Production of 2-substituted 4-hydroxy-4-methyltetrahydropyrans having stable odoriferous quality

Patent metadata

Field	Value
Publication number	US-10023550-B2
Application number	US-201515303976-A
Country	US
Kind code	B2
Filing date	Apr 8, 2015
Priority date	Apr 14, 2014
Publication date	Jul 17, 2018
Grant date	Jul 17, 2018

Abstract

The present invention relates to a method for the production of 2-substituted 4-hydroxy-4-methyltetrahydropyrans from the acid-catalyzed reaction of 3-methylbut-3-ene-1-ol with an aldehyde, a stable odoriferous quality being achieved and avoiding off-odors that interfere with the odor sensation.

First claim

The invention claimed is:

1. A process for the preparation of 2-substituted 4-hydroxy-4-methyltetrahydropyrans of the formula (I)

in which
R 1 is straight-chain or branched C 1 -C 12 -alkyl, straight-chain or branched C 2 -C 12 -alkenyl, unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted cycloalkyl having in total 3 to 20 carbon atoms or unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted aryl having in total 6 to 20 carbon atoms,

which comprises the following steps)
a) reacting 3-methylbut-3-en-1-ol of the formula (IV)

with an aldehyde of the formula (V)
R 11 —CHO  (V)

in which
R 11 is straight-chain or branched C 1 -C 12 -alkyl, straight-chain or branched C 2 -C 12 -alkenyl, unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted cycloalkyl having in total 3 to 20 carbon atoms or unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted aryl having in total 6 to 20 carbon atoms,
in the presence of an acidic catalyst, where a reaction mixture is obtained which comprises at least one 2-substituted 4-hydroxy-4-methyltetrahydropyran of the formula (I),

b) the reaction mixture from step a) is subjected to a distillative separation to give at least one fraction enriched in the 2-substituted 4-hydroxy-4-methyltetrahydropyrans of the formula (I), and
c) where the reaction mixture from step a), prior to use in step b) and/or during use in step b), is brought into contact with an acidic ion exchanger and/or admixed with 1 to 250 ppm, based on the weight of the reaction mixture, of a strong acid.

2. The process according to claim 1 , wherein the reaction mixture from step a), during the use in step b) is brought into contact with an acidic ion exchanger and/or admixed with a strong acid.

3. The process according to claim 1 , wherein a fraction obtained during the distillative separation in step b), is admixed with a strong acid.

4. The process according to claim 1 , wherein the bottom of the distillative separation in step b) or, in the case of a multi-stage distillation, the bottom of the first distillation stage of the distillative separation in step b) is admixed with a strong acid.

5. The process according to claim 1 , where a strong acid is used which is selected from sulfuric acid, hydrochloric acid, methanesulfonic acid and p-toluenesulfonic acid.

6. The process according to claim 1 , where sulfuric acid is used as strong acid.

7. The process according to claim 1 , where the reaction mixture from step a), prior to use in step b), is admixed with 1 to 250 ppm by weight based on the total weight of the reaction mixture, of a strong acid.

8. The process according to claim 1 , wherein the bottom of the distillative separation in step b) or, in the case of a multi-stage distillation, the bottom of the first distillation stage of the distillative separation in step b) is admixed with 1 to 250 ppm by weight, based on the total weight of the bottom product, of a strong acid.

9. The process according to claim 1 , where, in step a), a reaction mixture is obtained which comprises at least one 2-substituted 4-hydroxy-4-methyltetrahydropyran of the formula (I),
at least one dioxane compound (II)

and at least one of the compounds (III.1), (III.2) or (III.3)

in which
R 1 is straight-chain or branched C 1 -C 12 -alkyl, straight-chain or branched C 2 -C 12 -alkenyl, unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted cycloalkyl having in total 3 to 20 carbon atoms or unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted aryl having in total 6 to 20 carbon atoms.

10. The process according to claim 6 , where, in step a), a reaction mixture is obtained which additionally comprises at least one compound which is selected from:
3-methylbut-3-en-1-ols of the formula (IV)
aldehydes of the formula (V)
acetals of the general formula (VI)

in which
R 1 is straight-chain or branched C 1 -C 12 -alkyl, straight: chain or branched C 2 -C 12 -alkenyl, unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted cycloalkyl having in total 3 to 20 carbon atoms or unsubstituted or C 1 -C 12 -alkyl- and/or C 1 -C 12 -alkoxy-substituted aryl having in total 6 to 20 carbon atoms.

11. The process according to claim 1 , where the reaction mixture obtained in step a) comprises
60 to 85% by weight of at least one compound (I),
5 to 15% by weight of at least one compound (II),
5-15% by weight of at least one of the compounds (III.1), (III.2) or (III.3),
0-10% by weight of at least one 3-methylbut-3-en-1-ol (IV),
0-5% by weight of at least one aldehyde (V), and
0-5% by weight of at least one compound (VI),
based on the total weight of the reaction mixture.

12. The process according to claim 1 , where the radical R 1 is isobutyl or phenyl.

13. The process according to claim 1 , in which the reaction in step a) takes place in the presence of an acidic catalyst which is selected from hydrochloric acid, sulfuric acid, methanesulfonic acid, p-toluenesulfonic acid and strongly acidic cation exchangers.

14. The process according to claim 1 , in which the reaction in step a) is carried out in the presence of a strongly acidic cation exchanger and further in the presence of added water.

15. The process according to claim 1 , where, for the separation in step b), a device is used which comprises
a feed column with rectification section situated above the feed point and stripping section positioned below the feed point,
an upper combining column communicating with the upper end of the rectification section and a lower combining column communicating with the lower end of the stripping section, and
a discharge column communicating with the upper combining column and the lower combining column.

16. The process according to claim 1 , where the distillative separation in step b) takes place in an arrangement of distillation columns which comprises a dividing-wall column or an interconnection of at least two thermally coupled conventional distillation columns.

17. The process according to claim 1 , where, for the distillative separation of the reaction product from step a), an arrangement of distillation columns is used which comprises an upstream conventional distillation column and a downstream dividing-wall column or a downstream interconnection of two thermally coupled distillation columns.

18. The process according to claim 1 , where the distillative separation in step b) comprises
b1) subjecting the reaction mixture from step a) which comprises at least one 2-substituted 4-hydroxy-4-methyltetrahydropyran of the formula (I),
at least one dioxane compound (II)

and at least one of the compounds (III.1), (III.2) or (III.3)

Assignees

• Basf Se

Inventors

• Stork Timon
• Dehn Martine
• Ebel Klaus
• Beck Karl
• Salden Axel
• Pelzer Ralf

Classifications

• C11B9/008

  the hetero rings containing six atoms · CPC title

• C07D319/06

  not condensed with other rings · CPC title

• C07C43/303

  having acetal carbon atoms bound to acyclic carbon atoms · CPC title

• C07D309/10 Primary

  Oxygen atoms · CPC title

• C07D309/18

  containing only hydrogen and carbon atoms in addition to the ring hetero atom · CPC title