which should relieve vent flow.
You may have to lower crammer speed some while these adjustments are going on, then you can increase crammer to just below vent flow to maximize output rates.
Having said all of this, I'm assuming your formulation is well balanced to your extruder (lube balance,process aid, etc.?)
Also, if this "never happened before", were any blending room mistakes sent to your silo?? I highly recommend a Brabender fusion/stability curve be run--not on EVERY batch out of the mixer, but at least six or eight times during an eight hour shift!

Regards,
Skip

[This message has been edited by 2beeps (edited 07-01-2001).]

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