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US5480928A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of stable dispersions of ethylene oxide polymers

Assignee: Union Carbide Chemicals and Plastics Technology LLC
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Filing: 1971-12-01
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Granted: 1996-01-02
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Expires: 1991-12-01
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Abstract

Abstract A process for producing a stable dispersion of ethylene oxide polymer which comprises contacting (a) a slurry of granular ethylene oxide polymer in a first inert normally-liquid hydrocarbon diluent, with (b) a second inert, normally-liquid organic diluent such as propylene glycol, and (c) a suspending agent, e.g., silica, (d) under agitation which is sufficient to provide intimate mixing of said ethylene oxide polymer and said suspending agent with said second diluent; and (e) recovering a stable dispersion comprising particulate ethylene oxide polymer and suspending agent in said second diluent.

Inventors

  • 👤 Julius J. Stratta
  • 👤 Julian K. Rose
  • 👤 Herbert J. Paxton, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-10 01:11
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/02; C08J3/09; C08L; C08L71/00; C08L71/02; C08J2371/00; C08J2371/02; Y; Y10; Y10S; Y10S524/00; Y10S524/923; Y10T; Y10T137/00; Y10T137/0318; Y10T137/0391

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 238 words
A process for producing a stable dispersion of ethylene oxide polymer which comprises (a) a slurry of granular ethylene oxide polymer in a first inert normally-liquid hydrocarbon diluent, said polymer having an average molecular weight of at least about 100,000; with (b) a second inert, normally-liquid organic diluent (i) which is a non-solvent for said granular ethylene oxide polymer, (ii) which has a boiling point higher than said first hydrocarbon diluent, (iii) which is composed of carbon, hydrogen, and oxygen atoms, said atoms being of the group consisting of alcoholic hydroxylic oxygen, aliphatic etheric oxygen, and mixtures thereof, and (iv) which is selected from the group consisting of propylene glycol, 1,3-butylene glycol, 1,4-butylene glycol, 1,6-hexylene glycol, ethylene glycol, 2-methylpentane-2,4-diol, octane-1,2diol, dodecanediol, diethylene glycol, dipropylene glycol, dibutylene glycol, glycerol, erythritol, pentaerythritol, 1,1,1-trimethylolethane, glycols, polyoxpropylene glycols, mixed polyoxyethylene-oxypropylene glycols, mono-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxyethylene glycols, and polypropylene glycols, di-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxyethylene glycols, and polypropylene glycols; and (c) a suspending agent which is non-reactive with said ethylene oxide polymer, said first diluent, and said second diluent; (d) under agitation which is sufficient to provide intimate mixing of said ethylene oxide polymer and said suspending agent with said diluent; and (e) recovering a stable dispersion comprising particulate ethylene oxide polymer and suspending agent in second diluent.
Claim 2
Dependent Claim 238 words
A process for producing a stable dispersion of ethylene oxide polymer which comprises (a) a slurry of granular ethylene oxide polymer in a first inert normally-liquid hydrocarbon diluent, said polymer having an average molecular weight of at least about 100,000; with (b) a second inert, normally-liquid organic diluent (i) which is a non-solvent for said granular ethylene oxide polymer, (ii) which has a boiling point higher than said first hydrocarbon diluent, (iii) which is composed of carbon, hydrogen, and oxygen atoms, said atoms being of the group consisting of alcoholic hydroxylic oxygen, aliphatic etheric oxygen, and mixtures thereof, and (iv) which is selected from the group consisting of propylene glycol, 1,3-butylene glycol, 1,4-butylene glycol, 1,6-hexylene glycol, ethylene glycol, 2-methylpentane-2,4-diol, octane-1,2diol, dodecanediol, diethylene glycol, dipropylene glycol, dibutylene glycol, glycerol, erythritol, pentaerythritol, 1,1,1-trimethylolethane, glycols, polyoxpropylene glycols, mixed polyoxyethylene-oxypropylene glycols, mono-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxyethylene glycols, and polypropylene glycols, di-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxyethylene glycols, and polypropylene glycols; and (c) a suspending agent which is non-reactive with said ethylene oxide polymer, said first diluent, and said second diluent; (d) under agitation which is sufficient to provide intimate mixing of said ethylene oxide polymer and said suspending agent with said diluent; and (e) recovering a stable dispersion comprising particulate ethylene oxide polymer and suspending agent in second diluent.
Claim 3
Dependent Claim 33 words
The process of claim 1 wherein there is formed two phases, one phase comprising said first diluent and a second phase comprising said second diluent, said ethylene oxide polymer, and said suspending agent.
Claim 4
Dependent Claim 23 words
The process of claim 1 wherein said ethylene oxide polymer is of the group consisting of poly(ethylene oxide) and ethylene oxide/propylene oxide copolymers.
Claim 5
Dependent Claim 13 words
The process of claim 3 wherein said ethylene oxide polymer is poly(ethylene oxide).
Claim 6
Dependent Claim 322 words
In a catalytic process for producing granular ethylene polymer which has an average molecular weight of at least about 100,000 which comprises polymerizing a monomeric feed comprising ethylene oxide or mixtures comprising ethylene oxide and polymerizable olefin monoxide comonomers; in the presence of a first inert, normally-liquid hydrocarbon diluent in which said monomeric feed is soluble and in which the resulting granular ethylene oxide polymer product is insoluble; at a temperature below about the melting point of said granular ethylene oxide polymer; and for a second period of time sufficient to produce said granular ethylene oxide polymer as a slurry in said first diluent; the improvement which comprises contacting (a) said slurry of granular olefin oxide polymer; with (b) a second inert, normally-liquid organic diluent (i) which is non-solvent for said granular olefin oxide polymer, (ii) which has a boiling point higher than said first diluent, (iii) which is composed of carbon, hydrogen, and oxygen atoms, said atoms being of the group consisting of alcoholic hydroxylic oxygen, aliphatic etheric oxygen, and mixtures thereof, and (iv) which is selected from three group consisting of propylene glycol, 1,3-butylene glycol, 1,4-butylene glycol, 1,6-hexylene glycol, ethylene glycol, 2-methylpentane-2,4-diol, octane-1,2-diol, dodecanediol, diethylene glycol, dipropylene glycol, dibutylene glycol, glycerol, erythritol, pentaerythritol, 1,1,1-trimethylolethane, 1,1,1-trimethylolpropane, polyoxyethylene glycols, polyoxypropylene glycols, mixed polyoxymethylene-oxypropylene glycols, mono-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxethylene glycols, and polypropylene glycols, di-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxethylene glycols, and polypropylene glycols; and (c) a suspending agent which is non-reactive with said ethylene oxide polymer, said first diluent, and said second diluent; (d) under agitation which is sufficient to provide a shear stress of at least 10 dynes/centimeter 2 and in which said oxide polymer is intimately contracted with said diluent; and (e) recovering a stable dispersion comprising particulate ethylene oxide polymer and suspending agent in said diluent.
Claim 7
Dependent Claim 322 words
In a catalytic process for producing granular ethylene polymer which has an average molecular weight of at least about 100,000 which comprises polymerizing a monomeric feed comprising ethylene oxide or mixtures comprising ethylene oxide and polymerizable olefin monoxide comonomers; in the presence of a first inert, normally-liquid hydrocarbon diluent in which said monomeric feed is soluble and in which the resulting granular ethylene oxide polymer product is insoluble; at a temperature below about the melting point of said granular ethylene oxide polymer; and for a second period of time sufficient to produce said granular ethylene oxide polymer as a slurry in said first diluent; the improvement which comprises contacting (a) said slurry of granular olefin oxide polymer; with (b) a second inert, normally-liquid organic diluent (i) which is non-solvent for said granular olefin oxide polymer, (ii) which has a boiling point higher than said first diluent, (iii) which is composed of carbon, hydrogen, and oxygen atoms, said atoms being of the group consisting of alcoholic hydroxylic oxygen, aliphatic etheric oxygen, and mixtures thereof, and (iv) which is selected from three group consisting of propylene glycol, 1,3-butylene glycol, 1,4-butylene glycol, 1,6-hexylene glycol, ethylene glycol, 2-methylpentane-2,4-diol, octane-1,2-diol, dodecanediol, diethylene glycol, dipropylene glycol, dibutylene glycol, glycerol, erythritol, pentaerythritol, 1,1,1-trimethylolethane, 1,1,1-trimethylolpropane, polyoxyethylene glycols, polyoxypropylene glycols, mixed polyoxymethylene-oxypropylene glycols, mono-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxethylene glycols, and polypropylene glycols, di-lower alkyl ethers of ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, polyoxethylene glycols, and polypropylene glycols; and (c) a suspending agent which is non-reactive with said ethylene oxide polymer, said first diluent, and said second diluent; (d) under agitation which is sufficient to provide a shear stress of at least 10 dynes/centimeter 2 and in which said oxide polymer is intimately contracted with said diluent; and (e) recovering a stable dispersion comprising particulate ethylene oxide polymer and suspending agent in said diluent.
Claim 8
Dependent Claim 19 words
The process of claim 5 wherein said second diluent is propylene glycol and wherein said suspending agent is silica.
Claim 9
Dependent Claim 34 words
The process of claim 6 wherein said slurry comprises from about 2 to about 98 weight percent granular ethylene oxide polymer, based on the total weight of said polymer and said first hydrocarbon diluent.

References Cited (Backward Citations)

US2937156A Cited
US3634303A Cited
US3736288A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1999-01-01 1999-07-03 2000-01-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2003-01-01 2003-07-03 2004-01-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2007-01-01 2007-07-03 2008-01-02 $7700.00 Window Closed / Lapsed

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