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US4028341A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of polyphenylene oxides with hydrolytically stable copper catalysts

Assignee: General Electric Co
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Filing: 1975-01-13
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Granted: 1977-06-07
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Expires: 1995-01-13
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Abstract

Abstract An improved process for the preparation of high molecular weight polyphenylene oxides by oxidatively coupling a di-ortho-substituted phenol with an oxygen-containing gas under polymer-forming reaction conditions in a liquid reaction system is provided by using a specific copper-amine complex soluble in the reaction mixture comprising copper ion, bromide ion, a specific class of hindered secondary diamines and a specific group of tertiary monoamines. The process is characterized by a reaction system which (1) results in the formation of higher molecular weight polymer in a given reaction time or polymer of comparable molecular weight in substantially decreased reaction time, (2) permits the use of extremely low copper-to-phenol ratio, and (3) permits the reaction to be carried out in a solvent system where the water of reaction forms a separate phase without the necessity of removing the water phase.

Inventors

  • 👤 Allan S. Hay

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 23:48
CPC Classifications
C; C08; C08G; C08G65/00; C08G65/34; C08G65/38; C08G65/44

Claims Analysis

Total Claims: 24
Claim 1
Independent Claim 222 words
A process for formation of a polyphenylene oxide having the formula ##STR5## where R and R' are lower primary alkyl and n is a number representing the average degree of polymerization and is at least 100 which comprises: oxidatively coupling the corresponding monohydric phenol with an oxygen-containing gas under polymer-forming reaction conditions in a liquid reaction mixture which is essentially free of ammonium ion and in which the phenol is soluble in the presence of a copper-amine complex soluble in the reaction mixture comprising a. copper ion b. bromide ion c. a diamine having the formula R.sub.b HN--R.sub.a --NHR.sub.c where R a is C 2-4 -alkylene or C 3-7 -cycloalkylene and R b and R c are isopropyl or C 4-8 -tertiary alkyl, including cycloalkyl, in which only the α-carbon atom has no hydrogens, there being at least two and no more than three carbon atoms separating the two nitrogen atoms d. a tertiary amine which is N-methylpyrrolidine, triethylenediamine or a trialkylamine wherein at least two of the alkyl groups are methyl and the third is C 1-8 primary or C 3-8 secondary alkyl, wherein, the molar ratio of (b) to (a) is at least 2, the molar ratio of (c) to (a) is at least 1 and the ratio of equivalents of (d) to moles of (a) is at least 6.
Claim 2
Dependent Claim 222 words
A process for formation of a polyphenylene oxide having the formula ##STR5## where R and R' are lower primary alkyl and n is a number representing the average degree of polymerization and is at least 100 which comprises: oxidatively coupling the corresponding monohydric phenol with an oxygen-containing gas under polymer-forming reaction conditions in a liquid reaction mixture which is essentially free of ammonium ion and in which the phenol is soluble in the presence of a copper-amine complex soluble in the reaction mixture comprising a. copper ion b. bromide ion c. a diamine having the formula R.sub.b HN--R.sub.a --NHR.sub.c where R a is C 2-4 -alkylene or C 3-7 -cycloalkylene and R b and R c are isopropyl or C 4-8 -tertiary alkyl, including cycloalkyl, in which only the α-carbon atom has no hydrogens, there being at least two and no more than three carbon atoms separating the two nitrogen atoms d. a tertiary amine which is N-methylpyrrolidine, triethylenediamine or a trialkylamine wherein at least two of the alkyl groups are methyl and the third is C 1-8 primary or C 3-8 secondary alkyl, wherein, the molar ratio of (b) to (a) is at least 2, the molar ratio of (c) to (a) is at least 1 and the ratio of equivalents of (d) to moles of (a) is at least 6.
Claim 3
Dependent Claim 31 words
The process of claim 1, wherein the reaction is carried out in the presence of benzene, chlorobenzene or toluene, containing up to 250% methanol by weight based on the monohydric phenol.
Claim 4
Dependent Claim 21 words
The process of claim 1, wherein the molar ratio of the monohydric phenol to the copper ion is at least 500.
Claim 5
Dependent Claim 33 words
The process of claim 1, wherein R a is ethylene or propylene, R b and R c have from 3 to 5 carbon atoms, and the tertiary monoamine is a C 1-4 -alkyldimethylamine.
Claim 6
Dependent Claim 19 words
The process of claim 4, wherein R a is ethylene and R b and R c are each tert-butyl.
Claim 7
Dependent Claim 41 words
The process of claim 5, wherein the ratio of (b) to (a) is at least 4 and the ratio of (d) to (a) is at least 9 and the molar ratio of the monohydricphenol to copper ion is at least 700.
Claim 8
Dependent Claim 31 words
The process of claim 2, wherein R and R' are each methyl, R a is ethylene, R b and R c are each tertiary butyl and the tertiary monoamine is trimethylamine.
Claim 9
Dependent Claim 27 words
The process of claim 7, wherein the ratio of (b) to (a) is at least 3 and the ratio of (d) to (a) is at least 9.
Claim 10
Dependent Claim 12 words
The process of claim 8, wherein toluene is used as the solvent.
Claim 11
Dependent Claim 31 words
The process of claim 2, wherein R and R' are each methyl, R a is ethylene, R b and R c are each tertiary butyl and the tertiary monoamine is n-butyldimethylamine.
Claim 12
Dependent Claim 27 words
The process of claim 10, wherein the ratio of (b) to (a) is at least 3 and the ratio of (d) to (a) is at least 9.
Claim 13
Dependent Claim 12 words
The process of claim 11, wherein toluene is used as the solvent.
Claim 14
Dependent Claim 47 words
The process of claim 2, wherein R and R' are each methyl, the molar ratio of the monomeric phenol to copper ion is at least 700, the ratio of (b) to (a) is at least 4 and the ratio of (d) to (a) is at least 9.
Claim 15
Dependent Claim 10 words
The process of claim 13, wherein the solvent is toluene.
Claim 16
Dependent Claim 19 words
The process of claim 1, wherein the reaction is carried out in the presence of a phase transfer agent.
Claim 17
Dependent Claim 20 words
The process of claim 15, wherein the reaction is carried out in the substantial absence of a polar hydrolytic solvent.
Claim 18
Dependent Claim 51 words
The process of claim 15, wherein the reaction is carried at a temperature within the range of from about 15° C. to about 60° C., at a monomer to solvent ratio within the range of from about 15:85 to about 30:70, and in the presence of a lower alkanol or glycol.
Claim 19
Dependent Claim 41 words
The process of claim 17, wherein the phase transfer agent is selected from quaternary ammonium, phosphonium or tertiary sulfonium compounds or mixtures thereof, and the mole equivalent ratio of phase transfer agent per atom of copper is at least about 0.1:1.
Claim 20
Dependent Claim 23 words
The process of claim 18, wherein the mole equivalent ratio of phase transfer agent per atom of copper is at least about 0.25:1.
Claim 21
Dependent Claim 14 words
The process of claim 19, wherein the phase transfer agent is tricaprlylylmethyl ammonium chloride.
Claim 22
Dependent Claim 52 words
The process of claim 15, wherein the reaction is carried out in the absence of a polar hydrolytic solvent at a temperature within the range of from about 15° C. to about 60° C., and the mole equivalent ratio of phase transfer agent per atom of copper is at least about 1:1.
Claim 23
Dependent Claim 23 words
The process of claim 21, wherein the phase transfer agent is selected from quaternary ammonium, phosphonium or tertiary sulfonium compounds, or mixtures thereof.
Claim 24
Dependent Claim 14 words
The process of claim 22, wherein the phase transfer agent is tricaprlylylmethyl ammonium chloride.

References Cited (Backward Citations)

US3306874A Cited
US3306875A Cited
US3838102A Cited
US3900445A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-06-06 1980-12-06 1981-06-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-06 1984-12-06 1985-06-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-06 1988-12-06 1989-06-07 $7700.00 Window Closed / Lapsed

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