Process for preparing triallyl isocyanurate (TAIC)
View Patent ↗The invention is directed to an improved, reliably performable process for preparing triallyl isocyanurate (TAIC) by Cu 2+ -catalysed rearrangement of triallyl cyanurate (TAC) at at least 90° C. According to the invention, TAC and, if required, also a Cu 2+ catalyst and solvent are fed continuously to a start reaction mixture after onset of the initially inhibited isomerization reaction, the isomerization is performed at from 90 to 160° C. and an amount of reaction mixture equivalent to the amount of reactant is drawn off continuously and sent to the workup. Preference is given to effecting the isomerization in TAIC as the reaction medium.
1. A process for preparing triallyl isocyanurate (TAIC), comprising rearrangement of triallyl cyanurate (TAC) in the presence of a Cu salt at a temperature of at least 90° C., wherein
TAC and a Cu 2+ salt are introduced continuously in an amount of 0.01 to 1% by weight of Cu 2+ , based on TAC, separately from one another or in the form of a mixture comprising these components, into a TAIC-containing reaction mixture which has been formed at at least 90° C. by rearrangement of TAC in the presence of a Cu 2+ salt and has not been cooled below 90° C. thereafter, the rearrangement is performed under these conditions while maintaining a temperature in the range of 90 to 160° C. and an amount of reaction mixture corresponding to the addition is discharged continuously and TAIC is isolated therefrom.
2. The process according to claim 1 , wherein
the rearrangement of TAC to TAIC is performed in the presence of an aprotic solvent which is stable at 90 to 160° C. with respect to a combination of Cu 2+ and TAC.
3. The process according to claim 1 ,
wherein
TAC and, if required, additionally Cu 2+ salt are introduced into the reaction mixture in the form of an aprotic solvent which is stable at 90 to 160° C. with respect to a combination of Cu 2+ and TAC.
4. The process according to claim 2 ,
wherein
TAC and a Cu 2+ salt are introduced separately or in a mixture, where the individual components or the mixture may additionally comprise an aprotic solvent which is stable at the reaction temperature with respect to a combination of Cu 2+ and TAC, into a TAIC-containing reaction mixture which has been formed at 90 to 160° C. by rearrangement of TAC in the presence of a Cu 2+ salt and of an aprotic solvent which is stable at the reaction temperature mentioned with respect to a combination of Cu 2+ and TAC.
5. The process according to claim 2 ,
wherein
the aprotic solvent used is an aliphatic, cycloaliphatic or aromatic hydrocarbon, a diester of carbonic acid, an ester of an aliphatic or aromatic carboxylic acid or an ether.
6. The process according to claim 1 ,
wherein
the rearrangement is performed at a temperature in the range from 110 to 140° C.
7. The process according to claim 1 ,
wherein
the Cu 2+ salt used is an anhydrous salt, especially a salt from the group of CuCl 2 , CuBr 2 , CuI 2 , Cu(RCOO) 2 where R=alkyl or aryl.
8. The process according to claim 7 ,
wherein
the catalyst fed continuously to the reaction mixture is CuCl 2 in an amount of 0.02 to 0.2% by weight of Cu 2+ , based on TAC.
9. The process according to claim 1 ,
wherein
the Cu 2+ salt fed in continuously is a bottom product which has been obtained by distilling TAIC out of the reaction mixture drawn off continuously, the temperature of the bottom product not having been cooled to a temperature of below 90° C. before its reuse.
10. A process for preparing TAC, comprising rearrangement of triallyl cyanurate (TAC) in the presence of a Cu salt at a temperature of at least 90° C.,
wherein
TAC is introduced continuously into a TAIC-containing start reaction mixture which has been formed at at least 90° C. by rearrangement of TAC in the presence of a Cu 2+ salt and has not been cooled below 90° C. thereafter, the rearrangement is performed under these conditions while maintaining a temperature in the range of 90 to 160° C., and TAIC which forms is distilled continuously out of the reaction mixture under reduced pressure, the addition rate of TAC (g of TAC/min) corresponding essentially to the distillation rate of TAIC (g of TAIC/min).
11. The process according to claim 10 ,
wherein
the rearrangement is performed in the presence of 0.01 to 1% by weight of Cu 2+ , based on the TAC used to prepare the start reaction mixture.
12. The process according to claim 10 ,
wherein
the rearrangement is performed at 110 to 140° C.
13. The process according to claim 10 ,
wherein
TAC is added at such a rate that the TAIC distilled off is virtually free of unconverted TAC.
14. The process according to claim 2 ,
wherein
TAC and, if required, additionally Cu 2+ salt are introduced into the reaction mixture in the form of an aprotic solvent which is stable at 90 to 160° C. with respect to a combination of Cu 2+ and TAC.
15. The process according to claim 3 ,
wherein
TAC and a Cu 2+ salt are introduced separately or in a mixture, where the individual components or the mixture may additionally comprise an aprotic solvent which is stable at the reaction temperature with respect to a combination of Cu 2+ and TAC, into a TAIC-containing reaction mixture which has been formed at 90 to 160° C. by rearrangement of TAC in the presence of a Cu 2+ salt and of an aprotic solvent which is stable at the reaction temperature mentioned with respect to a combination of Cu 2+ and TAC.
16. The process according to claim 11 ,
wherein
the rearrangement is performed at 110 to 140° C.