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US5246779A Expired / Lapsed US ⏱️ 0.0 years remaining

Microfine propylene polymer powders and process for their preparation

Assignee: Equistar Chemicals LP
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Filing: 1992-08-10
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Granted: 1993-09-21
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Expires: 2012-08-10
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Abstract

Abstract The present invention is directed to improved microfine propylene polymer powders having reduced fines which are comprised of spherical or substantially spherical particles and have a number average particle size from about 25 to about 60. A process for preparing the improved powders is also provided. The process involves dispersing a molten propylene homopolymer or copolymer which has been visbroken in a liquid medium in the presence of a nonionic surfactant, cooling the dispersion below the melt point of the propylene polymer and recovering the powder.

Inventors

  • 👤 Manfred Heimberg
  • 👤 Daniel J. Ondrus

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 23:13
CPC Classifications
C; C08; C08F; C08F8/00; C08F8/50; B; B29; B29C; B29C48/00; B29C48/25; B29C48/92; B29C2948/00; B29C2948/92; B29C2948/92504; B29C2948/92704; B29C48/022; B29C48/36; B29C48/395; C08F2800/00; C08F2800/20; C08F2810/00; C08F2810/10; Y; Y10; Y10S; Y10S525/00; Y10S525/938; Y10T; Y10T428/00; Y10T428/29; Y10T428/2982

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 152 words
In a process for producing propylene polymer powders comprising the steps of: (1) heating a propylene polymer to above the melt point of the polymer with a nonionic surfactant which is a block copolymer of ethylene oxide and propylene oxide and a polar liquid medium which is not a solvent for the propylene polymer; said nonionic surfactant present in an amount from 4 to 50 percent, based on the weight of the propylene polymer, and the weight ratio of said polar liquid medium to propylene polymer ranging from 0.5:1 to 10:1; (2) dispersing the mixture to produce droplets of the desired size; (3) cooling the dispersion to below the melt point of the propylene polymer; and (4) recovering the propylene polymer powder; to obtain powders having reduced fines and improved particle size distribution; the improvement wherein the propylene polymer is a visbroken propylene polymer having a melt flow rate greater than 1.
Claim 2
Dependent Claim 152 words
In a process for producing propylene polymer powders comprising the steps of: (1) heating a propylene polymer to above the melt point of the polymer with a nonionic surfactant which is a block copolymer of ethylene oxide and propylene oxide and a polar liquid medium which is not a solvent for the propylene polymer; said nonionic surfactant present in an amount from 4 to 50 percent, based on the weight of the propylene polymer, and the weight ratio of said polar liquid medium to propylene polymer ranging from 0.5:1 to 10:1; (2) dispersing the mixture to produce droplets of the desired size; (3) cooling the dispersion to below the melt point of the propylene polymer; and (4) recovering the propylene polymer powder; to obtain powders having reduced fines and improved particle size distribution; the improvement wherein the propylene polymer is a visbroken propylene polymer having a melt flow rate greater than 1.
Claim 3
Dependent Claim 26 words
The process of claim 1 wherein the propylene polymer is a homopolymer of propylene or a copolymer of propylene with up to 25 weight percent ethylene.
Claim 4
Dependent Claim 18 words
The process of claim 2 wherein the propylene polymer has a crystallinity content from 40 to 75 percent.
Claim 5
Dependent Claim 22 words
The process of claim 2 wherein the melt flow rate of the visbroken propylene polymer is from 2 up to about 100.
Claim 6
Dependent Claim 21 words
The process of claim 4 wherein the propylene polymer is visbroken by contacting with an organic peroxide at an elevated temperature.
Claim 7
Dependent Claim 21 words
The process of claim 4 wherein the visbroken propylene polymer is polypropylene having a melt flow rate from 2 to 40.
Claim 8
Dependent Claim 14 words
The process of claim 6 wherein the melt flow rate is 5 to 35.
Claim 9
Dependent Claim 32 words
The process of claim 4 wherein the visbroken propylene polymer is a random copolymer of propylene and 1 to 10 weight percent ethylene having a melt flow rate from 2 to 40.
Claim 10
Dependent Claim 14 words
The process of claim 8 wherein the melt flow rate is 5 to 35.
Claim 11
Dependent Claim 16 words
The process of claim 9 wherein the random copolymer contains 1 to 5 weight percent ethylene.
Claim 12
Dependent Claim 42 words
A visbroken propylene polymer microfine powder comprised of particles which are spherical or substantially spherical in shape and having a number average particle size from 25 to 60 microns and wherein particles under 10 microns in size do not exceed 10 percent.
Claim 13
Dependent Claim 42 words
A visbroken propylene polymer microfine powder comprised of particles which are spherical or substantially spherical in shape and having a number average particle size from 25 to 60 microns and wherein particles under 10 microns in size do not exceed 10 percent.
Claim 14
Dependent Claim 37 words
The microfine powder of claim 11 wherein the propylene polymer is a homopolymer of polypropylene or a copolymer of polypropylene with up to 25 weight percent ethylene visbroken to a melt flow rate of 2 to 100.
Claim 15
Dependent Claim 19 words
The microfine powder of claim 12 wherein the propylene polymer has a crystallinity content from 40 to 75 percent.
Claim 16
Dependent Claim 21 words
The microfine powder of claim 12 wherein the propylene polymer is polypropylene having a melt flow rate from 2 to 40.
Claim 17
Dependent Claim 32 words
The microfine powder of claim 12 wherein the propylene polymer is a random copolymer of propylene and 1 to 10 weight percent ethylene having a melt flow rate from 2 to 40.
Claim 18
Dependent Claim 17 words
The microfine powder of claim 12 having a number average particle size from 30 to 50 microns.
Claim 19
Dependent Claim 18 words
The microfine powder of claim 16 wherein particles under 10 microns in size do not exceed 5 percent.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1996-09-20 1997-03-22 1997-09-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2000-09-20 2001-03-22 2001-09-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2004-09-20 2005-03-22 2005-09-21 $7700.00 Window Closed / Lapsed

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