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US5198170A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for extrusion of powered PVC compounds

Assignee: Geon Co
•
Filing: 1992-08-17
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Granted: 1993-03-30
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Expires: 2012-08-17
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Abstract

Abstract This invention discloses an improved method for powder PVC extrusion using particulate PVC resin specified herein which enables smooth, dull surfaces for extrudates under broad processing conditions, in particular at relatively lower shear and temperature. The resins are characterized as having an average particle size ranging from 50 to 125 microns, a DOP porosity of from about 0.27 cc/gm to about 0.5 cc/gm, and a friability rating of 5 or less, preferably 2 or less depending on the stock temperature range during extrusion.

Inventors

  • 👤 Roman B. Hawrylko

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 23:21
CPC Classifications
B; B29; B29B; B29B9/00; B29B9/12; B29B9/02; B29B9/06

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 103 words
In a method for the preparation of pelletized PVC compound from powder, comprising the steps of mixing a polyvinyl chloride resin to form a powder blend and extruding said blend, the improvement comprising employing a PVC resin having a weight average particle size in a range of from 50 microns to 125 microns, a DOP porosity in a range of from about 0.27 cc per gram (cc/gm) of said resin to 0.50 cc/gm, and a resin friability rating of from 0 to 5 and extruding said compound to form pellets at a stock temperature of from about 315° F. to about 350° F.
Claim 2
Dependent Claim 103 words
In a method for the preparation of pelletized PVC compound from powder, comprising the steps of mixing a polyvinyl chloride resin to form a powder blend and extruding said blend, the improvement comprising employing a PVC resin having a weight average particle size in a range of from 50 microns to 125 microns, a DOP porosity in a range of from about 0.27 cc per gram (cc/gm) of said resin to 0.50 cc/gm, and a resin friability rating of from 0 to 5 and extruding said compound to form pellets at a stock temperature of from about 315° F. to about 350° F.
Claim 3
Dependent Claim 83 words
In a method for making an extruded article in an extruder from powder PVC the improvement comprising the step of extruding a powder PVC compound at a stock temperature of from about 350° F. to about 390° F., and employing a particulate polyvinyl chloride resin, wherein said resin has a weight average particle size in a range from 50 microns to 125 microns, a DOP porosity of from 0.27 cc/gm to 0.50 cc/gm, and a resin friability rating of from 0 to 2.
Claim 4
Dependent Claim 83 words
In a method for making an extruded article in an extruder from powder PVC the improvement comprising the step of extruding a powder PVC compound at a stock temperature of from about 350° F. to about 390° F., and employing a particulate polyvinyl chloride resin, wherein said resin has a weight average particle size in a range from 50 microns to 125 microns, a DOP porosity of from 0.27 cc/gm to 0.50 cc/gm, and a resin friability rating of from 0 to 2.
Claim 5
Dependent Claim 13 words
A method of claim 2 wherein said extruder is a single screw extruder.
Claim 6
Dependent Claim 12 words
A method of claim 2 wherein said extruder is a twin-screw extruder.
Claim 7
Dependent Claim 17 words
A method of claim 1 wherein said average particle size is from 60 microns to 115 microns.
Claim 8
Dependent Claim 17 words
A method of claim 5 wherein said average particle size is from 70 microns to 100 microns.
Claim 9
Dependent Claim 121 words
In a method of extruding a louver from a rigid PVC compound comprising the step of extruding said compound in an extruder, the improvement comprising employing a particulate polyvinyl chloride resin having a weight average particle size in a range of from about 50 microns to about 125 microns, a DOP porosity of from 0.27 cc/gm to 0.5 cc/gm, and a resin friability rating of from 0 to 5, wherein: when the stock temperature of extrudate is from about 315° F. to about 350° F., said resin has a friability of 0 to 5, and wherein when said stock temperature of extrudate is from about 350° F. to about 390° F. said resin has a friability of from 0 to 2.
Claim 10
Dependent Claim 121 words
In a method of extruding a louver from a rigid PVC compound comprising the step of extruding said compound in an extruder, the improvement comprising employing a particulate polyvinyl chloride resin having a weight average particle size in a range of from about 50 microns to about 125 microns, a DOP porosity of from 0.27 cc/gm to 0.5 cc/gm, and a resin friability rating of from 0 to 5, wherein: when the stock temperature of extrudate is from about 315° F. to about 350° F., said resin has a friability of 0 to 5, and wherein when said stock temperature of extrudate is from about 350° F. to about 390° F. said resin has a friability of from 0 to 2.
Claim 11
Dependent Claim 17 words
A method of claim 2 wherein said average particle size is from 60 microns to 115 microns.

References Cited (Backward Citations)

US3374296A Cited
US3884607A Cited
US4243629A Cited
US4446086A Cited
US4871498A Cited
US4889673A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1996-03-29 1996-09-28 1997-03-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2000-03-29 2000-09-28 2001-03-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2004-03-29 2004-09-28 2005-03-30 $7700.00 Window Closed / Lapsed

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