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US3622555A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for producing low bulk density, free-flowing polymer powders

Assignee: Dow Chemical Co
•
Filing: 1969-06-02
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Granted: 1971-11-23
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Expires: 1989-06-02
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Abstract

Abstract Free-flowing powders of normally solid, thermoplastic organic polymers, e.g., polyethylene, having decreased bulk densities are prepared by (1) dispersing a particulate form of the thermoplastic polymer in a nonsolvent liquid medium containing a nonionic wetting agent, (2) heating the resulting dispersion to a temperature from about 10* C. below the Vicat softening point to about the Vicat softening point of the polymer while subjecting the dispersion to agitation and (3) cooling the dispersion under continued agitation. Such powers are useful in flame spraying, fluid-bed coating and the like.

Inventors

  • 👤 Raymand A Rothenbury
  • 👤 Richard W Ford

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 09:38
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/12; C08J3/16

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 13 words
The method according to claim 1 wherein the wetting agent is aliphatic alcohol.
Claim 2
Dependent Claim 11 words
The method according to claim 2 wherein the alcohol is n-propanol.
Claim 3
Dependent Claim 22 words
The method according to claim 2 wherein the medium contains from about 2 to about 20 volume percent of the aliphatic alcohol.
Claim 4
Dependent Claim 14 words
The method according to claim 1 wherein the wetting agent is a polyoxyethylene agent.
Claim 5
Dependent Claim 15 words
The method according to claim 5 wherein the polyoxyethylene agent is an alkyl phenoxypolyoxyethylene ethanol.
Claim 6
Dependent Claim 22 words
The method according to claim 5 wherein the medium contains from about 0.2 to about 0.5 volume percent of the polyoxyethylene agent.
Claim 7
Dependent Claim 13 words
The method according to claim 1 wherein the polymer is an olefin polymer.
Claim 8
Dependent Claim 12 words
The method according to claim 8 wherein the olefin polymer is polyethylene.
Claim 9
Dependent Claim 121 words
The method according to claim 1 comprising the steps of (1) dispersing a finely divided powder of polyethylene in an aqueous medium in proportions such that the medium-to-powder ratio is from about 5:1 to 100:1 by weight, said aqueous medium containing about 2 to about 20 volume percent based on the medium of n-propanol, (2) heating the resulting dispersion to a temperature ranging from about 5* to 2* C. below the Vicat softening point of the polyethylene for at least two minutes while subjecting the dispersion to agitation at a rate only sufficient so that the particles of said powder do not agglomerate and (3) cooling the dispersion under continued agitation until the resulting heat softened particles of said powder harden.
Claim 10
Dependent Claim 241 words
A method according to claim 1 for preparing low bulk density, free-flowing powders of a normally solid, water-insoluble, thermoplastic organic polymer selected from the group consisting of the homopolymers and copolymers of the following monomers; Alpha -olefins, monovinylidene aromatic compounds, alkyl acrylates and derivatives thereof, and vinyl acetate, said method comprising the steps of (1) dispersing a finely divided powder of the normally solid, water-insoluble, thermoplastic organic polymer in a nonsolvent liquid dispersing medium in proportions such that a stirrable slurry results, said dispersing medium containing from about 0.1 to about 100 volume percent based on the volume of the medium of a nonionic wetting agent which is a nonsolvent for the polymer, said agent selected from the group consisting of aliphatic monohydric alcohols, dihydric alcohols, trihydric alcohols, polyhydric alcohols and polyoxyalkylene, the remaining portion of the medium being water, with the proviso that when the wetting agent is a polyoxyalkylene the medium contains from about 0.1 to about 1 volume percent of the wetting agent; (2) heating the resulting dispersion to a temperature ranging from about 10* C. below the Vicat softening point to about the Vicat softening point of the polymer until the particles of said polymer are heat-softened while subjecting the dispersion to agitation at a rate only sufficient so that the particles of said powder do not agglomerate into large masses; and (3) cooling the dispersion under continued agitation until the resulting heat-softened particles of powder harden.
Claim 11
Dependent Claim 67 words
The method according to claim 11 wherein the thermoplastic organic polymer is selected from the group consisting of homopolymers and copolymers of Alpha -olefins and the wetting agent is selected from the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, n-pentanol, cyclohexanol, ethylene glycol, propylene glycol, butylene glycol, glycerol, sorbitol, mannitol, ethylene glycol polyether, ethylene nonyl phenol polyEther, alkyl phenoxypolyoxyethylene ethanol, and propylene glycol fatty acid ester.

References Cited (Backward Citations)

US2870113A Cited
US3422049A Cited
US3101329A Cited
US3432483A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-11-22 1975-05-24 1975-11-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-11-22 1979-05-24 1979-11-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-11-22 1983-05-24 1983-11-23 $7700.00 Window Closed / Lapsed

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