Granted Patent B2

US 7,928,269 · App. 12/317,874 · Granted Apr 19, 2011

Abstract

Claims (29)

1. A process for separating at least one tertiary alcohol from at least one secondary alcohol from pine oil, the process comprising:

reacting the pine oil comprising the at least one secondary alcohol and the at least one tertiary alcohol with at least one C 3 -C 30 carboxylic acid ester, and at least one base, wherein the secondary alcohol is esterified to produce at least one secondary ester, with the proviso that the base is not a hydroxide; and

separating the tertiary alcohol from the secondary ester.

2. The process of claim 1 , wherein the pine oil further comprises water, and before the pine oil is reacted with the C 3 -C 30 carboxylic acid ester and the base, the pine oil is treated to substantially remove the water.

3. The process of claim 1 , wherein the secondary alcohol is borneol, fenchol, or mixtures thereof.

4. The process of claim 1 , wherein the secondary ester is borneol ester, fenchol ester, or mixtures thereof.

5. The process of claim 1 , wherein the tertiary alcohol is terpineol.

6. The process of claim 1 , wherein the tertiary alcohol is α-terpineol, γ-terpineol, or mixtures thereof.

7. The process of claim 1 , wherein the C 3 -C 30 carboxylic acid ester comprises a C 7 -C 20 carboxylic acid moiety.

8. The process of claim 1 , wherein the C 3 -C 30 carboxylic acid ester is isopropyl myristate.

9. The process of claim 1 , wherein the base is a strong organic base.

10. The process of claim 1 , wherein the base is a strong inorganic base, with the proviso that the base is not a hydroxide.

11. The process of claim 1 , wherein the base is an alkoxide, an alkoxide salt, or mixtures thereof.

12. The process of claim 1 , wherein the base is selected from sodium methoxide, sodium ethoxide, sodium isopropoxide, potassium methoxide, potassium ethoxide, potassium isopropoxide, sodium oxide, sodium hydride, sodium amide, calcium oxide, magnesium oxide, sodium carbonate, potassium carbonate, cesium carbonate, DBU (1,8-diazabicyclo[5.4.0]undec-7-ene), DABCO (1,4-diazabicyclo[2.2.2]octane), DMAP (4-(dimethylamino)pyridine), 1,8-bis(dimethylamino)naphthalene, phosphazene bases, and mixtures thereof.

13. The process of claim 1 , wherein the tertiary alcohol is separated from the secondary ester by distillation.

14. The process of claim 1 , wherein the process produces at least 95% by weight of at least one tertiary alcohol.

15. The process of claim 1 , wherein the process produces at least 99% by weight of at least one tertiary alcohol.

16. A process for separating terpineol from borneol and fenchol in pine oil, the process comprising:

treating the pine oil comprising the borneol, the fenchol, and the terpineol to substantially remove water present in the pine oil to produce a substantially anhydrous pine oil mixture;

substantially removing the fenchol from the substantially anhydrous pine oil mixture to produce a borneol and terpineol mixture;

reacting the borneol and terpineol mixture with at least one C 3 -C 30 carboxylic acid ester and at least one base, wherein the borneol is esterified to produce a borneol ester, with the proviso that the base is not a hydroxide; and

separating the terpineol from the borneol ester.

17. A process for producing fragrance-quality terpineol, the process comprising:

distilling pine oil comprising water, terpenes, fenchol, borneol, and terpineol to substantially remove the water, the terpenes, and the fenchol to produce a mixture comprising a majority of borneol and terpineol;

reacting the mixture comprising the majority of the borneol and the terpineol with at least one C 3 -C 30 carboxylic acid ester comprising at least one C 7 -C 20 carboxylic acid moiety and at least one strong organic base, wherein the majority of the borneol is esterified to produce a borneol ester; and

distilling the terpineol from the borneol ester, wherein the distilled terpineol comprises at least 95% by weight of the terpineol.

18. The process of claim 17 , wherein the distilled terpineol comprises at least 99% by weight of the terpineol.

19. The process of claim 17 , wherein the distilled terpineol comprises at least 25% by weight of α-terpineol.

20. The process of claim 17 , wherein the distilled terpineol comprises at least 35% by weight of α-terpineol.

Assignments (13)