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US3997624A Expired / Lapsed US ⏱️ 0.0 years remaining

Polyethylene waxes

Assignee: Princeton Polymer Laboratories Inc
•
Filing: 1975-10-01
•
Granted: 1976-12-14
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Expires: 1995-10-01
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Abstract

Abstract Low molecular weight ethylene homo and copolymer waxes are prepared at pressures below 1000 psi and at temperatures below 120° C. using free radical catalysts having 10-hour half-lifes at not over 60° C.

Inventors

  • 👤 Donald E. Hudgin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 15:58
CPC Classifications
C; C08; C08F; C08F210/00; C08F210/02; Y; Y10; Y10S; Y10S585/00; Y10S585/929; Y10S585/946

Claims Analysis

Total Claims: 28
Claim 1
Independent Claim 149 words
A process of preparing an ethylene polymer wax having a molecular weight of 1,000 to 10,000 consisting essentially of polymerizing a member of the group consisting of (1) ethylene and (2) a mixture of ethylene with a copolymerizable monomer selected from the group consisting of vinyl acetate, acrylic acid, methacrylic acid, maleic anhydride and a copolymerizable alpha monoolefin, said monomers being present in an amount to provide not over 50 mol % of the polymer units, in the presence of a free radical forming catalyst having a 10-hour half life at 30° to 60° C., said polymerization being carried out at a temperature of 20° to 120° C. and a pressure of 300 to 900 psi and in an inert or chain transfer solvent having a molecular weight of not over 200 and selected from the group consisting of hydrocarbons, ethers, carboxylic acid esters and ketones and mixtures thereof.
Claim 2
Dependent Claim 149 words
A process of preparing an ethylene polymer wax having a molecular weight of 1,000 to 10,000 consisting essentially of polymerizing a member of the group consisting of (1) ethylene and (2) a mixture of ethylene with a copolymerizable monomer selected from the group consisting of vinyl acetate, acrylic acid, methacrylic acid, maleic anhydride and a copolymerizable alpha monoolefin, said monomers being present in an amount to provide not over 50 mol % of the polymer units, in the presence of a free radical forming catalyst having a 10-hour half life at 30° to 60° C., said polymerization being carried out at a temperature of 20° to 120° C. and a pressure of 300 to 900 psi and in an inert or chain transfer solvent having a molecular weight of not over 200 and selected from the group consisting of hydrocarbons, ethers, carboxylic acid esters and ketones and mixtures thereof.
Claim 3
Dependent Claim 16 words
The process of claim 1 wherein the reaction is carried out at 40° to 120° C.
Claim 4
Dependent Claim 16 words
The process of claim 2 wherein the reaction is carried out at 40° to 70° C.
Claim 5
Dependent Claim 13 words
The process of claim 3 wherein the pressure is 600 to 900 psi.
Claim 6
Dependent Claim 12 words
The process of claim 1 wherein the catalyst is a peroxy catalyst.
Claim 7
Dependent Claim 24 words
The process of claim 5 wherein the solvent is selected from the group consisting of a hydrocarbon and a heterocyclic ether and mixtures thereof.
Claim 8
Dependent Claim 28 words
The process of claim 6 wherein the solvent is selected from the group consisting of hexane, benzene, propylene oxide, tetrahydrofuran, dioxolane and a mixture of hexane and tetrahydrofuran.
Claim 9
Dependent Claim 10 words
The process of claim 7 wherein the solvent is tetrahydrofuran.
Claim 10
Dependent Claim 10 words
The process of claim 8 wherein said member is ethylene.
Claim 11
Dependent Claim 13 words
The process of claim 9 wherein the temperature is 40° to 70° C.
Claim 12
Dependent Claim 13 words
The process of claim 10 wherein the pressure is 600 to 900 psi.
Claim 13
Dependent Claim 12 words
The process of claim 11 wherein the catalyst is t-butyl peroxy pivalate.
Claim 14
Dependent Claim 14 words
The process of claim 7 wherein the catalyst is dicyclohexylperoxydicarbonate or t-butyl peroxy pivalate.
Claim 15
Dependent Claim 10 words
The process of claim 1 wherein said member is ethylene.
Claim 16
Dependent Claim 22 words
The process of claim 14 wherein the solvent is a hydrocarbon or a cyclic ether and the catalyst is a peroxy catalyst.
Claim 17
Dependent Claim 13 words
The process of claim 15 wherein the temperature is 40° to 70° C.
Claim 18
Dependent Claim 17 words
The process of claim 1 wherein said member is a mixture of ethylene and said copolymerizable monomer.
Claim 19
Dependent Claim 22 words
The process of claim 17 wherein the solvent is a hydrocarbon or a cyclic ether and the catalyst is a peroxy catalyst.
Claim 20
Dependent Claim 13 words
A process of claim 18 wherein the temperature is 40° to 70° C.
Claim 21
Dependent Claim 39 words
The process of claim 1 wherein the solvent is an alkane, cycloalkane, aromatic hydrocarbon free of non-benzenoid unsaturation or a cyclic ether having 3 to 6 atoms in the ring of which 1 to 2 are ether oxygen atoms.
Claim 22
Dependent Claim 28 words
The process of claim 1 wherein (2) is a mixture of ethylene with (a) vinyl acetate, (b) acrylic acid, (c) methacrylic acid, (d) maleic anhydride or (e) propylene.
Claim 23
Dependent Claim 10 words
The process of claim 21 wherein said member is (2).
Claim 24
Dependent Claim 15 words
The process of claim 1 wherein the catalyst is a peroxy catalyst or azo catalyst.
Claim 25
Dependent Claim 12 words
The process of claim 23 wherein the catalyst is an azo catalyst.
Claim 26
Dependent Claim 10 words
The process of claim 24 wherein the catalyst is 2-6-butylazo-2-cyano-4-methoxy-4-methylpentane.
Claim 27
Dependent Claim 30 words
The process of claim 1 wherein the solvent is selected from the group consisting of a hydrocarbon, a heterocyclic ether, a ketone and a carboxylic acid ester and mixtures thereof.
Claim 28
Dependent Claim 31 words
The process of claim 26 wherein the solvent is selected from the group consisting of hexane, benzene, propylene oxide, tetrahydrofuran, dioxolane, acetone, ethyl acetate and a mixture of hexane and tetrahydrofuran.

References Cited (Backward Citations)

US3714135A Cited
US3835107A Cited
US3862257A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-12-14 1980-06-14 1980-12-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-12-14 1984-06-14 1984-12-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-12-14 1988-06-14 1988-12-14 $7700.00 Window Closed / Lapsed

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