Preparation of tetrakis [3-(3,5-di-tert-butyl-4-hydroxy phenyl) propionyl oxymethyl] methane
View Patent ↗A transesterification process for the preparation of tetrakis [3-(3,5-di-tert-butyl-4-hydroxy phenyl)propionyl oxymethyl] methane by the reaction of methyl-(3,5-di-tert-butyl-4-hydroxy phenyl)propionate ester with pentaerythritol wherein the reaction takes place in the presence of an ester exchange catalyst combination consisting of (a) at least one basic or neutral catalyst and (b) at least one metal compound capable of behaving as a Lewis acid and wherein the reaction is conducted through a first stage in which only basic or neutral catalyst is present in the reaction mixture followed by a second stage which commences with the addition of Lewis acid catalyst to the reaction mixture when the amount of di-substituted intermediate product contained within the reaction mixture is less than 20 area % analyzed by HPLC. The preferred basic catalysts are lithium hydroxide and lithium hydroxide monohydrate. The preferred Lewis acid catalyst is zinc octanoate.
1. A transesterification process for the preparation of tetrakis [3-(3,5-di-tertbutyl-4-hydroxy phenyl)propionyl oxymethyl] methane by the reaction of methyl-(3,5-di-tert-butyl-4-hydroxy phenyl)propionate ester with pentaerythritol wherein the reaction takes place in the presence of an ester exchange catalyst combination consisting of (a) at least one basic or neutral catalyst and (b) zinc octanoate wherein the reaction is conducted through a first stage in which only the at least one basic or neutral catalyst is present in the reaction mixture followed by a second stage which commences with the addition of the zinc octanoate to the reaction mixture when the amount of di-substituted intermediate product contained within the reaction mixture is less than 20 area % analyzed by HPLC.
2. A process as claimed in claim 1 wherein the Lewis acid is added to the intermediate reaction mixture when the amount of di-substituted intermediate product contained within the reaction mixture is less than 10 area %.
3. A process as claimed in claim 1 wherein the basic or neutral catalyst is selected from a group Ia alkali metal, a group Ia alkali metal compound or a group IIa alkaline earth compound.
4. A process as claimed in claim 3 wherein the basic or neutral catalyst is lithium hydroxide, lithium hydroxide monohydrate, lithium methoxide, lithium hydride, lithium acetate or lithium amide.
5. A process as claimed in claim 4 wherein the basic catalyst is lithium hydroxide or lithium hydroxide monohydrate.
6. A process as claimed in claim 1 wherein the crude undistilled reaction mixture from the preparation of the methyl-(3,5-di-tertbutyl-4-hydroxy phenyl)propionate is used without neutralization or is used with partial neutralization with a carboxylic acid in the transesterification process.
7. A process as claimed in claim 1 wherein the methanol by-product of the transesterification reaction is removed by solvent sparging, nitrogen sparging and/or application of vacuum.
8. A transesterification process for the preparation of tetrakis [3-(3,5-di-tertbutyl-4-hydroxy phenyl)propionyl oxymethyl]methane by the reaction of a C 2 to C 4 alkyl ester other than methyl-(3,5-di-tert-butyl-4-hydroxy phenyl)propionate ester with pentaerythritol wherein the reaction takes place in the presence of an ester exchange catalyst combination consisting of (a) at least one basic or neutral catalyst and (b) zinc octanoate wherein the reaction is conducted through a first stage in which only the at least one basic or neutral catalyst is present in the reaction mixture followed by a second stage which commences with the addition of the zinc octanoate to the reaction mixture when the amount of di-substituted intermediate product contained within the reaction mixture has been reduced to less than 20 area % analyzed by HPLC.