BONRATH WERNER (CH)
MUELLER MARC-ANDRÉ (CH)
WUESTENBERG BETTINA (CH)
ZHU, Y. ET AL.: "FT-IR spectra of all sixteen isomers of retinal, their isolation, and other spectroscopic properties.", TETRAHEDRON, vol. 48, no. 46, 1992, pages 10061 - 10074, XP055699509, ISSN: 0040-4020, DOI: 10.1016/S0040-4020(01)89036-0
KUK, J.C. ET AL.: "General Preparation and Controlled Cyclization of Acyclic Terpenoids", JOURNAL OF ORGANIC CHEMISTRY, vol. 73, no. 5, 2008, pages 1991 - 1994, XP055699506, ISSN: 0022-3263, DOI: 10.1021/jo702303a
| Claims 1. Process for the production of a compound of formula (II) in the presence of at least one strong Bnzsnsted acid. 2. Process according to claim 1 , wherein the acid is a solid acid. 3. Process according to claim 1 or 2, wherein the acid is an ion-exchange resin, which has sulfonic acid groups. 4. Process according to claim 1 , wherein the acid is a liquid acid. 5. Process according to claim 1 or 4, wherein the acid is a compound of the following formula (VI) R-SOsH (VI), wherein R is Ci-C4-alkyl, Cl, Chh or CF3. 6. Process according to claim 1 , 4 or 5, wherein the acid is chosen from the group consisting of CH3SO3H, CISO3H and CF3SO3H. 7. Process according to anyone of the preceding claims, wherein the acid is used in an amount of 0.5 mol-equivalent (in view of the compound of formula (I)) up to 10 mol-equivalent (in view of the compound of formula (I)). 8. Process according to anyone of the preceding claims, wherein the process is carried out in the presence of at least one inert solvent. 9. Process according to anyone of the preceding claims, wherein the process is carried out in at least one polar aprotic solvent. 10. Process according to anyone of the preceding claims, wherein the process is carried out at a temperature of from -50°C to 50°C. 11. Process according to anyone of the preceding claims, wherein the process is carried out at a residence time (t) of 5 - 30 minutes. 12. Process according to anyone of the preceding claims, wherein the process is carried out batch-wise. 13. Process according to anyone of the preceding claims 1 - 11 , wherein the process is carried out continuously. 14. A compound of formula (III) |
OF VITAMIN A DERIVATIVES FROM POLYENES BY CYCLISATION
The present invention relates to a cyclisation process of specific polyenes. The obtained compounds, which comprise a carbon ring are useful intermediates in the organic syntheses (for example in the production of specific isoprenoids, preferably in the production of vitamin A and derivatives of vitamin A).
Due to the importance of vitamin A (and derivatives of vitamin A) and the complexity of its synthesis there is always a need for improving the synthesis of vitamin A (and derivatives of vitamin A) and/or finding alternative routes to produce vitamin A (and derivatives of vitamin A).
Surprisingly, it was found that it is possible to cyclisize the compound of formula
(I)
which results in useful intermediates for organic synthesis (especially of the production of vitamin A and/or its derivatives).
Therefore, the present invention relates to the cyclisation of a compound of formula
(I)
in the presence of an acid. The main product of this reaction is the compound of formula (II)
Compound of formula (II) is an important intermediate in the production of specific isoprenoids (especially of vitamin A and its derivatives).
The cyclisation reaction of the present invention also provides the following products (compounds of formula (III), (IV) and (V)):
Surprisingly, it is possible (by the process of the present invention) to keep the amounts of the side products low and therefore produce the main product (compound of formula (II)) in a high amount.
Surprisingly, this is achieved by the use of at least one strong Bnzsnsted acid in the process according to the present invention.
Therefore, the present invention relates a process (P) for to the production of a compound of formula (II)
in the presence of at least one strong Bnzsnsted acid.
The strong Bnzsnsted acid can be solid as well as liquid. Examples of solid strong Bnzsnsted acid are ion-exchange resins, which have usually sulfonic acid groups, e.g. sodium polystyrene sulfonate or polyAMPS,
A further example of solid acid catalysts useful for this cyclisation reaction are alkylsulphinic acid on a carrier such as silica.
Typical examples of such ion-exchange resins are i.e. Amberlyst ® 15, Amberlyst ® 16 and Amberlyst ® 36 and Deloxan ASP 1/9.
It is also possible to use a liquid acid, which has a Pk a value similar to sulfonic acids.
Preferred liquid acids are those of formula (VI)
R-SOsH (VI), wherein R is Ci-C4-alkyl, Cl, Chh or CF3.
It is also possible to use a liquid acid, which is preferably a compound of formula (VI)
R-SOsH (VI), wherein R is Ci-C4-alkyl, Cl, CH3 or CF3.
The preferred liquid acids are CFI3SO3FI, CISO3FI and CF3SO3FI. The most preferred liquid acid is CFI3SO3FI.
Therefore, the present invention also relates to a process (P1 ), which is process (P), wherein the acid is a solid acid. Therefore, the present invention also relates to a process (PT), which is process (P1 ), wherein the acid is an ion-exchange resin, which has sulfonic acid groups.
Therefore, the present invention also relates to a process (P2), which is process (P), wherein the acid is a liquid acid.
Therefore, the present invention also relates to a process (P2’), which is process (P2), wherein the acid is a compound of the following formula (VI)
R-SOsH (VI),
wherein R is Ci-C 4 -alkyl, Cl, CH3 or CF3.
Therefore, the present invention also relates to a process (P2”), which is process (P2) or (P2’), wherein the acid is chosen from the group consisting of CH 3 SO 3 H, CISOsH and CF 3 SO 3 H.
Therefore, the present invention also relates to a process (P2’”), which is process (P2), (P2’) or (P2’”), wherein the liquid acid is CH3SO3H.
The acid, which is used in the process according to the present invention is used in an amount of 0.5 mol-equivalent (in view of the compound of formula (I)) up to 10 mol-equivalent (in view of the compound of formula (I)).
Preferably, the amount of the acid is 0.5 - 8 mol-equivalent (in view of the compound of formula (I)).
Therefore, the present invention also relates to a process (P3), which is process (P), (P1 ), (PT), (P2), (P2’), (P2”) or (P2’”), wherein the acid is used in an amount of 0.5 mol-equivalent (in view of the compound of formula (I)) up to 10 mol- equivalent (in view of the compound of formula (I)). Therefore, the present invention also relates to a process (P3’), which is process (P), (P1 ), (PT), (P2), (P2’), (P2”) or (P2’”), wherein the acid is used in an amount of 0.5 - 8 mol-equivalent (in view of the compound of formula (I)).
The process according to the present invention can be carried out in the presence of at least one inert solvent. Suitable solvents are polar aprotic solvents such as CH2CI2.
Therefore, the present invention also relates to a process (P4), which is process (P), (P1 ), (P1’), (P2), (P2’), (P2”), (P2’”), (P3) or (P3’), wherein the process is carried out in the presence of at least one inert solvent.
Therefore, the present invention also relates to a process (P4’), which is process (P4), wherein the process is carried out in at least one polar aprotic solvent.
Therefore, the present invention also relates to a process (P4”), which is process (P4), wherein the process is carried out in CH2CI2.
The process according to the present invention is usually carried out at a temperature of from -50°C to about 50°C. Preferably at a temperature of from -40°C to about 40°C.
Therefore, the present invention also relates to a process (P5), which is process (P), (P1 ), (P1’), (P2), (P2’), (P2”), (P2’”), (P3), (P3’), (P4), (P4’) or (P4”), wherein the process is carried out at a temperature of from -50°C to 50°C. Therefore, the present invention also relates to a process (P5’), which is process (P), (P1 ), (PV), (P2), (P2’), (P2”), (P2’”), (P3), (P3’), (P4), (P4’) or (P4”), wherein the process is carried out at a temperature of from -40°C to 40°C.
The process according to the present invention is usually carried out at a residence time (t) of 5 - 30 minutes, preferably 10 - 20 minutes.
Therefore, the present invention also relates to a process (P6), which is process (P), (P1 ), (P1’), (P2), (P2’), (P2”), (P2’”), (P3), (P3’), (P4), (P4’) > (P4”), (P5) or (P5’), wherein the process is carried out at a residence time (t) of 5 - 30 minutes.
Therefore, the present invention also relates to a process (P6’), which is process (P), (P1 ), (P1’), (P2), (P2’), (P2”), (P2’”), (P3), (P3’), (P4), (P4’) > (P4”), (P5) or (P5’), wherein the process is carried out at a residence time (t) of 10 - 20 minutes.
The process according to the present invention can be carried out batch-wise as well as continuously.
Therefore, the present invention also relates to a process (P7), which is process (P), (P1 ), (P1’), (P2), (P2’), (P2”), (P2’”), (P3), (P3’), (P4), (P4’) > (P4”), (P5), (P5’), (P6) or (P6’), wherein the process is carried out batch-wise.
Therefore, the present invention also relates to a process (P7’), which is process (P), (P1 ), (P1’), (P2), (P2’), (P2”), (P2’”), (P3), (P3’), (P4), (P4’) > (P4”), (P5), (P5’), (P6) or (P6’), wherein the process is carried out continuously
The compound of formula (II) is obtained in significantly higher amount than the other products of the cyclisation process. The obtained other products (compounds of formula (III), (IV) and (V) can be removed easily from the compound of formula (II).
Furthermore, the product (III)
which is obtained in a higher amount than the other product (IV), (V) is not known.
Therefore, the present invention also relates to a compound of formula (III)
It is possible to convert the compound of formula (III) into the compound (II) in an easy and simple way (by acid treatment at a slightly increased reaction time)
The following examples serve to illustrate the invention. The temperature is given in °C and all percentages are related to the weight.
Examples
Example
Example 1
17.7 g (0.18 mol) of methane sulfonic acid is mixed with Dichloromethane (40 ml) and cooled to -38 °C
8.8g (0.034 mol) of compound of formula (I) is added under stirring in a period of 10 minutes.
The mixture is stirring another 15 min at -30 to -39 °C.
The reaction mixture is quenched in 80 ml water and extracted with 80 ml t-BME. Layers were separated.
The water layer is extracted with 2 x 40 ml t-BME and the organic layer is washed with 40 ml water.
The organic layer neutralized with 5 ml EtsN (pH:9) and then washed with 50 ml water.
After separation of the layers, the organic phase is dried on Na 2 S0 4 and concentrated on a rotavapor.
The overall yield of the compound of formula (II) was 44%.