Process for producing polycarbonate resin with tertiary alryl phenol molecular weight modifier

Claim 2

A process for producing a polycarbonate resin having a viscosity-average molecular weight of from 9,000 to 50,000 as measured at 20° C. using a 6.0 g/l solution of the polycarbonate resin in methylene chloride, which comprises reacting at least one bisphenol compound with phosgene or a carbonate precursor in the presence of a phenol compound selected from the group consisting of tert-hexylphenol and tert-amylphenol, which phenol compound is used as a molecular weight modifier.

Claim 3

The process according to claim 1, wherein said carbonate precursor is diphenyl carbonate.

Claim 4

The process according to claim 1, wherein said bisphenol compound is selected from the group consisting of bis-(4-hydroxyphenyl)methane, 1,1-bis-(4-hydroxyphenyl)ethane, 1,1-bis(4-hydroxyphenyl)propane, 2,2-bis-(4-hydroxyphenyl)propane, 2,2-bis-(4-hydroxyphenyl)butane, 2,2-bis-(4-hydroxyphenyl)pentane, 2,2-bis-(4-hydroxyphenyl)-3-methylbutane, 2,2-bis-(4-hydroxyphenyl) hexane, 2,2-bis-4-hydroxyphenyl)-4-methylpentane, 1,1-bis-(4-hydroxyphenyl)cyclopentane, 1,1-bis-(4-hydroxyphenyl)cyclohexeane, bis-(4-hydroxy-3-methylphenyl)methane, 1,1-bis-(4-hydroxy-3-methylphenyl)ethane, 2,2-bis-(4-hydroxy-3-methylphenyl)propane, 2,2-bis-(4-hydroxy-3-ethylphenyl)propane, 2,2-bis-(4-hydroxy-3-isopropylphenyl)propane, 2,2-bis-(4-hydroxy-3-secbutylphenyl)propane, bis-(4-4-hydroxyphenyl)phenylmethane, 1,1-bis-(4-hydroxyphenyl))-1-phenylpropane, bis-(4-hydroxyphenyl)diphenylmethane, bis-(4-hydroxyphenyl)dibenzylmethane, 4,4'-dihhydroxydiphenylether, 4,4'-dihydroxydiphenylsulfone, 4,4'-dihydroxydiphenylsulfide and pheolphthalein.

Claim 5

The process according to claim 1, wherein an effective amount of an aqueous alkaline solution or pyridine is added as an acid acceptor with the bisphenol compound while introducing phosgene thereto.

Claim 6

The process according to claim 1, wherein the phenol compound is used in an amount of from 1.0 to 10 mol % relative to the bisphenol compound.

Claim 7

The process according to claim 1, wherein the viscosity-average molecular weight is from 9,000 to 30,000.

Claim 8

The process according to claim 6, wherein the phenol compound is used in an amount of from 2.0 to 9.0 mol % relative to the bisphenol compound.

Claim 9

The process according to claim 1, wherein the viscosity-average molecular weight is from 9,000 to 22,000.

Claim 10

The process according to claim 8, wherein the phenol compound is used in an amount of from 4.2 to 9.0 mol % relative to the bisphenol compound.

Claim 11

The process according to claim 1, which further comprises adding a tertiary amine or quaternary ammonium compound catalyst to said reaction mixture when an aqueous alkaline solution is used as an acid acceptor.

Claim 12

The process according to claim 4, wherein said aqueous alkaline solution is an aqueous sodium hydroxide solution.

Claim 13

The process according to claim 10, wherein said tertiary amine is selected from the group consisting of trimethylamine and triethylamine; and said quaternary ammonium compound is selected from the group consisting of tetrabutylammonium chloride and benzyltributylammonium bromide.