| WO2005012222A1 | 2005-02-10 | |||
| WO2009034510A2 | 2009-03-19 | |||
| WO2004050595A1 | 2004-06-17 |
| CN107759445A | 2018-03-06 | |||
| EP0472966A1 | 1992-03-04 | |||
| US2470872A | 1949-05-24 | |||
| US2671058A | 1954-03-02 | |||
| US2981697A | 1961-04-25 | |||
| US1926148A | 1933-09-12 | |||
| US20040141911A1 | 2004-07-22 | |||
| US6054113A | 2000-04-25 | |||
| US4840930A | 1989-06-20 | |||
| EP0398636A1 | 1990-11-22 | |||
| US5601798A | 1997-02-11 | |||
| US4477336A | 1984-10-16 |
PIRES ELISABET ET AL: "Optimization of the Synthesis of Glycerol Derived Monoethers from Glycidol by Means of Heterogeneous Acid Catalysis", MOLECULES, vol. 23, no. 11, 6 November 2018 (2018-11-06), pages 2887, XP055981171, DOI: 10.3390/molecules23112887
FENG XIAO ET AL: "Creation of Exclusive Artificial Cluster Defects by Selective Metal Removal in the (Zn, Zr) Mixed-Metal UiO-66", JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, vol. 143, no. 51, 7 December 2021 (2021-12-07), pages 21511 - 21518, XP055981173, ISSN: 0002-7863, DOI: 10.1021/jacs.1c05357
"Rompp Chemie Lexikon", 1990, GEORG THIEME VERLAG, pages: 1311
HALASZ ET AL., MOLECULAR PHYSICS, vol. 100, 2002, pages 3232 - 3232
| CLAIMS A process for the preparation of a compound of formula (I) in the form of any of its stereoisomers or a mixture thereof; wherein Y is a sulfur atom, an oxygen atom or a NH group, and R1 represents a C1-12 alkyl, C2-12 alkenyl, a C5-12 cycloalkyl or C5-12 cycloalkenyl group, each optionally substituted by 1 to 3 CM alkyl groups; and each R2, R3, R4 represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group; comprising the reaction of a compound of formula (II) wherein X is a thiol group, alcohol group or primary amine group, and wherein Ri and R2 have the same meaning as defined above; with an epoxide of formula (III) wherein R3 and R4 have the same meaning as defined above; in the presence of a heterogeneous acidic catalyst. The process according to claim 1 , wherein the compound of formula (II) is of formula (Ha) in the form of any of its stereoisomers or a mixture thereof, wherein one dotted line is a carbon-carbon single or double bond and the other is a carboncarbon single bond; and X is a thiol group, alcohol group or primary amine group, and each R2, Rs, Re, R7 and Rs represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group; or R? and Rs are linked to each other and form a C5-7 cycloalkyl or cycloalkenyl group; and the compound of formula (I) is of formula (la) in the form of any of its stereoisomers or a mixture thereof, wherein Y is a sulfur atom, an oxygen atom or a NH group, and the dotted line, R2, Rs, Re, R7 and Rs have the same meaning as defined above; and each R3 and R4 represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group. The process according to any one of the preceding claims, wherein the compound of formula (II) is of formula (He) in the form of any of its stereoisomers or a mixture thereof, wherein X is a thiol group, alcohol group or primary amine group, and R2 a hydrogen atom or a C1-4 alkyl group; and the compound of formula (I) is of formula (Ic) in the form of any of its stereoisomers or a mixture thereof, wherein Y is a sulfur atom, an oxygen atom or a NH group, and each R2, R3, R4 represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group. The process according to any one of the preceding claims, wherein X is an alcohol group and Y is an oxygen atom. The process according to any one of the preceding claims, wherein R2 represents a methyl group. The process according to any one of the preceding claims, wherein each R3 and R4 represent a methyl group. The process according to any one of the preceding claims, wherein the heterogeneous acidic catalyst is an aluminosilicate catalyst. The process according to any one of the preceding claims, wherein the heterogeneous acidic catalyst is a zeolite or a clay. The process according to any one of the preceding claims, wherein the zeolite is a large pore zeolite. The process according to any one of the preceding claims, wherein the heterogeneous acidic catalyst is a hydrophobic zeolite. The process according to any one of the preceding claims, wherein the heterogeneous acidic catalyst is a zeolite having a FAU topology. The process according to any one of the preceding claims, wherein the heterogeneous acidic catalyst is a dealuminated ultrastable Y-type (USY) zeolite. The process according to any one of the preceding claims, wherein the Silicon : Aluminum ratio is in the range between 5 : 1 and 350 : 1 , preferably between 15 : 1 and 300 : 1 , more preferably between 30 : 1 and 250 : 1. The process according to any of the preceding claims used for the preparation of a compound of formula (IV) in the form of any of its stereoisomers or a mixture thereof; wherein Y is a sulfur atom, an oxygen atom or a NH group, and Ri represents a C1-12 alkyl, C2-12 alkenyl, a C5-12 cycloalkyl or C5-12 cycloalkenyl group, each optionally substituted by 1 to 3 CM alkyl groups; and each R2, R3, R4 represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group; and R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably a CM alkyl group, a C2-4 alkenyl group, a C3-6 cycloalkyl group; preferably a Ci-3 alkyl group, a C2-3 alkenyl group, a C3-5 cycloalkyl group; preferably an ethyl group, a vinyl group, a cyclopropyl or a cyclopentyl group, more preferably an ethyl group; and the compound of formula (IV) is formed by reacting the compound of formula (I) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group. The process according to claim 14, wherein the compound of formula (IV) is of formula (IVa) in the form of any of its stereoisomers or a mixture thereof; wherein one dotted line is a carbon-carbon single or double bond and the other is a carboncarbon single bond; and Y is a sulfur atom, an oxygen atom or a NH group, and each R2, R3, R4, Rs, Re and R? represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group; and Rs represents a CM alkyl group; or R? and Rs are linked to each other and form a C5-7 cycloalkyl or cycloalkenyl group; and R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably a C1-4 alkyl group, a C2-4 alkenyl group, a C3-6 cycloalkyl group; preferably a C1-3 alkyl group, a C2-3 alkenyl group, a C3-5 cycloalkyl group; preferably an ethyl group, a vinyl group, a cyclopropyl or a cyclopentyl group, more preferably an ethyl group; and the compound of formula (IVa) is formed by reacting the compound of formula (la) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group. The process according to anyone of claims 14 to 15, wherein the compound of formula (IV) is of formula (IVc) in the form of any of its stereoisomers or a mixture thereof; wherein Y is a sulfur atom, an oxygen atom or a NH group, and each R2, R3 and R4 represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group; and R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably a CM alkyl group, a C2-4 alkenyl group, a C3-6 cycloalkyl group; preferably a C1-3 alkyl group, a C2-3 alkenyl group, a C3-5 cycloalkyl group; preferably an ethyl group, a vinyl group, a cyclopropyl or a cyclopentyl group, more preferably an ethyl group; and the compound of formula (IVc) is formed by reacting the compound of formula (Ic) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group. |
Technical field of the invention
The present invention relates to the field of organic synthesis and, more specifically, it concerns a process for the preparation of an ether, thioether or secondary amine of formula (I) comprising the reaction of an alcohol, thiol or amine of formula (II) with an epoxide of formula (III) performed in the presence of a heterogeneous acidic catalyst.
Background of the invention
The ether, thioether or secondary amine derivatives represent highly desirable skeletons which could be used as such or as key intermediates useful to prepare more complex compounds in different fields such as, among others, perfumery, cosmetic, pharmaceutic or agrochemistry. A relevant ether derivative is for example 2-((3,3-dimethylcyclohexyl)methoxy)-2- methylpropan-1-ol, which is used for the synthesis of Helvetolide® (trademark from Firmenich SA, Suisse), representing one of the most sought-after ingredients in the perfumery industry. However, the possibilities of reaction pathways for the synthesis of Helvetolide® are limited and passes through 2-((3,3-dimethylcyclohexyl)methoxy)-2-methylpropan-1-ol as a key intermediate. Conventionally, a-3,3-Trimethylcyclohexanemethanol is reacted with 1 ,2-epoxy- 2-methylpropan in the presence of a homogeneous acidic catalyst, e.g. a soluble Lewis acid. Unfortunately, the selectivity and consequently the conversion efficiency (yield) of this reaction is low. This lack of efficiency mainly originates from unwanted side reactions comprising ring opening reactions of a-3,3-Trimethylcyclohexanemethanol and formation of heavier products coming from the reaction of 1 ,2-epoxy-2-methylpropan with the 2-((3,3- dimethylcyclohexyl)methoxy)-2-methylpropan-1-ol in-situ generated. In addition, homogeneous catalysts suitable for this reaction can as well be corrosive for the equipment used for performing the reaction. Furthermore, the use of homogeneous catalysts that require a basic post-reaction washing step appeared particularly problematic owing to the nature of 2- ((3,3-dimethylcyclohexyl)methoxy)-2-methylpropan-1-ol, which behaves as surfactant.
Consequently, there is a need to develop a reaction process with improved conversion efficiency and selectivity and therefore an improved yield and with a simplified workup procedure.
The present invention allows solving the above problem by using a heterogenous acidic catalyst in order to prepare an ether, thioether or secondary amine of formula (I). To the best of our knowledge, the invention’s conditions have never been reported in the prior art. Detailed description of the invention
Surprisingly, it has now been discovered that the preparation of a compound of formula (I) by reaction of a compound of formula (II) with an epoxide of formula (III) in presence of a heterogeneous acidic catalyst allows preparing a compound of formula (I) with high yield and high selectivity.
Therefore, a first object of the present invention is a process for the preparation of a compound of formula (I) in the form of any of its stereoisomers or a mixture thereof; wherein
Y is a sulfur atom, an oxygen atom or a NH group, and
R1 represents a C1-12 alkyl, C2-12 alkenyl, a C5-12 cycloalkyl or C5-12 cycloalkenyl group, each optionally substituted by 1 to 3 CM alkyl groups; and each R2, R3, R4 represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group; comprising the reaction of a compound of formula (II) wherein X is a thiol group, alcohol group or primary amine group, and wherein R1 and R2 have the same meaning as defined above; with an epoxide of formula (III) wherein R3 and R4 have the same meaning as defined above; in the presence of a heterogeneous acidic catalyst. For the sake of clarity, by the expression “any one of its stereoisomers or a mixture thereof”, or the similar, it is meant the normal meaning understood by a person skilled in the art, i.e. that the compounds cited in the invention can be a pure enantiomer or a mixture of enantiomers. In other words, the compounds cited in the invention may possess at least one stereocenter which can have two different stereochemistries (e.g. R or S), e.g. the R 1 group may comprise at least one stereocenter. Said compounds may even be in the form of a pure enantiomer or in the form of a mixture of enantiomers. The compounds cited in the invention may even be in the form of a pure diastereoisomer or in the form of a mixture of diastereoisomers when said compounds possess more than one stereocenter. Said compounds can be in a racemic form or scalemic form. Therefore, said compounds can be one stereoisomer or in the form of a composition of matter comprising, or consisting of, various stereoisomers.
It is understood that if Y is a sulfur atom, the compound comprises a thiolether group. It is understood that if Y is an oxygen atom, the compound comprises an ether group. It is understood that if Y is a NH group, the compound comprises a secondary amine group.
The term “optionally” is understood that a group can or cannot comprise a certain functional group or substituent.
The term “alkyl group” is understood as comprising linear or branched alkyl groups.
The term “alkenyl group” is understood as comprising linear or branched alkenyl groups.
The expression “C1-12 alkyl, C2-12 alkenyl, a C5-12 cycloalkyl or C5-12 cycloalkenyl group, each optionally substituted by 1 to 3 CM alkyl groups” is understood as the cycloalkyl or the cycloakenyl being optionally substituted by 1 to 3 C1-4 alkyl groups.
According to a particular embodiment, X is an alcohol group and Y is an oxygen atom.
According to a particular embodiment, R1 is a C1-10 alkyl, C2-10 alkenyl, a C5-10 cycloalkyl or C5- 10 cycloalkenyl group, each optionally substituted by 1 to 3 CM alkyl groups. Particularly, R1 is a C1-8 alkyl, C2-8 alkenyl, a C5-10 cycloalkyl or C5-10 cycloalkenyl group, each optionally substituted by 1 to 3 C1-4 alkyl groups. Particularly, R1 is a C1-6 alkyl, C2-6 alkenyl, a C5-10 cycloalkyl or C5-10 cycloalkenyl group, each optionally substituted by 1 to 3 C1-4 alkyl groups. Particularly, R1 is a C5-10 cycloalkyl or C5-10 cycloalkenyl group, preferably a C5-8 cycloalkyl or C5-8 cycloalkenyl group, , preferably a C5-7 cycloalkyl or C5-7 cycloalkenyl group, preferably a C5-6 cycloalkyl or C5-6 cycloalkenyl group, more preferably a Ce cycloalkyl group, each optionally substituted by 1 to 3 C1-4 alkyl groups, preferably by 1 to 2 C1-3 alkyl groups, even more preferably by 1 to 2 C1-2 alkyl groups. Even more particularly, R1 is a 3,3-dimetly-1- cyclohexyl group.
According to a particular embodiment, R 2 represents a hydrogen atom or a C1-3 alkyl group.
Particularly, R 2 represents a methyl or ethyl group, more preferably a methyl group.
According to a particular embodiment, R 3 represents a hydrogen atom or a C1-3 alkyl group.
Particularly, R 3 represents a methyl or ethyl group, more preferably a methyl group.
According to a particular embodiment, R 4 represents a hydrogen atom or a C1-3 alkyl group.
Particularly, R 4 represents a methyl or ethyl group, more preferably a methyl group.
According to a more particular embodiment, each R 3 and R 4 represent a methyl group.
According to a particular embodiment, the present invention is directed to a process, wherein the compound of formula (II) is of formula (Ila) in the form of any of its stereoisomers or a mixture thereof, wherein one dotted line is a carbon-carbon single or double bond and the other is a carbon-carbon single bond; and
X is a thiol group, alcohol group or primary amine group, and each R2, Rs, Re, R7 and Rs represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group; or
R7 and Rs are linked to each other and form a C5-7 cycloalkyl or cycloalkenyl group; and the compound of formula (I) is of formula (la) in the form of any of its stereoisomers or a mixture thereof, wherein
Y is a sulfur atom, an oxygen atom or a NH group, and the dotted line, R2, Rs, Re, R7 and Rs have the same meaning as defined above; and each R3 and R4 represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group.
For the sake of clarity, by the expression “one dotted line is a carbon-carbon single or double bond and the other is a carbon-carbon single bond” it is meant the normal meaning understood by a person skilled in the art, i.e. that the whole bonding (solid and dotted line) between the carbon atoms connected by said dotted line is a carbon-carbon single or double bond.
It is understood by a person skilled in the art that in case Rs represents a hydrogen atom, the dotted line between Rs and the neighboring carbon atom represents a hydrogen-carbon single bond.
For the sake of clarity, by the expression “in case R? and Rs are linked to each other, they form a C5-7 cycloalkyl or cycloalkenyl group” it is meant that R7 and Rs can be chemically connected via a carbon-carbon single or double bond forming a C5-7 cycloalkyl or cycloalkenyl group comprising the other carbon atoms of the structure.
According to particular embodiments, R 2 to R 8 have the same meanings as defined herein above.
According to a particular embodiment, the compound of formula (Ila) is of formula (I la,i) in the form of any of its stereoisomers or a mixture thereof, wherein
X is a thiol group, alcohol group or primary amine group, and R 2 a hydrogen atom or a C1-4 alkyl group; and the compound of formula (la) is of formula (I a, i)
in the form of any of its stereoisomers or a mixture thereof, wherein
Y is a sulfur atom, an oxygen atom or a NH group, and each R 2 , R 3 , R 4 represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group.
According to a particular embodiment, the present invention is directed to a process, wherein the compound of formula (II) is of formula (lib) in the form of any of its stereoisomers or a mixture thereof, wherein n is 0 or 1 ;
X is a thiol group, alcohol group or primary amine group, and one dotted line is a carbon-carbon single or double bond and the other is a carbon-carbon single bond; and each R2, Rs and Re represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group; and the compound of formula (I) is of formula (lb)
in the form of any of its stereoisomers or a mixture thereof, wherein
Y is a sulfur atom, an oxygen atom or a NH group, and the dotted line, n, R2, Rs and Re have the same meaning as defined above; and each R3 and R4 represent, when taken separately, independently from each other, a hydrogen atom or a C14 alkyl group.
According to particular embodiments, n is 1.
According to particular embodiments, R 2 to R 6 have the same meanings as defined herein above.
According to a particular embodiment, the present invention is directed to a process, wherein the compound of formula (II) is of formula (He) in the form of any of its stereoisomers or a mixture thereof, wherein
X is a thiol group, alcohol group or primary amine group, and R 2 a hydrogen atom or a C1-4 alkyl group; and the compound of formula (I) is of formula (Ic) in the form of any of its stereoisomers or a mixture thereof, wherein
Y is a sulfur atom, an oxygen atom or a NH group, and each R 2 , R 3 , R 4 represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group.
According to particular embodiments, R 2 to R 4 have the same meanings as defined herein above.
According to a more particular embodiment, the compound of formula (I) is of formula (Id) in the form of any of its stereoisomers or a mixture thereof; and the compound of formula (II) is of formula (lid) in the form of any of its stereoisomers or a mixture thereof, and the epoxide of formula (III) is of formula (Hid) Heterogeneous acidic catalyst
According to any embodiment of the present invention, the heterogeneous acidic catalyst may be amorphous or crystalline, particularly crystalline.
According to any embodiment of the present invention, the heterogeneous acidic catalyst may comprise at least one metal selected from the group consisting of silicon, tin, zirconium, hafnium or titanium or a mixture thereof and optionally at least one metal selected from the group consisting of aluminum, boron, iron or a mixture thereof. Preferably, the heterogeneous acidic catalyst comprises at least one metal selected from the group consisting of silicon or tin or a mixture thereof and optionally at least one metal selected from the group consisting of aluminum, boron, iron or a mixture thereof.
According to any embodiment of the present invention, the heterogeneous acidic catalyst may be a Lewis acid supported on a solid support.
A person skilled in the art is able to select suitable Lewis acids. Suitable Lewis acids may be HCIO4, BF3, AICI3, FeCh. CuCh, ZnCh, ZnBr2, ZrCL, TiCL orTiCl4-x(OR) x , wherein R represents a C1-12 alkyl or alkenyl group. Other suitable Lewis acids may be metal trifluoromethanesulfonates, wherein the metal may be a metal selected from the series of lanthanides, preferably lanthanum. Other suitable Lewis acids may be heteropolyacids (also called heteropolymetalates). A person skilled in the art is able to select suitable heteropolyacids based on his general knowledge in the field. Preferred heteropolyacids are silicotungstic acid (H4SiWi204o nH20), phosphomolybdic acid (H3Moi2P04o nH20) or phosphotungstic acid (H3Wi2P04o nH20).
According to an embodiment, the supported Lewis acid can be a mixture of two or more Lewis acids.
The solid support is understood to remain solid under the chosen reaction conditions. According to a particular embodiment, the solid support may be an organic or inorganic polymer. According to a particular embodiment, the solid support may be an inorganic support material. According to a particular embodiment, the inorganic support material may be a metal oxide. According to a particular embodiment, the inorganic support material may comprise a metal selected from the group consisting of silicon, tin, aluminum, zirconium, titanium, iron, boron or a mixture thereof, preferably silicon. According to a particular embodiment, the inorganic support material may be silicon dioxide. According to a particular embodiment, the supported Lewis acid is BFs/SiCh or HCICL/SiCh.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is an aluminosilicate catalyst.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a zeolite or a clay.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a clay.
The clay may be a commercially available clay. According to any embodiment of the present invention, the commercially available clay may contain water. Said water may be removed partly or totally before use. The person skilled in the art is well-aware of methods to remove water such as, for example, azeotropic distillation, vacuum striping or heating under nitrogen flow.
According to any embodiment of the present invention, the clay may be naturally occurring. According to any embodiment of the present invention, the heterogeneous acidic catalyst is an acid treated clay. An acidic treated clay is herein understood to be a clay that is subjected to an acidic treatment prior to its use as heterogeneous acidic catalyst according to the methods described in the patents US2470872A, US2671058A, US2981697A or US1926148A. A person skilled is able to select the most appropriate conditions for the acid treatment of the clay based on his general knowledge in the field and on the teaching of these patent applications.
Non-limiting examples of suitable clays may include type K clays such as K-5, K10-S300, K- 20, K-30, K-41 or K-306 (presently sold by Clariant), former Filtrol type clays such as F-20X, F20-XLM, F-21X, F-24X, F-25X, F-31X, F-54X, F-22, or F-118FF (presently sold by EP Minerals), Fulcat-22F, Fulcat-22B or Fulcat 435 (presently sold by Byk), EXBC 0001 (presently sold by Clariant). In an embodiment, the clay is K10-S300.
According to a preferred embodiment of the present invention, the heterogeneous acidic catalyst is a zeolite.
According to any embodiment of the present invention, the zeolite is used in its protonic form. The latter can be directly provided by the manufacturer and used as such or obtained by thermal decomposition of the ammonium-exchange form. In a particular embodiment, the zeolite is a preactivated zeolite. The preactivation may be carry out by removing trapped water as described earlier in the case of clays or by heating the zeolite at a temperature comprised between 300°C and 600°C for at least 1 hour under air or an inert gas.
The heterogeneous acidic catalyst is commercially available compound or can be prepared by several methods, such as the one reported in US20040141911 , US6054113, US4840930, US2470872 and EP0398636.
Non-limiting examples of suitable zeolites may include CBV780, CBV901 presently sold by Zeolyst or HSZ-385HUA or HSZ-390HUA presently sold by Tosoh.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a large pore zeolite.
By “the term large pore zeolite” it is meant the normal meaning in the art; i.e. a 12 membered ring zeolite having a pore size comprised in the range between 6.0 Angstrom and 7.5 Angstrom. Non-limiting examples of suitable large pore zeolite may include FAU, BEA, MOR.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a zeolite having a FAU topology.
The term FAU topology is understood to have the meaning conventionally used in the field of zeolites and are well-known to a person skilled in the art. The framework topology is usually defined by a three letters code following the rules set up by an IUPAC Commission on Zeolite Nomenclature in 1978 (R.M. Barrer, Pure Appl. Chem. 51 , 1091 (1979)).
A zeolite having a FAU topology is understood as zeolite with a faujasite crystal structure. A person skilled in the art is aware of the definition of the faujasite crystal structure, which is e.g. described in Rdmpp Chemie Lexikon, Georg Thieme Verlag, 9. Edition, 1990, page 1311
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a Y-type zeolite.
The term Y-type zeolite is understood to have the meaning conventionally used in the field of zeolites and is well-known to a person skilled in the art. A Y-type zeolite is understood to be a zeolite having a FAU topology. A Y-type zeolite is typically characterized by spherical, internal cavities (so called “supercages”) linked tetrahedrally through pore openings of about 8 Angstrom and comprising rings of twelve oxygen atoms.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a dealuminated zeolite. Dealumination is conventionally understood as removal of aluminum atoms from a zeolite structure. Dealumination leads to an increase of the Silicon : Aluminum ratio of a zeolite. Nonlimiting examples for suitable methods for dealumination known in the art are hydrothermal treatment, acidic treatment, treatment with gaseous halides or halogens or complexation with chelating agents. A person skilled in the art is aware of these methods and of ways to perform them.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a dealuminated ultrastable Y-type (USY) zeolite.
USY zeolites are typically prepared from Y-type zeolites to increase their stability and improve their catalytic activity by removing intra-framework aluminum with a combination of treatments comprising ion-exchange, steaming, acid leaching and calcination. Such treatments are for example described in the patents US5601798A and US4477336A and are well-known to a person skilled in the art.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a hydrophobic zeolite.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is a hydrophobic dealuminated USY zeolite.
Hydrophobicity of zeolites is conventionally defined by the hydrophobicity index (HI). The hydrophobicity index is defined as the amount (usually in grams) of cyclohexane adsorbed per weight (usually in grams) of water adsorbed on a unit amount of zeolite at vapor pressures of cyclohexane and water of 933 Pa (7 Torr) and 666 Pa (5 Torr), respectively, according to I. Halasz et al., Molecular Physics, 2002, 100, 3232-3232.
According to any embodiment of the present invention, the hydrophobicity index is between 5- 100, preferably between 10 and 75 and more preferably between 20 and 50.
According to any embodiment of the present invention, the Silicon : Aluminum ratio is in the range between 5 : 1 and 350 : 1 .
According to a preferred embodiment, the Silicon : Aluminum ratio is in the range between 10 : 1 and 325 : 1.
According to a preferred embodiment, the Silicon : Aluminum ratio is in the range between 15 : 1 and 300 : 1.
According to a preferred embodiment, the Silicon : Aluminum ratio is in the range between 22 : 1 and 275 : 1. According to a preferred embodiment, the Silicon : Aluminum ratio is in the range between 30 : 1 and 250 : 1.
According to a preferred embodiment, the Silicon : Aluminum ratio is in the range between 40 : 1 and 250 : 1.
According to a preferred embodiment, the Silicon : Aluminum ratio is in the range between 50 : 1 and 250 : 1.
In a particular embodiment, the heterogeneous acidic catalyst is selected from the group consisting of clay, zeolite, and supported Lewis acid. The clay, zeolite, and supported Lewis acid, respectively, can be as defined above.
The heterogeneous acidic catalyst can be added into the reaction medium of the invention’s process to form the compound of formula (I) in a large range of concentrations.
According to any embodiment of the present invention, the heterogeneous acidic catalyst is used in an amount of 2 to 50 wt.%, preferably 3 to 30 wt.%, more preferably 4 to 15 wt.%, even more preferably 5 to 10 wt.%, relative to the amount of epoxide of formula (III).
According to any embodiment of the present invention, the compound of formula (II) or (Ila) is used in an amount of 1.0 to 10 equivalents, preferably in an amount of 1.4 to 7 equivalents, more preferably in an amount of 1.8 to 4.2 equivalents, relative to the amount of epoxide of formula (III).
According to any embodiment of the present invention, the process temperature is kept in a range between 0 to 50 °C, preferably between 25 and 48°C, more preferably between 43 and 47°C. A person skilled in the art is able to select the preferred temperature as a function of the melting and boiling point of the starting and final products as well as the desired time of reaction, conversion or selectivity.
The invention’s process for the preparation of a compound of formula (I) can be carried out in the presence or absence of a solvent. When a solvent is required or used for practical reasons, then any solvent current in such reaction type can be used for the purposes of the invention. Non-limiting examples include C6-12 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 solvent such as acetonitrile, or ethereal solvents such as tetrahydrofuran, diethyether, methyl tetrahydrofuran or mixtures thereof. The choice of the solvent is function of the nature of the substrate and/or catalyst and the person skilled in the art is well able to select the solvent most suitable in each case to optimize the reaction.
The invention’s process for the preparation of a compound of formula (I) may be carried out under batch and/or continuous conditions.
A process according to any embodiment of the present invention can be used for the preparation of a compound of formula (IV) in the form of any of its stereoisomers or a mixture thereof; wherein
Y is a sulfur atom, an oxygen atom or a NH group, and
Ri represents a C1-12 alkyl, C2-12 alkenyl, a C5-12 cycloalkyl or C5-12 cycloalkenyl group, each optionally substituted by 1 to 3 CM alkyl groups; and each R2, R3, R4 represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group; and
R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably a C1- 4 alkyl group, a C2-4 alkenyl group, a C3-6 cycloalkyl group; preferably a C1-3 alkyl group, a C2-3 alkenyl group, a C3-5 cycloalkyl group; preferably an ethyl group, a vinyl group, a cyclopropyl or a cyclopentyl group, more preferably an ethyl group; by reacting the compound of formula (I) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group.
According to any embodiment of the present invention, the compound of formula (IV) is of formula (IVa) in the form of any of its stereoisomers or a mixture thereof; wherein one dotted line is a carbon-carbon single or double bond and the other is a carbon-carbon single bond; and
Y is a sulfur atom, an oxygen atom or a NH group, and each R2, R3, R4, Rs, Re and R? represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group; and
Rs represents a C14 alkyl group; or
R? and Rs are linked to each other and form a C5-7 cycloalkyl or cycloalkenyl group; and
R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably a C1- 4 alkyl group, a C2-4 alkenyl group, a C3-6 cycloalkyl group; preferably a C1-3 alkyl group, a C2-3 alkenyl group, a C3-5 cycloalkyl group; preferably an ethyl group, a vinyl group, a cyclopropyl or a cyclopentyl group, more preferably an ethyl group; and the compound of formula (IVa) is formed by reacting the compound of formula (la) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group.
According to any embodiment of the present invention, the compound of formula (IV) is of formula in the form of any of its stereoisomers or a mixture thereof; wherein one dotted line is a carbon-carbon single or double bond and the other is a carbon-carbon single bond; and
Y is a sulfur atom, an oxygen atom or a NH group, and each R2, R3 and R4 represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group; and
R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably a C1- 4 alkyl group, a C2-4 alkenyl group, a C3-6 cycloalkyl group; preferably a C1-3 alkyl group, a C2-3 alkenyl group, a C3-5 cycloalkyl group; preferably an ethyl group, a vinyl group, a cyclopropyl or a cyclopentyl group, more preferably an ethyl group; and the compound of formula (IVa) is formed by reacting the compound of formula (la) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group. According to any embodiment of the present invention, the compound of formula (IV) is of formula (IVb) in the form of any of its stereoisomers or a mixture thereof; wherein n is 0 or 1 ; and one dotted line is a carbon-carbon single or double bond and the other is a carbon-carbon single bond; and
Y is a sulfur atom, an oxygen atom or a NH group, and each R2, R3, R4, Rs and Re represent, when taken separately, independently from each other, a hydrogen atom or a CM alkyl group; and
R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably a C1- 4 alkyl group, a C2-4 alkenyl group, a C3-6 cycloalkyl group; preferably a C1-3 alkyl group, a C2-3 alkenyl group, a C3-5 cycloalkyl group; preferably an ethyl group, a vinyl group, a cyclopropyl or a cyclopentyl group, more preferably an ethyl group; and the compound of formula (IVb) is formed by reacting the compound of formula (lb) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group.
According to any embodiment of the present invention, the compound of formula (IV) is of formula (IVc) in the form of any of its stereoisomers or a mixture thereof; wherein
Y is a sulfur atom, an oxygen atom or a NH group, and each R2, R3 and R4 represent, when taken separately, independently from each other, a hydrogen atom or a C1-4 alkyl group; and
R10 represents a C1-6 alkyl group, a C2-6 alkenyl group, a C3-6 cycloalkyl group; preferably an ethyl group, an ethylene group, a cyclopropane or a cyclopentane group, more preferably an ethyl group; and the compound of formula (IVc) is formed by reacting the compound of formula (Ic) with a compound of formula Z-C(O)-R , wherein Z is a R -C(0)-0 group, thiol group, chlorine atom, alcohol group or amine group.
According to a particular embodiment, R 1 represents a C5-8 cycloalkyl optionally substituted by 1 to 2 C1-3 alkyl groups, even more 1 to 2 C1-2 alkyl groups, more preferably a Ce cycloalkyl substituted by 2 methyl groups.
According to a particular embodiment, R 2 represents a methyl or ethyl group, more preferably a methyl group.
According to a particular embodiment, R 3 represents a methyl or ethyl group, more preferably a methyl group.
According to a particular embodiment, R 4 represents a methyl or ethyl group, more preferably a methyl group.
According to a more particular embodiment, each R 3 and R 4 represent a methyl group.
According to a particular embodiment, R 5 represents a methyl or ethyl group, more preferably a methyl group.
According to a particular embodiment, R 6 represents a methyl or ethyl group, more preferably a methyl group.
According to a more particular embodiment, each R 5 and R 6 represent a methyl group.
According to a particular embodiment, R 7 represents a hydrogen atom.
According to a particular embodiment, R 8 represents a methyl or ethyl group, more preferably a methyl group.
According to any embodiment of the present invention, the compound of formula (IV) is of formula (IVd) in the form of any of its stereoisomers or a mixture thereof. Typical manners to execute the invention’s process are reported herein below in the examples, which should not be considered as limiting the invention. In the examples, unless otherwise specified, the abbreviations have the usual meaning in the art, the temperatures are indicated in degrees centigrade (°C) and percentages are indicated in weight percent (wt.%).
Examples
Example 1 : General catalyst screening procedure
In a 0.5L double jacketed glass reactor equipped with a mechanical stirrer, 130 g (0.832 mol) of (R)-1-((S)-3,3-dimethylcyclohexyl)ethan-1-ol (herein called Cyclademol™, origin DRT) were vigorously stirred at 45°C in the presence of 2.08 g of catalyst (10 wt.% vs isobutylene oxide (I BO)). To this solution, 20.8 g (0.288 mol) of isobutylene oxide (I BO, origin BASF) were slowly added in two hours and the reaction left further under stirring for another two hours. After filtration of the catalyst, the yield of (S)-2-((3,3-dimethylcyclohexyl)methoxy)-2-methylpropan- 1-ol vs IBO in the crude sample was evaluated by gas chromatography using n-decane as internal standard.
Example 2: Zeolite catalysts
Several zeolites as listed in table 1 were used as catalyst in the procedure of Example 1 . The results of this screening are shown in table 1. Each zeolite in Table 1 was calcined prior to use.
Table 1 : Freshly calcined zeolites
Example 3: As-received USY zeolites with lower catalyst loading
In a 1 L double jacketed glass reactor equipped with a mechanical stirrer, 400 g (2.56 mol) of (R)-1-((S)-3,3-dimethylcyclohexyl)ethan-1-ol (herein called Cyclademol™, origin DRT) were vigorously stirred at 45°C in the presence of 3.2 g of as-received catalyst (5 wt.% vs isobutylene oxide (IBO)). To this solution, 64 g (0.887 mol) of isobutylene oxide (IBO, origin BASF) were slowly added in two hours and the reaction left further under stirring for another two hours. After filtration of the catalyst, the yield of (S)-2-((3,3-dimethylcyclohexyl)methoxy)- 2-methylpropan-1-ol vs. IBO in the crude sample was evaluated by gas chromatography using n-decane as internal standard.
Table 2: As-received USY zeolites
Example 4: Comparative homogeneous catalyst
In a 0.5L double jacketed glass reactor equipped with a mechanical stirrer, 130 g (0.832 mol) of (R)-1-((S)-3,3-dimethylcyclohexyl)ethan-1-ol (herein called Cyclademol™, origin DRT) were vigorously stirred at 30°C in the presence of 16.8 mmol of a homogenous catalyst as defined in Table 3 below. To this solution, 20.8 g (0.288 mol) of isobutylene oxide (IBO, origin BASF) were slowly added in two hours and the reaction left further under stirring for another hour. After quenching of the solution with aqueous sodium citrate, the yield of (S)-2-((3,3- dimethylcyclohexyl)methoxy)-2-methylpropan-1-ol vs. IBO in the crude sample was evaluated by gas chromatography using n-decane as internal standard.
Table 3: Homogenous catalysts
Example 5: Preparation of 2-((3,5-dimethylhex-3-en-2-yl)oxy)-2-methylpropan-1-ol 14 g (0.109 mol) of 3,5-dimethylhex-3-en-2-ol (prepared according to the procedure described in W02004/050595 A1 - example 1) were vigorously stirred at 45 °C in the presence of 0.274 g of HSZ-390 HUA (Tosoh). To this solution, 2.74 g (0.038 mol) of isobutylene oxide (IBO, origin BASF) were slowly added in two hours and the reaction left further under stirring for another hour. After filtration of the solid catalyst, the yield of 2-((3,5-dimethylhex-3-en-2- yl)oxy)-2-methylpropan-1-ol vs. IBO in the crude sample was evaluated by gas chromatography using n-decane as internal standard and reached 42.3 mol.%.
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