US3622555A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for producing low bulk density, free-flowing polymer powders
Assignee: Dow Chemical Co
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Filing: 1969-06-02
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Granted: 1971-11-23
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Expires: 1989-06-02
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)
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 |