Azonaphthalene sulfonates as polymerization catalysts
AssigneeGeneral Electric Company
InventorsJohn Patrick Lemmon, Ronald James Wroczynski
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AssigneeGeneral Electric Company
InventorsJohn Patrick Lemmon, Ronald James Wroczynski
Estimating the term…
The present invention relates to a synthetic method comprising contacting at least one diaryl carbonate with one or more dihydroxy aromatic compounds in the presence of a transesterification catalyst under melt polymerization conditions to afford a product polycarbonate. The transesterifcation catalysts used according to the method of the present invention are azonaphthalene sulfonates in combination with tetraalkylammonium or tetraalkylphosphonium compounds which serve as co-catalysts. The transesterification catalysts employed according to the method of the present invention provide polycarbonates having reduced levels of Fries rearrangement product relative to conventionally employed catalysts such as sodium hydroxide in combination with tetramethylammonium hydroxide co-catalyst.
A method for the preparation of polycarbonate said method comprising contacting under melt polymerization conditions at least one diaryl carbonate with at least one dihydroxy aromatic compound in the presence of a transesterification catalyst to afford a polycarbonate, said transesterification catalyst comprising at least one azonaphthalene sulfonate catalyst and at least one co-catalyst.
A method for the preparation of bisphenol A polycarbonate said method comprising contacting at least one diaryl carbonate with bisphenol A in the presence of a transesterification catalyst, at a temperature in a range between about 180° C. and about 310° C. and a pressure in a range between about 760 and about 1 torr to afford a product polycarbonate, said transesterification catalyst comprising at least one azonaphthalene sulfonate catalyst and at least one co-catalyst.
A method for the preparation of bisphenol A polycarbonate, said method comprising contacting bisphenol A with diphenyl carbonate at a temperature in a range between about 180° C. and about 310° C. and a pressure in a range between about 760 torr and about 1 torr in the presence of at least one azonaphthalene sulfonate and tetrabutylphosphonium acetate, said diphenyl carbonate being present in an amount corresponding to between about 0.9 and about 1.2 moles diphenyl carbonate per mole of bisphenol A, said azonaphthalene sulfonate being present in an amount corresponding to between about 1×10−8 and about 2.5×10−4 moles azonaphtalaene-sulfonate per mole bisphenol A employed, said tetrabutylphosphonium acetate being present in an amount corresponding to between about 1×10−6 and about 1×10−2 moles tetrabutylphosphonium acetate per mole bisphenol A employed.
Dependencies are inferred from the claim text.