Method for producing oxacyclohexane or oxacyclopentane derivatives

JP2024529639A5Pending Publication Date: 2025-03-12FIRMENICH SA
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Patent Information

Application Number
JP2024505464
Authority / Receiving Office
JP · JP
Patent Type
Applications
Current Assignee / Owner
Priority Date
2021-07-30
Filing Date
2022-07-28
Publication Date
2025-03-12

AI Technical Summary

Technical Problem

Existing methods for producing oxacyclopentane and oxacyclohexane derivatives, such as Cetalox® and Ambrox®, rely on large amounts of clay catalysts, which are finite and have unpredictable properties, and there is a need for sustainable processes using recyclable, heterogeneous catalysts that maintain high conversion and selectivity.

Method used

The method involves cyclodehydrating 1,4-diols or 1,5-diols using a small amount of a heterogeneous acidic catalyst, specifically an aluminosilicate catalyst with a silicon:aluminum ratio of 3:1 or more, under non-supercritical conditions, to produce oxacyclopentane or oxacyclohexane derivatives.

Benefits of technology

This approach allows for high selectivity and conversion of diols to desired derivatives without relying on clay catalysts, using recyclable and stable aluminosilicate catalysts, thus promoting sustainable production.

✦ Generated by Eureka AI based on patent content.

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Abstract

The present invention relates to the field of organic synthesis, and more particularly to a process for the preparation of oxacyclopentane or oxacyclohexane derivatives of formula (II) comprising the cyclization of 1,4- or 1,5-diols of formula (I) in the presence of a heterogeneous acidic catalyst.
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Description

[Technical field]

[0001] Technical Field The present invention relates to the field of organic synthesis, and more particularly to a process for the preparation of oxacyclopentane or oxacyclohexane derivatives of formula (II) comprising the cyclization of 1,4- or 1,5-diols of formula (I) in the presence of a heterogeneous acidic catalyst.

[0002] background Oxacyclopentane or oxacyclohexane derivatives represent highly desirable scaffolds and can be used as such or as key intermediates useful for the preparation of more complex compounds in different fields such as fragrance, cosmetics, pharmaceuticals or agrochemicals, among others. Relevant oxacyclopentane derivatives in the fragrance industry are, for example, Cetalox® (3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan; manufacturer: Firmenich SA, Geneva, Switzerland) or Ambrox® ((3aR,5aS,9aS,9bR)-3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan; manufacturer: Firmenich SA, Geneva, Switzerland), which is the main component of natural ambergris. These perfuming ingredients represent some of the most sought-after ingredients in the fragrance industry. Several alternative methods for producing Cetalox® or Ambrox® have been developed, in particular via the cyclodehydration reaction of 1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol as the final step.

[0003] On the other hand, today there is a need to promote sustainable processes using recyclable catalysts, for example heterogeneous catalysts. Dehydration cyclization reactions in the presence of heterogeneous catalysts, especially for the production of Cetalox® or Ambrox® from the corresponding diols, have already been reported, for example in US Patent No. 5,670,670 or WO 2013007832, mainly using clay as catalyst. However, the reaction has only been exemplified with large amounts of clay. In addition, clay is a natural material with properties that depend on the deposition and origin, cannot be easily replicated, is a finite resource, and some clay catalysts reported, for example, in US Patent No. 5,670,670 or WO 2013007832 are no longer commercially available. The only example of dehydration cyclization reactions in the presence of synthetic heterogeneous catalysts with predictable and stable properties, i.e. different from clay, is disclosed in US Patent Application Publication No. 20100248316, where a large amount of basic zeolite is required.

[0004] Therefore, there remains a need to develop a sustainable dehydration cyclization process in the presence of small amounts of heterogeneous reliable catalysts while maintaining high conversion and selectivity.

[0005] The present invention makes it possible to solve the above problems by using a heterogeneous acidic catalyst to prepare oxacyclopentane or oxacyclohexane derivatives. To the best of the inventors' knowledge, the conditions of the present invention have not been reported in the prior art.

[0006] Summary of the Invention The present invention relates to a novel process which allows the preparation of oxacyclopentane or oxacyclohexane derivatives by cyclization of 1,4-diols or 1,5-diols in the presence of small amounts of heterogeneous acidic catalysts, which has not been reported or suggested in the prior art.

[0007] A first subject of the invention is therefore a compound of formula [ka] [In the formula, m is 1 or 2, Each R 1 and R 2 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups, independently of each other 1~18 Each R represents an alkyl group; 3 and R 4 C optionally containing, separately and independently of each other, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group; 1~18 Each R represents an alkyl group; 1 and R 2 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups. 4~11 represents an alkanediyl group, and / or R 2 and R 3 Together, C 2~18 represents an alkanediyl group, and / or R 3 and R 4 Together, C 4~9 represents an alkanediyl group, and / or R 1 and R 4 Together, C 2~9 represents an alkanediyl group; R 5 is a hydrogen atom or C 1~3 represents an alkyl group] in the form of any one of its stereoisomers or a mixture thereof, comprising the steps of: [ka] [In the formula, m, R 1 , R 2 , R 3 , R 4 and R 5has the same meaning as defined for the oxacyclopentane or oxacyclohexane derivative of formula (II), in the form of any one of its stereoisomers or a mixture thereof, wherein the cyclodehydration is carried out in the presence of a heterogeneous acidic catalyst, provided that a) The heterogeneous acid catalyst is not clay, b) if the heterogeneous acidic catalyst is an aluminosilicate catalyst, the silicon:aluminum ratio is 3:1 or greater; and c) The process is not carried out under supercritical conditions This is a method, which requires the following:

[0008] Description of the Invention Surprisingly, it has now been discovered that the dehydration and cyclization of 1,4-diols or 1,5-diols can be carried out in the presence of small amounts of heterogeneous acidic catalysts by choosing a catalyst different from the clay without compromising selectivity and conversion.

[0009] A first subject of the invention is therefore a compound of formula [ka] [In the formula, m is 1 or 2, Each R 1 and R 2 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups, independently of each other 1~18 Each R represents an alkyl group; 3 and R 4 C optionally containing, separately and independently of each other, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group; 1~18 Represents an alkyl group; Each R 1 and R 2C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups. 4~11 represents an alkanediyl group, and / or R 2 and R 3 Together, C 2~18 represents an alkanediyl group, and / or R 3 and R 4 Together, C 4~9 represents an alkanediyl group, and / or R 1 and R 4 Together, C 2~9 represents an alkanediyl group; R 5 is a hydrogen atom or C 1~3 represents an alkyl group] in the form of any one of its stereoisomers or a mixture thereof, comprising the steps of: [ka] [In the formula, m, R 1 , R 2 , R 3 , R 4 and R 5 has the same meaning as defined for the oxacyclopentane or oxacyclohexane derivative of formula (II), in the form of any one of its stereoisomers or a mixture thereof, wherein the cyclodehydration is carried out in the presence of a heterogeneous acidic catalyst, provided that a) The heterogeneous acid catalyst is not clay, b) if the heterogeneous acidic catalyst is an aluminosilicate catalyst, the silicon:aluminum ratio is 3:1 or greater; and c) The process is not carried out under supercritical conditions This is a method, which requires the following:

[0010] For clarity, the term "heterogeneous acidic catalyst" means that the heterogeneous catalyst is not basic, such as catalyst CBV100 or CBV320. In other words, the heterogeneous acidic catalyst is not CBV100 or CBV320.

[0011] For clarity, "oxacyclopentane or oxacyclohexane" or similar terms are meant to have the ordinary meaning understood by those skilled in the art, i.e., that an oxacyclopentane derivative is a tetrahydrofuran derivative and an oxacyclohexane derivative is a tetrahydropyran derivative.

[0012] For clarity, "1,4-diol or 1,5-diol" or similar terms refer to the ordinary meaning understood by those skilled in the art, i.e., a compound having at least two alcohol functional groups separated by 4 or 5 carbon atoms, e.g., (OH)-CH-CH-CH-CH-(OH) or (OH)-CH-CH-CH-CH-CH-CH-(OH). Those skilled in the art are familiar with the cyclization of 1,4-diols by the methods of the present invention to provide oxacyclopentane derivatives, and the cyclization of 1,5-diols by the methods of the present invention to provide oxacyclohexane derivatives.

[0013] For clarity, the phrase "any one of its stereoisomers or a mixture thereof" or similar phrases means the usual meaning understood by a person skilled in the art, i.e., that the compounds referred to in the present invention may be pure enantiomers or mixtures of enantiomers. In other words, the compounds referred to in the present invention may have at least one stereocenter that may have two different stereochemistries (e.g., R or S), e.g., R 1The group may contain at least one stereocenter. The compounds may be in the form of pure enantiomers or in the form of a mixture of enantiomers. The compounds referred to in the present invention may be in the form of pure diastereoisomers or even in the form of a mixture of diastereoisomers if the compounds have two or more stereocenters. The compounds may be in racemic or scalemic form. Thus, the compounds may be in one stereoisomer or in the form of a composition that includes or consists of various stereoisomers.

[0014] The term "optionally" is understood to mean that the group may or may not be substituted with or include the specified functional group.

[0015] The term "...optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups" is understood to mean that these groups can be attached laterally to said alkyl group, replacing a hydrogen atom of said alkyl group, or can be inserted into the alkyl chain, replacing a carbon atom of the alkyl group (if chemically possible). For example, the -CH2-CH2-CHOH-CH2- group represents a C4 alkyl group containing an alcohol group (substitution of a hydrogen atom), the -CH2-CH2-COO-CH2-CH2-OCO-CH2-CH2- group represents a C6 alkyl group containing two ester groups (substitution of a carbon atom / insertion into the alkyl chain), and similarly the -CH2-CH2-O-CH2-CH2-O-CH2-CH2- group represents a C6 alkyl group containing two ether groups.

[0016] "···R 1 and R 2 Together,...C 4~11 represents a linear, branched or cyclic alkanediyl group, and / or R 2 and R 3 Together, C 2~18 represents an alkanediyl group, and / or R 3 and R 4 together with... and / or R1 and R 4 It is understood that the above groups may form a (poly)cyclic alkyl group by the expression "R taken together represents ..." or similar expressions. In other words, compound (I) may be acyclic, monocyclic, bicyclic or tricyclic. For example, R 2 and R 3 , and R 3 and R 4 When taken together, the compounds of formula (I) contain a bicyclic moiety such as decalin. For example, R 2 , R 3 and R 4 taken together represent an alkanetriyl.

[0017] The terms "alkyl" and "alkanediyl" are understood to include linear, branched, cyclic or alicyclic alkyl and alkanediyl groups.

[0018] According to any embodiment of the present invention, the heterogeneous acidic catalyst is not a clay.

[0019] According to any embodiment of the present invention, the heterogeneous acidic catalyst may be amorphous or crystalline, in particular crystalline. The heterogeneous acidic catalyst comprises silicon and a second metal selected from the group consisting of aluminum, boron, iron, tin, titanium, zirconium, hafnium and mixtures thereof. In particular, the heterogeneous acidic catalyst is an aluminosilicate catalyst. In particular, the aluminosilicate catalyst is a zeolite.

[0020] According to any embodiment of the present invention, the heterogeneous acidic catalyst is free of alkali metals or alkaline earth metals or lanthanides. Even more specifically, the heterogeneous acidic catalyst is free of calcium, sodium, potassium and / or lanthanum. The term "free of" is understood as the catalyst contains less than 1 ppm, even less than 0.5 ppm, even less than 100 ppb, even less than 10 ppb, even less than 1 ppb of alkali metals or alkaline earth metals or lanthanides, and even the catalyst is free of alkali metals or alkaline earth metals or lanthanides.

[0021] According to a particular embodiment of the invention, the heterogeneous acidic catalyst has a hydrophilic surface.

[0022] According to any embodiment of the present invention, the zeolite is a large pore zeolite.

[0023] The term "large pore zeolite" has its usual meaning in the art, i.e. a 12-ring zeolite having pore sizes falling within the range between 6.0 angstroms and 8 angstroms, in particular between 6.0 angstroms and 7.5 angstroms.

[0024] According to any embodiment of the present invention, the zeolite has a FAU, BEA or MOR topology. In particular, the zeolite has a FAU topology. In particular, the zeolite does not have an MFI topology.

[0025] According to any embodiment of the present invention, the heterogeneous acidic catalyst is a dealuminated zeolite. Dealuminization is conventionally understood as the removal of aluminum atoms from the zeolite structure. Dealuminization increases the silicon:aluminum ratio of the zeolite. Non-limiting examples of suitable methods of dealumination known in the art are hydrothermal treatment, acidic treatment, treatment with gaseous halides or halogens, or complexation with chelating agents, or a combination of the above mentioned treatments. Those skilled in the art are aware of these methods and how to carry them out.

[0026] According to any embodiment of the present invention, the zeolite having FAU topology is a dealuminated ultrastable Y (USY) zeolite. USY zeolites are typically prepared from Y zeolites to increase their stability and improve their catalytic activity by removing the framework aluminum with a combination of treatments including ion exchange, steaming, acid leaching and calcination. Such treatments are described, for example, in US5601798 and US4477336 and are well known to those skilled in the art.

[0027] According to any embodiment of the present invention, the silicon:aluminum ratio is greater than or equal to 2.5:1, even greater than or equal to 3:1, even greater than or equal to 5:1, even greater than or equal to 8:1.

[0028] According to any embodiment of the present invention, the silicon:aluminum ratio is comprised in the range between 2.5:1 and 300:1. In particular, the silicon:aluminum ratio is comprised in the range between 3:1 and 300:1. In particular, the silicon:aluminum ratio is comprised in the range between 5:1 and 300:1. In particular, the silicon:aluminum ratio is comprised in the range between 5:1 and 150:1. In particular, the silicon:aluminum ratio is comprised in the range between 10:1 and 150:1. Even more particularly, the silicon:aluminum ratio is comprised in the range between 10:1 and 70:1.

[0029] According to any embodiment of the invention, the zeolite is used in its proton form. The latter is provided directly by the manufacturer and can be used as is or, if necessary, can be obtained by calcining an ammonium exchanger. Ideally, all samples should be preactivated before the reaction. Preactivation can be carried out by heating the zeolite at a temperature comprised between 300 ° C and 600 ° C for at least 1 hour.

[0030] Heterogeneous acid catalysts can be added to the reaction medium of the process of the invention to form the oxacyclopentane or oxacyclohexane derivatives of formula (II) in a wide range of concentrations. As non-limiting examples, values ​​of the heterogeneous acid catalyst concentration can be mentioned ranging from 0.5% to 20% by weight, relative to the total amount of 1,4-diol or 1,5-diol. In particular, the heterogeneous acid catalyst concentration can be comprised between 1% and 15% by weight. Even more particularly, the heterogeneous acid catalyst concentration can be comprised between 3% and 10% by weight. It goes without saying that the process also works with more catalyst. However, the optimum concentration of the heterogeneous acid catalyst will depend, as the skilled person knows, on the nature of the latter, on the nature of the substrate, on the temperature and on the desired reaction time.

[0031] Heterogeneous acidic catalysts are commercially available compounds or can be prepared by several methods, such as those reported in US Patent Publication No. 20040141911, US Patent No. 6,054,113, and US Patent No. 4,840,930.

[0032] Non-limiting examples of suitable heterogeneous acid catalysts include CBV720 (supplied by Zeolyst), CBV760 (supplied by Zeolyst), CBV780 (supplied by Zeolyst), HSZ-385HUA (supplied by Zeolyst), CBV21A (supplied by Zeolyst), HSZ-640HOA (supplied by Tosoh), CP814E * (Supplied by Zeolyst), CP814C * (supplied by Zeolyst) or CP811C-300 (supplied by Zeolyst).

[0033] According to any one of the embodiments of the present invention, the inventive process for producing an oxacyclopentane or oxacyclohexane derivative of formula (II) is not carried out under supercritical conditions, i.e. using a supercritical fluid, such as supercritical water or supercritical CO2.

[0034] According to any one of the embodiments of the present invention, the inventive process for preparing oxacyclopentane or oxacyclohexane derivatives of formula (II) is carried out at a temperature comprised between 0° C. and 150° C. In particular, the temperature ranges between 30° C. and 70° C. Of course, the skilled person can also select the preferred temperature depending on the melting and boiling points of the starting materials and the final product as well as the desired reaction time, conversion or selectivity.

[0035] The process of the present invention for preparing oxacyclopentane or oxacyclohexane derivatives of formula (II) can be carried out in the presence or absence of a solvent. If a solvent is required or used for practical reasons, any current solvent for such reaction types can be used for the purposes of the present invention. Non-limiting examples include C 6~12 Examples of suitable solvents include aromatic solvents such as xylene, toluene, 1,3-diisopropylbenzene, cumene pseudocumene, anisole or chlorobenzene or mixtures thereof, hydrocarbon solvents such as cyclohexane, heptane or mixtures thereof, nitrile solvents such as acetonitrile, ester solvents such as ethyl acetate or ether solvents such as tetrahydrofuran, diethyl ether, methyltetrahydrofuran or mixtures thereof. The choice of solvent depends on the nature of the substrate and / or catalyst, and the skilled person is well able to select the most suitable solvent in each case to optimize the reaction.

[0036] The process of the present invention for preparing the oxacyclopentane or oxacyclohexane derivatives of formula (II) may be carried out under batch or continuous conditions.

[0037] Water is formed during the process of the invention and may be removed from the reaction mixture, for example by azeotropic distillation or by carrying out the process of the invention under a slight reduced pressure.

[0038] The process of the present invention for preparing oxacyclopentane or oxacyclohexane derivatives of formula (II) may be carried out under atmospheric pressure or under slightly reduced pressure.

[0039] According to any one of the embodiments of the present invention, the 1,4-diol or 1,5-diol comprises a primary alcohol group and a tertiary alcohol group.

[0040] According to any one of the above embodiments of the present invention, the 1,4-diol or 1,5-diol of formula (I) is 9~ C 20 It is a compound.

[0041] According to any one of the embodiments of the present invention, m may be 1. In other words, the compound of formula (I) is a 1,4-diol and the compound of formula (II) is an oxacyclopentane derivative.

[0042] According to any one of the embodiments of the present invention, R 2 and R 3 Together, C 3~18 In particular, R may represent an alkanediyl group. 2 and R 3 Together, C 3~18 may represent a linear or branched alkanediyl group.

[0043] According to any one of the embodiments of the present invention, the 1,4-diol has the formula [ka] [In the formula, n is 0 or 1, Each R 7 , R 8 , R 9 , R 10 C optionally containing, separately and independently of each other, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group; 1~9 R represents an alkyl group; 6 C optionally containing one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~9 Represents an alkyl group; R 6 and R 7 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups. 3~9 represents a linear or branched alkanediyl group, and / or R 8 and R 9 Together, C 1~2 represents a linear alkanediyl group, and / or R 9 and R 10 Together, C 3~10 represents a linear or branched alkanediyl, and / or R 7 and R 10 Together, C 1~3 represents a linear or branched alkanediyl; and R 11 is a hydrogen atom or C 1~3 represents a straight-chain or branched alkyl group] in the form of any one of its stereoisomers or a mixture thereof.

[0044] According to any one of the embodiments of the present invention, the oxacyclopentane derivative has the formula [ka] [In the formula, n is 0 or 1, Each R 7 , R 8 , R 9 , R 10 C optionally containing, separately and independently of each other, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group; 1~9 R represents an alkyl group; 6 C optionally containing one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~9 Represents an alkyl group; R 6 and R 7C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups. 3~9 represents a linear or branched alkanediyl group, and / or R 8 and R 9 Together, C 1~2 represents a linear alkanediyl group, and / or R 9 and R 10 Together, C 3~10 represents a linear or branched alkanediyl, and / or R 7 and R 10 Together, C 1~3 represents a linear or branched alkanediyl; and R 11 is a hydrogen atom or C 1~3 represents a straight-chain or branched alkyl group] in the form of any one of its stereoisomers or a mixture thereof.

[0045] According to a particular embodiment, the compound of formula (III) may be a monocyclic, bicyclic or tricyclic compound, and the compound of formula (IV) may be a bicyclic or tricyclic compound.Preferably, the compound of formula (III) may be a monocyclic or bicyclic compound, and the compound of formula (IV) may be a bicyclic or tricyclic compound.Even more preferably, the compound of formula (III) may be a bicyclic compound, and the compound of formula (IV) may be a tricyclic compound.The above compound of formula (III) may be synthetic or natural.

[0046] According to any one of the embodiments of the present invention, R 7 , R 8 , R 9 , R 10 C optionally containing, independently of each other, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group 1~9 may represent an alkyl group; R 6C optionally containing one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~9 may represent an alkyl group; or R 6 and R 7 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups. 3~9 may represent a linear or branched alkanediyl group, and / or R 8 and R 9 Together, C 1~2 may represent a linear or branched alkanediyl group, and / or R 9 and R 10 Together, C 3~9 may represent a linear or branched alkanediyl group, and / or R 7 and R 10 Together, C 1~3 In particular, R may represent a linear or branched alkanediyl group. 7 , R 8 , R 9 , R 10 C optionally containing, independently of each other, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group 1~6 may represent an alkyl group; R 6 C optionally containing one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~9 may represent an alkyl group; or R 6 and R 7 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups. 3~8 may represent a linear or branched alkanediyl group, and / or R 8 and R 9 Together, C 1~2 may represent a linear alkanediyl group, and / or R 9 and R10 Together, C 3~8 may represent a linear or branched alkanediyl group, and / or R 7 and R 10 Together, C 1~3 In particular, R may represent a linear or branched alkanediyl group. 7 , R 8 , R 9 , R 10 C optionally containing, independently of each other, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group 1~4 may represent an alkyl group; R 6 C optionally containing one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~9 may represent an alkyl group; or R 6 and R 7 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups. 3~8 may represent a linear or branched alkanediyl group, and / or R 8 and R 9 Together, C 1~2 may represent a linear alkanediyl group, and / or R 9 and R 10 Together, C 3~8 may represent a linear or branched alkanediyl group, and / or R 7 and R 10 Together, C 1~3 It may represent a linear or branched alkanediyl group.

[0047] According to any one of the embodiments of the present invention, the above R 7 The group is a hydrogen atom or a C 1~3 In particular, R 7 The group may represent a hydrogen atom or a methyl group. Even more specifically, R 7 The group may represent a hydrogen atom.

[0048] According to any one of the embodiments of the present invention, the above R 8 The group is a hydrogen atom or a C 1~3 In particular, R 8 The group may represent a hydrogen atom or a methyl group. Even more specifically, R 8 The group may represent a hydrogen atom.

[0049] According to any one of the embodiments of the present invention, the above R 9 The group is a hydrogen atom or a C 1~3 In particular, R 9 The group may represent a hydrogen atom or a methyl group. Even more specifically, R 9 The group may represent a hydrogen atom.

[0050] According to any one of the embodiments of the present invention, the above R 10 The group is a hydrogen atom or a C 1~3 In particular, R 10 The group may represent a hydrogen atom or a methyl group. Even more specifically, R 10 The group may represent a hydrogen atom.

[0051] According to any one of the embodiments of the present invention, the above R 6 and R 7 Together, C 3~6 It may represent a linear or branched alkanediyl group, or more preferably a C4 branched alkanediyl group.

[0052] According to any one of the embodiments of the present invention, the above R 8 and R 9 Together, C 1~2 It may represent a linear alkanediyl group or more preferably a C2 linear alkanediyl group.

[0053] According to any one of the embodiments of the present invention, the above R 9 and R 10 Together, C3~6 It may represent a linear or branched alkanediyl group, or more preferably a C6 branched alkanediyl group.

[0054] According to any one of the embodiments of the present invention, the above R 7 and R 10 may be taken together to represent a C3 branched alkanediyl group.

[0055] According to any one of the embodiments of the present invention, n may be 1.

[0056] According to any one of the embodiments of the present invention, the 1,4-diol has the formula [ka] [In the formula, each R 6 and R 11 has the same meaning as defined above, and R 12 and R 13 are independent of each other, C 1~3 The compound may be in the form of any one of its stereoisomers or a mixture thereof, wherein R represents a straight-chain or branched alkyl group.

[0057] According to any one of the embodiments of the present invention, the oxacyclopentane derivative has the formula [ka] [In the formula, each R 6 , R 11 , R 12 and R 13 has the same meaning as defined above] in the form of any one of its stereoisomers or a mixture thereof.

[0058] According to any one of the embodiments of the present invention, R 6 C optionally containing one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~6 In particular, R6 C optionally containing one or two functional groups selected from ether, ester and carbonyl groups 1~4 In particular, R 6 C optionally containing one or two functional groups selected from ether, ester and carbonyl groups 1~3 It may be a linear or branched alkyl group. In particular, R 6 may be a methyl, ethyl or n-propyl group. Even more specifically, R 6 may be a methyl group.

[0059] According to any one of the embodiments of the present invention, R 11 is C 1~3 It may be a linear alkyl group. In particular, R 11 may be a methyl or ethyl group. Even more specifically, R 11 may be a methyl group.

[0060] According to any one of the embodiments of the present invention, R 12 may be a methyl or ethyl group. Even more specifically, R 12 may be a methyl group.

[0061] According to any one of the embodiments of the present invention, R 13 may be a methyl or ethyl group. Even more specifically, R 13 may be a methyl group.

[0062] According to a particular embodiment of the invention, the 1,4-diol may be 1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol and the corresponding oxacyclopentane derivative may be 3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan, which has four stereocenters and is in the R or S configuration or a mixture thereof. In other words, the 1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol may be in the form of a substantially pure stereoisomer or a mixture of stereoisomers. According to a particular embodiment of the invention, compound (I), (III) or (V) may be 1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol in the form of a mixture of stereoisomers containing at least 80% of both stereoisomers (1RS,2RS,4aSR,8aSR)-1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol and (1RS,2SR,4aSR,8aSR)-1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol. In particular, compound (I), (III) or (V) may be 1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol in the form of a mixture of stereoisomers containing at least 50% of (1RS,2RS,4aSR,8aSR)-1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol. Even more particularly, compound (I), (III) or (V) may be 1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol in the form of a mixture of stereoisomers containing at least 75% of (1RS,2RS,4aSR,8aSR)-1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol. According to certain embodiments of the present invention, compound (I), (III) or (V) may be (1RS,2RS,4aSR,8aSR)-1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol.For clarity, the expression "1RS,2RS,4aSR,8aSR" means an equimolar mixture of 1R,2R,4aS,8aS and 1S,2S,4aR,8aR, and the expression "1RS,2SR,4aSR,8aSR" means an equimolar mixture of 1R,2S,4aS,8aS and 1S,2R,4aR,8aSR. According to a particular embodiment of the present invention, compound (I), (III) or (V) may be (1R,2R,4aS,8aS)-1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol.

[0063] According to any embodiment of the present invention, the method of the present invention is stereoselective, i.e., the cyclodehydration of 1,4-diol (1R,2R,4aS,8aS)-1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol provides (3aR,5aS,9aS,9bR)-3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan.

[0064] Compounds of formula (I), (III) and (V) can be prepared by several methods known in the art, for example, in the case of 1-(2-hydroxyethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol, which can be obtained by hydrogenation of sclareolide, as reported in WO2019175158.

[0065] Exemplary methods for carrying out the methods of the present invention are reported in the Examples hereinafter. EXAMPLES

[0066] The invention will now be described in further detail by the following examples, in which abbreviations have their usual meaning in the art and temperatures are given in degrees Celsius (° C.). Gas chromatography was prepared on an Agilent 7890 A series equipped with a HP5 column (30 m×0.25 mm ID, 0.25 μm film) and tetradecane was used as the internal standard.

[0067] [Example 1] (Typical Experimental Procedure for Preactivation of Zeolite Catalysts) a) In still air 10 g of the neat zeolite, as reported in Table I, was placed in a muffle furnace (static air) and heated at 10 °C for 10 min. -1 The mixture was heated to 550° C. for 3 hours.

[0068] b) Under flowing gas 30 kg of the neat zeolite as reported in Table I, specifically CBV780, was placed in a tubular oven and heated at 5°C for 5 min under a nitrogen or air (50 mL / min) flow. -1 The mixture was heated to 550° C. for 3 hours.

[0069] [Example 2] (General cyclodehydration procedure for preparing oxacyclopentanes starting from 1,4-diols) (1S,2R,4aS,8aS)-1-(hydroxymethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol (1,4-diol, 80 g, 0.317 moles) was charged to a 500 ml reactor, diluted with toluene (320 g, 3.47 moles) at 20 wt % and then heated to 50° C. Once the desired temperature was reached, preactivated zeolite from Table I (6.42 g - preactivation was performed as reported in Example 1) was added and the reaction was stirred for 6 hours to give 93.5% of the desired (3aR,5aS,9aS,9bR)-3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan product (oxacyclopentane). The results of cyclodehydration using various zeolite topologies and structures are reported in Table I and demonstrate the important role of zeolite acidity and topology. [Table 1-1] [Table 1-2]

[0070] [Example 3] (Dehydration cyclization to produce oxacyclopentanes starting from 1,4-diols using different solvents) Example 2 was repeated using preactivated CBV780 and carrying out the reactions in various solvents as included in Table II. [Table 2]

[0071] [Example 4] (Dehydration cyclization to produce oxacyclopentanes starting from 1,4-diols under reduced pressure) Example 2 was repeated using 4 g of CBV780 (5 wt%) and carrying out the reaction under reduced pressure for 12 h to gradually remove the water formed in-situ. After separation by filtration and distillation, an isolated yield of 90.0 mol% (3aR,5aS,9aS,9bR)-3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan was obtained with 99.9 GC%.

[0072] [Example 5] (Dehydration cyclization to produce oxacyclopentanes starting from 1,4-diols using non-preactivated CBV780) Example 2 was repeated using 5 wt. % of non-preactivated CBV780 (neat) and carrying out the reaction at 70° C. for 4 hours. Under these conditions, 88% of the desired (3aR,5aS,9aS,9bR)-3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan was obtained. The reaction can also be carried out at 50° C. for 24 hours to give the desired oxacyclopentane with 90 GC%.

[0073] [Example 6] (Dehydration and cyclization to produce oxacyclopentanes starting from 1,4-diols using strongly acidic ion exchange resins under dry conditions) (1S,2R,4aS,8aS)-1-(hydroxymethyl)-2,5,5,8a-tetramethyldecahydronaphthalen-2-ol (1,4-diol, 80 g, 0.317 moles) was charged to a 500 ml reactor, diluted with toluene (320 g, 3.47 moles) at 20% by weight, and then heated to 50° C. Once the desired temperature was reached, Amberlyst A-15 dry matter (4 g) was added and the reaction was stirred for 6 hours to give 69.7% of the desired (3aR,5aS,9aS,9bR)-3a,6,6,9a-tetramethyldodecahydronaphtho[2,1-b]furan product (oxacyclopentane). Similar results were obtained when Amberlyst A-35 dry matter was used.

Claims

1. The following formula: 【Chemistry 1】 [Wherein m is 1 or 2; Each R 1 and R 2 C optionally contains one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups, independently of each other. 1~18 represents an alkyl group; 3 and R 4 C optionally containing, separately and independently of one another, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group; 1~18 represents an alkyl group; 1 and R 2 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups; 4~11 represents an alkanediyl group, and / or R 2 and R 3 Together, C 2~18 represents an alkanediyl group, and / or R 3 and R 4 Together, C 4~9 represents an alkanediyl group, and / or R 1 and R 4 Together, C 2~9 represents an alkanediyl group; R 5 is a hydrogen atom or C 1~3 represents an alkyl group] in the form of any one of its stereoisomers or a mixture thereof, comprising the steps of: 【Chemistry 2】 [In the formula, m, R 1 , R 2 , R 3 , R 4 and R 5 has the same meaning as defined for the oxacyclopentane or oxacyclohexane derivatives of formula (II), in the form of any one of its stereoisomers or a mixture thereof, wherein the cyclodehydration is carried out in the presence of a heterogeneous acidic catalyst, provided that a) the heterogeneous acid catalyst is not a clay; b) when the heterogeneous acidic catalyst is an aluminosilicate catalyst, the silicon:aluminum ratio is 3:1 or greater; and c) The process is not carried out under supercritical conditions. The method is provided as follows.

2. The method of claim 1 , wherein the heterogeneous acidic catalyst is crystalline.

3. 3. The method of claim 1 or 2, wherein the heterogeneous acidic catalyst comprises silicon and a second metal selected from the group consisting of aluminum, boron, iron, tin, titanium, zirconium, hafnium and mixtures thereof.

4. 3. The process of claim 1 or 2, wherein the heterogeneous acidic catalyst does not contain calcium, potassium, sodium and / or lanthanum.

5. 3. The process of claim 1 or 2, wherein the heterogeneous acidic catalyst is an aluminosilicate catalyst.

6. The process of claim 5, wherein the aluminosilicate catalyst is a zeolite.

7. 7. The method of claim 6, wherein the zeolite is a large pore zeolite.

8. 7. The method of claim 6, wherein the zeolite has a FAU, BEA or MOR topology.

9. 3. The method according to claim 1 or 2, wherein the silicon:aluminium ratio is comprised in the range between 3:1 and 300:1, preferably in the range between 5:1 and 300:

1.

10. 9. The method of claim 8, wherein the zeolite having the FAU topology is a dealuminated ultrastable Y (USY) zeolite.

11. 7. The process of claim 6, wherein the zeolite is used in its proton form.

12. 3. The method of claim 1 or 2, wherein m is 1.

13. The 1,4-diol has the following formula: 【Chemistry 3】 [Wherein, n is 0 or 1; Each R 7 , R 8 , R 9 , R 10 C optionally containing, separately and independently of one another, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group; 1~9 represents an alkyl group; R 6 C optionally contains one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~9 represents an alkyl group; R 6 and R 7 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups; 3~9 represents a linear or branched alkanediyl group, and / or R 8 and R 9 Together, C 1~2 represents a linear alkanediyl group, and / or R 9 and R 10 Together, C 3~10 represents a linear or branched alkanediyl, and / or R 7 and R 10 Together, C 1~3 represents a linear or branched alkanediyl; and R 11 is a hydrogen atom or C 1~3 3. The method according to claim 1 or 2, wherein the compound is in the form of any one of its stereoisomers or a mixture thereof, wherein R represents a linear or branched alkyl group.

14. The oxacyclopentane derivative is represented by the following formula: 【Chemistry 4】 [Wherein, n is 0 or 1; Each R 7 , R 8 , R 9 , R 10 C optionally containing, separately and independently of one another, a hydrogen atom or one or two functional groups selected from among an ether, ester, carbonyl, amine, amide or alcohol group; 1~9 represents an alkyl group; R 6 C optionally contains one or two functional groups selected from ether, ester, carbonyl, amine, amide or alcohol groups; 1~9 represents an alkyl group; R 6 and R 7 C optionally containing one or two functional groups selected from among ether, ester, carbonyl, amine, amide or alcohol groups; 3~9 represents a linear or branched alkanediyl group, and / or R 8 and R 9 Together, C 1~2 represents a linear alkanediyl group, and / or R 9 and R 10 Together, C 3~10 represents a linear or branched alkanediyl, and / or R 7 and R 10 Together, C 1~3 represents a linear or branched alkanediyl; and R 11 is a hydrogen atom or C 1~3 3. The method according to claim 1 or 2, wherein the compound is in the form of any one of its stereoisomers or a mixture thereof, wherein R represents a linear or branched alkyl group.

15. The 1,4-diol has the following formula: 【Chemistry 5】 [In the formula, each R 6 and R 11 has the same meaning as defined in claim 13, and each R 12 and R 13 are, independently of each other, C 1~3 3. The method according to claim 1 or 2, wherein the compound is in the form of any one of its stereoisomers or a mixture thereof, wherein the alkyl group is a straight-chain or branched alkyl group.