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US4407987A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymeric resins and blends with high packing densities

Assignee: Geon Co
•
Filing: 1981-10-27
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Granted: 1983-10-04
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Expires: 2001-10-27
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Abstract

Abstract A powder blend of rigid polyvinyl chloride resin having higher packing densities than previously known is disclosed. The higher packing densities provide improved physical properties and production rates. There is also disclosed a process for the manufacture of a powder blend of suitable thermoplastic polymer resins having high packing densities for processing into articles. The process includes mixing and thermokinetically heating a batch of powder blend in a high intensity mixer having a plurality of blades attached to arms rotating about an axis with a blade tip speed of at least about 25 meters/second to a predetermined temperature below commencement of agglomeration, and cooling the batch in a high intensity mixer having a plurality of blades attached to arms rotating about an axis with a blade tip speed less than about 16 meters/second but sufficient to attain high packing densities, to a temperature at which the batch can be stored without agglomeration occuring.

Inventors

  • 👤 Zenas Crocker
  • 👤 David V. Wise

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 05:31
CPC Classifications
B; B29; B29B; B29B7/00; B29B7/80; B29B7/82; B01; B01F; B01F35/00; B01F35/20; B01F35/22; B01F35/221; B01F35/2214; B01F35/22142; B01F35/221421; B01F35/2215; B01F35/2216; B01F35/22161; B29B13/00; B29B13/04; B29B13/045; B29B7/002; B29B7/005; B29B7/02; B29B7/06; B29B7/10; B29B7/12; B29B7/16; C; C08; C08J; C08J3/00; C08J3/20; C08J3/203; B29K; B29K2105/00; B29K2105/0005; B29K2105/0032; B29K2105/06; B29K2105/16; B29K2105/25; B29K2105/251

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 161 words
In a process for the manufacture of a particulate polymeric resin blend suitable for forming plastic articles in which a particulate composition comprising a thermoplastic polymeric resin is mixed and thermokinetically heated in a high intensity mixer having a plurality of blades attached to arms rotating with a blade tip speed of at least about 25 meters per second to effect blending of the composition and heating thereof to an elevated temperature below commencement of agglomeration of the particulate composition, and in which the blended and heated particulate composition is cooled in a mixer to a temperature at which the particulate composition can be stored without agglomeration, the improvement wherein the blend and heated particulate composition is cooled in a high intensity mixer with blades attached to arms rotating in said mixer, said arms being rotated at a blade tip speed of not more than 16 meters per second whereby the particulate cooled polymeric resin blend has a high packing density.
Claim 2
Dependent Claim 161 words
In a process for the manufacture of a particulate polymeric resin blend suitable for forming plastic articles in which a particulate composition comprising a thermoplastic polymeric resin is mixed and thermokinetically heated in a high intensity mixer having a plurality of blades attached to arms rotating with a blade tip speed of at least about 25 meters per second to effect blending of the composition and heating thereof to an elevated temperature below commencement of agglomeration of the particulate composition, and in which the blended and heated particulate composition is cooled in a mixer to a temperature at which the particulate composition can be stored without agglomeration, the improvement wherein the blend and heated particulate composition is cooled in a high intensity mixer with blades attached to arms rotating in said mixer, said arms being rotated at a blade tip speed of not more than 16 meters per second whereby the particulate cooled polymeric resin blend has a high packing density.
Claim 3
Dependent Claim 32 words
A process according to claim 1 wherein said particulate resin blend comprises at least one additive selected from the group consisting of processing aids, lubricants, stabilizers, antioxidants, impact modifiers, fillers and pigments.
Claim 4
Dependent Claim 27 words
A process according to claim 1 wherein the blade tip speed is in the range of about 25 to 45 meters/second for the mixing and heating step.
Claim 5
Dependent Claim 18 words
A process according to claim 1 wherein the mixing and heating step is less than about 20 seconds.
Claim 6
Dependent Claim 16 words
A process according to claim 1 wherein the cooling step is less than about 40 seconds.
Claim 7
Dependent Claim 22 words
A process according to claim 1 wherein the mixing and heating step and cooling step occur in the same high intensity mixer.
Claim 8
Dependent Claim 14 words
A powder blend comprising rigid polyvinyl chloride made by the process of claim 1.
Claim 9
Dependent Claim 12 words
A process according to claim 1 wherein said resin comprises polyvinyl chloride.
Claim 10
Dependent Claim 35 words
A process according to claim 8 wherein the temperature to which said batch is mixed and heated is below 200 C. and the temperature to which said batch is cooled is below about 60 C.
Claim 11
Dependent Claim 32 words
A process according to claim 8 wherein said particulate resin blend comprises at least one additive selected from the group consisting of processing acids, lubricants, stabilizers, antioxidants, impact modifiers, fillers and pigments.

References Cited (Backward Citations)

CA813775A Cited
US3263980A Cited
US3229002A Cited
US3472491A Cited
US4049593A Cited
US3957723A Cited
US4046728A Cited
US4230615A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-10-03 1987-04-04 1987-10-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-10-03 1991-04-04 1991-10-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-10-03 1995-04-04 1995-10-04 $7700.00 Window Closed / Lapsed

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