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Method for the controlled polymerization of polyphenylene oxide polymers

Assignee: General Electric Co
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Filing: 1977-12-29
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Granted: 1980-04-01
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Expires: 1997-12-29
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Abstract

Abstract A novel process is described for the control of molecular weight in the preparation of polyphenylene oxide polymers. The process is based on the slow addition of additional amounts of a monomeric phenol to a polyphenylene oxide polymerization reaction mixture which comprises a main charge of a monomeric phenol, a polyphenylene oxide polymerization catalyst and a solvent, while continuing polymerization.

Inventors

  • 👤 James G. Bennett, Jr.
  • 👤 Glenn D. Cooper

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 18:47
CPC Classifications
C; C08; C08G; C08G65/00; C08G65/34; C08G65/38; C08G65/44

Claims Analysis

Total Claims: 26
Claim 1
Independent Claim 87 words
A process for preparation of polyphenylene oxide polymer having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of a phenolic monomer, an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture an additional amount of phenolic monomer at a rate that is sufficient to control polymerization and producing a polyphenylene oxide polymer of a predetermined molecular weight.
Claim 2
Dependent Claim 87 words
A process for preparation of polyphenylene oxide polymer having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of a phenolic monomer, an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture an additional amount of phenolic monomer at a rate that is sufficient to control polymerization and producing a polyphenylene oxide polymer of a predetermined molecular weight.
Claim 3
Dependent Claim 109 words
A process as defined in claim 1 wherein the phenolic monomer has the formula: ##STR5## wherein X is a substituent selected from the group consisting of hydrogen, chlorine, bromine and iodine, Q is a monovalent substituent selected from the group consisting of hydrocarbon radicals, halohydrocarbon radicals having at least two carbon atoms between the halogen atom and the phenol nucleus; hydrocarbonoxy radicals and halohydrocarbonoxy radicals having at least two carbon atoms between the halogen atom and the phenol nucleus; Q' and Q" are the same as Q and in addition may be halogen, with the proviso that Q, Q' and Q" are all free of a tertiary alpha-carbon atom.
Claim 4
Dependent Claim 15 words
A process as defined in claim 1 wherein the catalyst is a complex copper-amine catalyst.
Claim 5
Dependent Claim 79 words
A process as defined in claim 1 wherein the catalyst is a complex manganese catalyst of the formula (L) x Mn wherein L is hydroxyoxime ligand of the formula: ##STR6## wherein R a , R b , R c and R d are independently selected from the group consisting of hydrogen, acyclic and cyclic hydrocarbon radicals, and n is a positive integer equal to 0 to 1, and x is a positive number at least equal to about 10.
Claim 6
Dependent Claim 24 words
A process as defined in claim 3 wherein the complex copper-amine catalyst is based on a copper compound and a primary or secondary amine.
Claim 7
Dependent Claim 14 words
A process as defined in claim 5 wherein the amine is a dialkyl amine.
Claim 8
Dependent Claim 63 words
A process as defined in claim 3 wherein the catalyst comprises (a) a copper compound (b) a diamine of the formula: R.sup.1 HN--R.sup.2 --NHR.sup.1 wherein each R 1 is independently isopropyl, a C 4-8 tertiary alkyl or a cycloalkyl group having no hydrogens on the alpha-carbon atom and R 2 is C 2-4 alkylene or C 3-7 cycloalkylene; and (c) a tertiary amine.
Claim 9
Dependent Claim 19 words
A process as defined in claim 3 wherein the copper-amine catalyst is derived from cuprous oxide, butyldimethylamine and N,N'-di-tert-butylethylenediamine.
Claim 10
Dependent Claim 19 words
A process as defined in claim 3 wherein the copperamine catalyst is derived from cuprous oxide, butyldimethylamine and N,N'-di-tert-butylethylenediamine.
Claim 11
Dependent Claim 88 words
A process for the preparation of poly(2,6-dimethyl-1,4-phenylene oxide) polymer having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of a phenolic monomer, an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture an additional amount of phenolic monomer at a rate that is sufficient to control polymerization and producing a poly(2,6-dimethyl-1,4-phenylene oxide polymer of a predetermined molecular weight.
Claim 12
Dependent Claim 88 words
A process for the preparation of poly(2,6-dimethyl-1,4-phenylene oxide) polymer having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of a phenolic monomer, an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture an additional amount of phenolic monomer at a rate that is sufficient to control polymerization and producing a poly(2,6-dimethyl-1,4-phenylene oxide polymer of a predetermined molecular weight.
Claim 13
Dependent Claim 21 words
A process as defined in claim 10 wherein the catalyst is a manganese catalyst derived from manganese chloride and benzoin oxime.
Claim 14
Dependent Claim 116 words
A process for preparation of polyphenylene oxide polymer, having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of from 85 to 99.9% by weight of the total amount of monomer adding during the reaction of an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture at a rate of 0.2 to 15% by weight of the main phenolic monomer charge per hour of reaction time an additional amount of phenolic monomer, and controlling the polymerization and producing a polyphenylene oxide polymer of a predetermined molecular weight.
Claim 15
Dependent Claim 116 words
A process for preparation of polyphenylene oxide polymer, having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of from 85 to 99.9% by weight of the total amount of monomer adding during the reaction of an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture at a rate of 0.2 to 15% by weight of the main phenolic monomer charge per hour of reaction time an additional amount of phenolic monomer, and controlling the polymerization and producing a polyphenylene oxide polymer of a predetermined molecular weight.
Claim 16
Dependent Claim 109 words
A process as defined in claim 12 wherein the phenolic monomer has the formula: ##STR7## wherein X is a substituent selected from the group consisting of hydrogen, chlorine, bromine and iodine, Q is a monovalent substituent selected from the group consisting of hydrocarbon radicals, halohydrocarbon radicals having at least two carbon atoms between the halogen atom and the phenol nucleus; hydrocarbonozy radicals and halohydrocarbonoxy radicals having at least two carbon atoms between the halogen atom and the phenol nucleus; Q' and Q" are the same as Q and in addition may be halogen, with the proviso that Q, Q' and Q" are all free of a tertiary alpha-carbon atom.
Claim 17
Dependent Claim 15 words
A process as defined in claim 12 wherein the catalyst is a complex copper-amine catalyst.
Claim 18
Dependent Claim 80 words
A process as defined in claim 12 wherein the catalyst is a complex manganese catalyst of the formula (L) x Mn wherein L is a hydroxyoxime ligand of the formula: ##STR8## wherein R a , R b , R c and R d are independently selected from the group consisting of hydrogen, acyclic and cyclic hydrocarbon radicals, and n is a positive integer equal to 0 to 1, and x is a positive number at least equal to about 10.
Claim 19
Dependent Claim 24 words
A process as defined in claim 14 wherein the complex copper-amine catalyst is based on a copper compound and a primary or secondary amine.
Claim 20
Dependent Claim 14 words
A process as defined in claim 16 wherein the amine is a dialkyl amine.
Claim 21
Dependent Claim 63 words
A process as defined in claim 14 wherein the catalyst comprises (a) a copper compound (b) a diamine of the formula: R.sup.1 HN--R.sup.2 --NHR.sup.1 wherein each R 1 is independently isopropyl, a C 4-8 tertiary alkyl or a cycloalkyl group having no hydrogens on the alpha-carbon atom and R 2 is C 2-4 alkylene or C 3-7 cycloalkylene; and (c) a tertiary amine.
Claim 22
Dependent Claim 19 words
A process as defined in claim 14 wherein the copper-amine catalyst is based on cupric chloride and di-n-butyl amine.
Claim 23
Dependent Claim 19 words
A process as defined in claim 14 wherein the copper-amine catalyst is based on cuprous oxide, butyldimethylamine and N,N'-di-tert-butylethylenediamine.
Claim 24
Dependent Claim 120 words
A process for the preparation of poly(2,6-dimethyl-1,4-phenylene oxide) polymer, having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of from 85 to 99.9% by weight of the total amount of monomer added during the reaction of a phenolic monomer, an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture at a rate of 0.2 to 15% by weight of the main phenolic monomer charge per hour of reaction time an additional amount of phenolic monomer, and controlling the polymerization and producing a poly(2,6-dimethyl-1,4-phenylene oxide polymer of a predetermined molecular weight.
Claim 25
Dependent Claim 120 words
A process for the preparation of poly(2,6-dimethyl-1,4-phenylene oxide) polymer, having a predetermined molecular weight, said process comprising the steps of: (a) adding oxygen to a reaction mixture comprising a main charge of from 85 to 99.9% by weight of the total amount of monomer added during the reaction of a phenolic monomer, an oxidative coupling catalyst and a solvent; and (b) while continuing the addition of oxygen to the reaction mixture of step (a), adding to said reaction mixture at a rate of 0.2 to 15% by weight of the main phenolic monomer charge per hour of reaction time an additional amount of phenolic monomer, and controlling the polymerization and producing a poly(2,6-dimethyl-1,4-phenylene oxide polymer of a predetermined molecular weight.
Claim 26
Dependent Claim 22 words
A process as defined in claim 21 wherein the catalyst is a complex manganese catalyst based on manganese chloride and benzoin oxime.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-01 1983-10-01 1984-04-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-01 1987-10-01 1988-04-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-01 1991-10-01 1992-04-01 $7700.00 Window Closed / Lapsed

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