Author
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Topic: compounding POM
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schou Member Posts: 1 From:Esbjerg, Denmark Registered: May 2002
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posted May 19, 2002 04:56 PM
What is the best screw dimension for compounding POM. Also, I have heard that nonvented extruders are best for POM. Is this true?IP: Logged |
Tom C Moderator Posts: 531 From:Brodheadsville, PA USA Registered: Jun 2001
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posted May 19, 2002 09:22 PM
POM can be difficult to handle. If it is overheated it will break dowm and release formaldehyde. Copolymer is more stable than homopolymer versions. In extrusion, and extrusion compounding, everthing plays a role in the process not only the screw geometry. This is why I am a proponent of simulation as a tool in helping to design a process. For POM a couple of basic suggestions: 1) Low barrels temperatures. Degradation is difficult to control becasue the degradation temperatures are only slightly above the melt temperature. 2) Low screw speed. Lower it even more if formaldehyde is a problem. 3) Deep screw channels lower shear rates and temperature buildup. Shallow channels provide more temperature control. What is best depends on the material, extruder specifications, and type of optimization required. Feeding, melting and mixing only add more dimensions to the screw geometry issue. Extrusion (especially resins like POM) isn't for the faint hearted (or those with sensitive noses.) Warning!!! The level of formaldehyde vapors coming off a POM extrusion which is improperly run can be dangerous! Be sure proper personal protective gear is used while developing a process. Tom C
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lianis Senior Member Posts: 9 From: Registered: May 2005
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posted May 27, 2005 11:13 AM
testIP: Logged |
lianis Senior Member Posts: 9 From: Registered: May 2005
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posted May 27, 2005 11:30 AM
testIP: Logged |
lianis Senior Member Posts: 9 From: Registered: May 2005
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posted May 27, 2005 11:30 AM
testIP: Logged |
lianis Senior Member Posts: 9 From: Registered: May 2005
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posted May 27, 2005 11:42 AM
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