Process for the preparation of aromatic carbonic diesters
First Claim
1. Process for the preparation of carbonic diesters containing at least one aromatic ester group from carbonic diesters containing at least one aliphatic ester group by catalysed transesterification with a phenol, characterised in that the catalyst used is a titanium dioxide having a surface area of at least 90 m2 /g as determined by the BET method in an amount of 0.1 to 200% by weight, relative to the carbonic diester used, which contains at least one aliphatic ester group.
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Abstract
Carbonic diesters containing at least one aromatic ester group can be prepared from carbonic diesters containing at least one aliphatic ester group by transesterification using a phenol, titanium dioxide having a surface area of at least 20 m2 /g as determined by the BET method being used as catalyst.
41 Citations
10 Claims
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1. Process for the preparation of carbonic diesters containing at least one aromatic ester group from carbonic diesters containing at least one aliphatic ester group by catalysed transesterification with a phenol, characterised in that the catalyst used is a titanium dioxide having a surface area of at least 90 m2 /g as determined by the BET method in an amount of 0.1 to 200% by weight, relative to the carbonic diester used, which contains at least one aliphatic ester group.
- View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10)
- 4. Process according to claim 2, characterised in that the carbonic diesters contain at least one aliphatic ester group of the formula
- space="preserve" listing-type="equation">R.sup.3 O--CO--OR.sup.4
in which R3 and R4, independently of one another, denote straight-chain or branched C1 -C8 -alkyl, cyclopropyl, cyclopentyl or cyclohexyl, in which furthermore R3 can denote substituted or unsubstituted phenyl.
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5. Process according to claim 1, characterised in that a phenol of the formula ##STR6## in which R5 denotes hydrogen, C1 -C4 -alkyl, C2 -C4 -alkenyl, C1 -C4 -alkoxy, C5 -C6 -cycloalkyl, phenyl, fluorine, chlorine, bromine or cyano;
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R6 represents hydrogen C1 -C4 -alkyl, C2 -C4 -alkenyl, C1 -C4 -alkoxy, fluorine, chlorine, bromine and R7 represents hydrogen, C1 -C4 -alkyl or the group ##STR7## in which X denotes a single bond, --CH2 --, C2 -C5 -cycloalkylidene, oxygen, sulphur, --CO--, --SO-- or --SO2 --, in which R6 and R7 together can also denote a fused benzene ring, is used for transesterification.
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6. Process according to claim 1, characterised in that a phenol of the formula ##STR8## in which R8 and R9, independently of one another, denote hydrogen, C1 -C4 -alkyl or chlorine, is used.
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7. Process according to claim 1, characterised in that the phenol is a bisphenol of the formula ##STR9## in which R10 and R11, independently of one another, can denote hydrogen, C1 -C4 -alkyl, C2 -C4 -alkenyl, C1 -C4 -alkoxy, C5 -C6 -cycloalkyl, fluorine, chlorine or bromine, and
Y represents a single bond, --CH2 --, --C2 --H5 -alkylidene, C5 -C6 -cycloalkylidene, sulphur or --SO2 --. -
8. Process according to claim 1, characterised in that the reaction is carried out at a temperature of 50°
- -300°
C.
- -300°
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9. Process according to claim 1 wherein the catalyst is used in an amount of 2 to 50% by weight relative to the carbonic diester used.
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10. Process according to claim 1 wherein the reaction is carried out at a temperature of 100°
- -250°
C.
- -250°
Specification