Patent Application
20240327341
The present disclosure is directed to novel polythiol compounds which may be derived from bio-renewable resources. In particular, the present disclosure is directed to polythiol compounds which may be derived from phenols, polyphenols or phenolic acids which may be sourced bio-renewably.
The chemical industry is currently reliant on a historically inexpensive, petroleum-based carbon feedstock that generates a small collection of platform chemicals from which highly efficient chemical conversions lead to the manufacture of a large variety of chemical products. The current approach to producing these carbon-based chemicals is, however, inherently non-sustainable as we consume feedstock that required millions of years to form. The creation of a sustainable chemical industry will only occur when the timescale of feedstock formation equates to the timescale of its utilization to make chemicals.
Given the intrinsic need for carbon in chemical products, biomass-with its short formation time—must ultimately become the feedstock for the chemical industry. Biomass does represent an inexpensive feedstock but, if the chemical industry is to move to a biomass feedstock without a significant cost disruption, an efficient production paradigm will need to be developed that allows inexpensive and efficient processing of biomass.
Thiol-ene and thiol-epoxy polymers are attractive materials for coatings, adhesives and sealants due to their ease of fabrication and low shrinkage and stress. Moreover, the use of so-called “click reactions” in the synthesis of these materials provides an ecologically-friendly technology on account of the limited amount of waste originated, the low energy consumption, the completeness of the reaction process and the high yield without the formation of by-products that leads to the formation of homogenous three-dimensional network structures. In addition, such click reactions can be performed in the absence of solvent and in an air atmosphere—on account of the limited water and oxygen sensitivity of the reactants-which is of benefit to a number of technological applications.
Problematically, however, thiol-containing, ene-containing and epoxide compounds are traditionally derived from petrochemical sources. As such, certain authors have tried to derivatize compounds occurring naturally in biomass to enable their use in inter alia click reactions.
US2019/211139 (Robertson et al) discloses a resin comprising: (A) a naturally occurring aromatic compound wherein the aromatic compound has been modified to contain at least one epoxidized hydroxy group and at least one epoxidized carboxylic acid group; and (B) a curing agent selected from an anhydride, an acid, an alcohol, a thiol, a phenol, or an amine; provided that the aromatic compound is not an epoxidized version of gallic acid.
US2008/0021209A1A (East et al.) discloses a method for the synthesis of bisglycidyl ethers of anhydrosugars derived from renewable sources, including isosorbide, isomannide and isoidide. The bisglycidyl ethers are mooted to be useful substitutes for bisphenol A diglycidyl ethers.
WO2010/136725A1 (Centre National de la Recherche Scientifique (C.N.R.S.) et al.) describes a process for preparing epoxy resins from a mixture of epoxidized phenolic compounds, wherein said epoxidized phenolic compounds are obtained by epoxidation of natural phenolic compounds selected from the group consisting of simple phenol, phenol acid, coumarin, naphthoquinone, stilbenoid, flavonoid, isoflavonoid, anthocyanin, condensed tannin and hydrolysable tannin.
U.S. Pat. No. 8,513,374 B2 (Dasgupta) describes-ene compounds which are derivatives of a plant polyphenol and which are selected from the group consisting of curcumin diallyl carbonate, tetrahydrocurcumin diallyl carbonate, resveratrol triallyl carbonate, mono-O-allyl curcumin, tetra-allyl curcumin, di-allyl tetrahydrocurcumin, tetra-allyl tetrahydrocurcumin and tri-O-allyl resveratrol. The utility of these allyl functionalized compounds as monomers in formation of polymers via thiol-ene chemistry is disclosed.
These citations do not teach or suggest thiol functional compounds which may be derived from bio-renewable compounds. There is therefore considered to be a need in the art to provide such thiol functional compounds.
In accordance with a first aspect of the invention, there is provided a polythiol compound having the general Formula VIA, VIB or VIC:
As regards said general formulae, it is preferred that R1 is an unsubstituted C1-C12 alkylene group, more preferably an unsubstituted C1-C4 alkylene group; and, R2 is H or methyl.
Representative and important polythiols in accordance with these general formulae are selected from VIAa, VIBa or VICa:
In accordance with a further aspect of the invention, there is provided a process for preparing a compound having the general Formula VIA, VIB, VIC or VID:
X—(R1)—C(R2)═CH2 (II)
R3—C(50 O)—SH (IV)
The compounds of Formula IA, IB, IC and ID can be provided directly or be derived from phenols, phenolic acids and polyphenols which may be sourced bio-renewably.
In this aspect of the disclosure, it is preferred that said primary allyl compound (II) is characterized in that: R° is C1-C2 alkyl; R1 is an unsubstituted C1-C12 alkylene group, preferably an unsubstituted C1-C4 alkylene group; and, R2 is H or Me. In important embodiments, said primary allyl compound (II) is selected from the group consisting of: 3-chloro-1-propene, 3-bromoprop-1-ene; 3-iodoprop-1-ene; methyl prop-2-enyl carbonate; and, ethyl prop-2-enyl carbonate.
As regards step b) above, it is preferred that said reactant thiol acid (IV) is characterized in that: R3 is C1-C4 alkyl, C6 aryl, C7-C18 alkylaryl or C7-C18 aralkyl. A particular preference may be noted for said thiol acid (IV) being selected from the group consisting of thioacetic acid, thiopropionic acid, thiobutyric acid, thioisobutyric acid, thiobenzoic acid, 2-methyl-thiobenzoic acid, 3-methyl-thiobenzoic acid, 4-methyl-thiobenzoic acid, 2,4-dimethyl-thiobenzoic acid and 3,5-dimethyl-thiobenzoic acid. And good results have been obtained where either thioacetic or thiobenzoic acid is used as the reactant thiol acid (IV).
In accordance with an alternative aspect of the invention, there is provided a process for preparing a compound having the general Formula VIB, VIC or VID
As regards said thiolate ester compound of Formula VII, it is preferred that: R1 is an unsubstituted C1-C12 alkylene group; R2 is H or Me; and, R3 is C1-C4 alkyl, C6 aryl, C7-C18 alkylaryl or C7-C18 aralkyl. In important embodiments: R1 is an unsubstituted C1-C4 alkylene group; R2 is H or Me; and, R3 is a C1-C4 alkyl.
The deprotection step of the alternative processes above (c), β)) may be performed reductively but is preferably performed by acid-catalysed or base-catalysed hydrolysis.
In accordance with a still further aspect of the disclosure there is provided the use of a polythiol compound having the general formula VIA, VIB or VIC as defined herein above and in the appended claims as a reactive component of an one (1K) or two (2K) component curable composition.
The disclosure also provides a curable composition comprising:
Component a) of the curable composition may comprise, in particular, at least one polythiol compound having the general Formula VIA, VIB or VIC.
In accordance with a yet still further aspect of the present disclosure, there is provided a compound of general Formula IIIC:
It is preferred in said Formula IIIC that: R1 is an unsubstituted C1-C12 alkylene group, preferably a C1-C4 alkylene group; and, R2 is H or Me. In an exemplary compound, R1 is methylene and R2 is H. The compound of Formula IIIC is considered to be an important and novel intermediate formed in the first process defined herein above.
In accordance with a final aspect of the present invention, there is provided a compound of general formula VID:
As regards said general formula and subject to said proviso, it is preferred that R1 is an unsubstituted C1-C12 alkylene group, more preferably an unsubstituted C1-C4 alkylene group; and, R2 is H or methyl.
It will be recognized that, when compounds IA, IB, IC and ID are sourced biorenewably, the resultant compounds will have a significant biocarbon content, wherein biocarbon content (%) is defined as: 100*(No. of Carbon Atoms of Biobased Starting Material (I)/No. of Carbon Atoms of Synthesized Polythiol). The following attainable biocarbon contents may be noted: Compound VIAa, 77%: Compound VIBa, 37%; and, Compound VICa, 71%.
As used herein, the singular forms “a”, “an” and “the” include plural referents unless the context clearly dictates otherwise.
The terms “comprising, “comprises” and “comprised of” as used herein are synonymous with “including”, “includes”, “containing” or “contains”, and are inclusive or open-ended and do not exclude additional, non-recited members, elements or method steps.
As used herein, the term “consisting of” excludes any element, ingredient, member or method step not specified. For completeness, the term “comprising” encompasses “consisting of”.
When amounts, concentrations, dimensions and other parameters are expressed in the form of a range, a preferable range, an upper limit value, a lower limit value or preferable upper and limit values, it should be understood that any ranges obtainable by combining any upper limit or preferable value with any lower limit or preferable value are also specifically disclosed, irrespective of whether the obtained ranges are clearly mentioned in the context.
Further, in accordance with standard understanding, a weight range represented as being “from 0” specifically includes 0 wt. %: the ingredient defined by said range may or may not be present in the composition.
The terms “preferred”, “preferably”, “desirably”, “in particular” and “particularly” are used frequently herein to refer to embodiments of the disclosure that may afford particular benefits, under certain circumstances. However, the recitation of one or more preferable, preferred, desirable or particular embodiments does not imply that other embodiments are not useful and is not intended to exclude those other embodiments from the scope of the disclosure.
As used throughout this application, the word “may” is used in a permissive sense—that is meaning to have the potential to—rather than in the mandatory sense.
As used herein, room temperature (RT) is 23° C. plus or minus 2° C. As used herein, “ambient conditions” means the temperature and pressure of the surroundings in which the composition is located or in which an adhesive, sealant, coating or composite structure obtained from said composition is located.
The molecular weights referred to in this specification—to describe to macromolecular, oligomeric and polymeric components of the curable compositions—can be measured with gel permeation chromatography (GPC) using polystyrene calibration standards, such as is done according to ASTM 3536.
The term “molar equivalents” is used in accordance with its standard meaning: it thus refers to the number of moles of specified compound or functional group A in relation to the number of moles of specified compound or functional group B.
As used herein, the term “equivalent (eq.”) relates, as is usual in chemical notation, to the relative number of reactive groups present in the reaction.
The term “equivalent weight” as used herein refers to the molecular weight divided by the number of a function concerned. As such, “epoxide equivalent weight” (EEW) means the weight of resin, in grams, that contains one equivalent of epoxide.
As used herein, the term “water” is intended to encompass tap water, spring water, purified water, de-ionized water, de-mineralized and distilled water.
As used herein “basicity” means the quality of being a base, not an acid. More particularly, in accordance with the Lewis theory of acids and bases, a base is an electron-pair donor. This definition encompasses but is not limited to Brønsted-Lowry bases, which compounds act as proton acceptors.
As used herein, the term “one component (1K) composition” refers to a composition where, during storage of the composition, the composition components are all admixed together but the properties of the composition, including viscosity, remain consistent enough over the time of storage to permit successful utility of the composition at a later time.
“Two-component (2K) compositions” are understood to be compositions in which a first component (A) and a second component (B) must be stored in separate vessels because of their (high) reactivity. The two components are mixed only shortly before application and then react, typically without additional activation, with bond formation and thereby formation of a polymeric network. Herein higher temperatures may be applied in order to accelerate the cross-linking reaction.
Certain embodiments of the present disclosure describe dual cure compositions. As used herein, the term “dual cure composition” refers to a composition that will cure upon exposure to two different cure conditions. For example, the dual cure compositions may cure upon exposure to a combination of thermal energy and radiation. Thermal energy is intended to encompass: radiant energy, such as infrared or microwave energy; and, conductive thermal energy, such as that produced by a heated plate or an oven. As used herein, the term “radiation” encompasses: ionizing radiation, such as an electrons beam; and, actinic radiation.
As used herein, the term “free radical initiator” refers to any chemical species which, upon exposure to sufficient energy—in the form of light or heat, for example—decomposes into two parts which are uncharged, but which each possess at least one unpaired electron. Thus a thermal free radical initiator generates free upon exposure to heat. And known thermal free radical initiators include, but are not limited to, peroxide compounds, azo compounds and persulfate compounds.
The term “photoinitiator” as used herein denotes a compound which can be activated by an energy-carrying activation beam—such as electromagnetic radiation—upon irradiation therewith. Specifically, a “free-radical photoinitiator” herein refers to a photoactive compound that generates free radicals, which radicals could herein initiate polymerization or reaction by addition to C═C double bonds present in the compositions.
The term “aprotic solvents” as used herein refers to solvents that do not yield or accept a proton. Conversely “protic solvents” are those solvents capable of yielding or accepting a proton. The “polar solvent” as used herein refers to a solvent having a dielectric constant (ε) of more than 5 as measured at 25° C.: the term encompasses both aprotic and protic solvents. The determination of dielectric constant (ε) is well known in the art and is within the knowledge of the skilled person: the use of measured voltages across parallel plate capacitors in such determinations may be mentioned.
As used herein, the term “epoxide” denotes a compound characterized by the presence of at least one cyclic ether group, namely one wherein an ether oxygen atom is attached to two adjacent carbon atoms thereby forming a cyclic structure. The term is intended to encompass monoepoxide compounds, polyepoxide compounds (having two or more epoxide groups) and epoxide terminated prepolymers. The term “monoepoxide compound” is meant to denote epoxide compounds having one epoxy group. The term “polyepoxide compound” is meant to denote epoxide compounds having at least two epoxy groups. The term “diepoxide compound” is meant to denote epoxide compounds having two epoxy groups.
The epoxide may be unsubstituted but may also be inertly substituted. Exemplary inert substituents include chlorine, bromine, fluorine and phenyl.
As used herein, “(meth)acryl” is a shorthand term referring to “acryl” and/or “methacryl”. Thus the term “(meth)acrylate” refers collectively to acrylate and methacrylate. Likewise, “allyl” and “methallyl” are designated herein in a summarizing manner as “(meth)allyl”.
As used herein, “C1-Cn alkyl” group refers to a monovalent group that contains 1 to n carbons atoms, that is a radical of an alkane and includes straight-chain and branched organic groups. As such, a “C1-C18 alkyl” group refers to a monovalent group that contains from 1 to 18 carbons atoms, that is a radical of an alkane and includes straight-chain and branched organic groups. Examples of alkyl groups include, but are not limited to: methyl; ethyl; propyl; isopropyl; n-butyl; isobutyl; sec-butyl; tert-butyl; n-pentyl; n-hexyl; n-heptyl; and, 2-ethylhexyl. In the present invention, such alkyl groups may be unsubstituted or may be substituted with one or more halogen. Where applicable for a given moiety (R), a tolerance for one or more non-halogen substituents within an alkyl group will be noted in the specification.
The term “C1-Cn hydroxyalkyl” as used herein refers to a HO-(alkyl) group having from 1 to n carbon atoms, where the point of attachment of the substituent is through the oxygen-atom and the alkyl group is as defined above.
An “alkoxy group” refers to a monovalent group represented by —OA where A is an alkyl group: non-limiting examples thereof are a methoxy group, an ethoxy group and an iso-propyloxy group. The term “C1-C12 alkoxyalky” as used herein refers to an alkyl group having an alkoxy substituent as defined above and wherein the moiety (alkyl-O-alkyl) comprises in total from 1 to 12 carbon atoms: such groups include methoxymethyl (—CH2OCH3), 2-methoxyethyl (—CH2CH2OCH3) and 2-ethoxyethyl.
As used herein, the term “C1-C8 alkanol” refers to compounds of the general formula ROH, where R is an alkyl group having from 1 to 8 carbon atoms as defined above. In the described method steps, a preference for a C1-C4 alkanol and more particularly for methanol or ethanol should be noted.
The term “C1-Cn alkylene” as used herein, is defined as saturated, divalent hydrocarbon radical having from 1 to n carbon atoms. In general in the present disclosure, such alkylene groups may be unsubstituted or may be substituted with one or more halogen or one or more hydroxyl. Where applicable for a given moiety (R), a tolerance for one or more non-halogen substituents within an alkylene group will be noted in the specification.
By the term “C2-C18 oxyalkylene group” is meant two or more alkylene groups linked by one or more oxygen atoms in ether linkage, said group having in total from 2 to 19 carbon exams. Examples thereof include mono-ether groups being represented by -alkylene-O-alkylene- and di-ether groups being represented by -alkylene-O-alkylene-O-alkylene-, wherein the term alkylene has the meaning assigned above.
By the term “C2-C18 thioalkylene group” is meant two or more alkylene groups linked by one or more sulphur atoms in thioether linkage, said group having in total from 2 to 19 carbon exams. Examples thereof include mono-thioether groups being represented by -alkylene-S-alkylene- and di-ether groups being represented by -alkylene-S-alkylene-S-alkylene-, wherein the term alkylene has the meaning assigned above.
The term “C3-C30 cycloalkyl” is understood to mean a saturated, mono-or polycyclic hydrocarbon group having from 3 to 30 carbon atoms. In the present invention, such cycloalkyl groups may be unsubstituted or may be substituted with one or more halogen. Where applicable for a given moiety (R), a tolerance for one or more non-halogen substituents within a cycloalkyl group will be noted in the specification. Examples of cycloalkyl groups include: cyclopropyl; cyclobutyl; cyclopentyl; cyclohexyl; cycloheptyl; cyclooctyl; adamantane; and norbornane.
The term “C3-C30 hydroxycycloalky” as used herein refers to a HO-(cycloalkyl) group having from 3 to 30 carbon atoms, where the point of attachment of the substituent is through the oxygen-atom and the cycloalkyl group is as defined above.
As used herein, an “C6-C18 aryl” group used alone or as part of a larger moiety—as in “aralkyl group”—refers to monocyclic, bicyclic and tricyclic ring systems in which the monocyclic ring system is aromatic or at least one of the rings in a bicyclic or tricyclic ring system is aromatic. The bicyclic and tricyclic ring systems include benzofused 2-3 membered carbocyclic rings. In the present invention, such aryl groups may be unsubstituted or may be substituted with one or more halogen. Where applicable for a given moiety (R), a tolerance for one or more non-halogen substituents within an aryl group will be noted in the specification. Exemplary aryl groups include: phenyl; indenyl; naphthalenyl, tetrahydronaphthyl, tetrahydroindenyl; tetrahydroanthracenyl; and, anthracenyl. And a preference for phenyl groups may be noted.
The term “C6-C18 arylene” denotes a divalent hydrocarbon radical having from 6 to 18 carbon atoms which is derived from an aryl group as defined above. An exemplary arylene group is phenylene (—C6H4—).
As used herein, “C2-C20 alkenyl” refers to hydrocarbyl groups having from 2 to 20 carbon atoms and at least one unit of ethylenic unsaturation. The alkenyl group can be straight chained, branched or cyclic and may optionally be substituted with one or more halogen. Where applicable for a given moiety (R), a tolerance for one or more non-halogen substituents within an alkenyl group will be noted in the specification. The term “alkenyl” also encompasses radicals having “cis” and “trans” configurations, or alternatively, “E” and “Z” configurations, as appreciated by those of ordinary skill in the art. Examples of said C2-C20 alkenyl groups include, but are not limited to: —CH═CH2; —CH═CHCH3; —CH2CH═CH2; —C(═CH2)(CH3); —CH═CHCH2CH3; —CH2CH═CHCH3; —CH2CH2CH═CH2; —CH═C(CH3)2; —CH2C(═CH2)(CH3); —C(═CH2)CH2CH3; —C(CH3)═CHCH3; —C(CH3)CH═CH2; —CH═CHCH2CH2CH3; —CH2CH═CHCH2CH3; —CH2CH2CH═CHCH3; —CH2CH2CH2CH═CH2; —C(═CH2)CH2CH2CH3; —C(CH3)═CHCH2CH3; —CH(CH3)CH═CHCH; —CH(CH3)CH2CH═CH2; —CH2CH═C(CH3)2; 1-cyclopent-1-enyl; 1-cyclopent-2-enyl; 1-cyclopent-3-enyl; 1-cyclohex-1-enyl; 1-cyclohex-2-enyl; and, 1-cyclohexyl-3-enyl.
As used herein, “alkylaryl” refers to alkyl-substituted aryl groups, both groups being defined as above. Further, as used herein “aralky” means an alkyl group substituted with an aryl radical as defined above. The term “C1-Cn aralalkylene” as used herein is defined as a saturated, divalent hydrocarbon radical having from 1 to n carbon atoms in which an alkylene group as defined above is substituted with an aryl radical as defined above.
The term “hetero” as used herein refers to groups or moieties containing one or more heteroatoms, such as N, O, Si and S. Thus, for example “heterocyclic” refers to cyclic groups having, for example, N, O, Si or S as part of the ring structure. “Heteroalkyl”, “heterocycloalkyl” and “heteroary” moieties are alkyl, cycloalkyl and aryl groups as defined hereinabove, respectively, containing N, O, Si or S as part of their structure.
As regard the compositions and process conditions which may be defined, the term “substantially free” is intended to mean that a compound, element, ion or other like component is not deliberately added to the composition or reaction mixture and is present, at most, in only trace amounts which will have no (adverse) effect on the desired properties of the composition or the progress of the reaction. An exemplary trace amount is less than 1000 ppm by weight of the composition. The term “substantially free” encompasses those embodiments where the specified compound, element, ion, or other like component is completely absent from the composition or reaction mixture or is not present in any amount measurable by techniques generally used in the art.
The term “anhydrous” as used herein has equivalence to the term “substantially free of water”. Water is not deliberately added to a given composition and is present, at most, in only trace amounts which will have no (adverse) effect on the desired properties of the composition.
The initial reactants of the process of the present disclosure may be described as follows:
Eugenol is an allyl chain-substituted guaiacol. Whilst eugenol is naturally present in inter alia celery, dill, ginger, lemon balm, vanilla, wood avens and wormwood, it is conventionally extracted from certain essential oils derived from clove, nutmeg, cinnamon, basil and bay leaf. Eugenol can also be derived from the constituent guaiacyl and syringyl structural units present in lignin.
This compound is classified as a phenolic acid and is found naturally in gall nuts, sumac, witch hazel, tea leaves and oak bark. It is further found in a number of land plants—such as the parasitic plant Cynomorium coccineum—and the aquatic plant Myriophyllum spicatum and the blue green alga Microcystis aeruginosa.
Without intention to limit the present invention, this compound may be synthesized by the reaction of guaiacol (2-methoxyphenol) with vanillin (4-hydroxy-3-methoxybenzaldehyde).
Guaiacol (2-methoxyphenol) consists of a phenol having a methoxy substituent at the ortho position. Whilst the biosynthesis of guaiacol by Leptoglossus phyllopus has been reported, guaiacol is more conventionally derived from the flowering plants guaiacum, from celery seeds, tobacco leaves, orange leaves and lemon peels or as the predominant aromatic monomer of depolymerized lignin. The distillation products of wood and in particular hardwood dry distillation oil are important sources of guaicol.
Vanillin (4-hydroxy-3-methoxybenzaldehyde) is the main chemical compound of the extract of the seed pods of the orchid Vanilla planifolia. However, other sustainable sources of vanillin are known. It can, for example, be obtained from guaiacol sourced in the above mentioned manner or it may itself be derived from thermal and/or electro-chemical lignin depolymerization processes.
The described reaction of vanillin and guaiacol should be performed in the presence of a catalyst, with proton acids and/or Lewis acids being suitable in this regard. Exemplary proton acids include hydrochloric acid, sulfuric acid, phosphoric acid, perchloric acid, oxalic acid, trifluoracetic acid and organic sulfonic acids, such as methanesulfonic acid and p-toluenesulfonic acid (PTSA). Exemplary Lewis acids include boron trifluoride, ferric chloride, zinc chloride, zinc bromide, stannic chloride and titanium chloride. It is noted that good results have been obtained where the reaction is performed either with concentrated sulfuric acid or with p-toluene sulfonic acid mediated zinc chloride.
Exemplary solvents for this reaction are polar aprotic solvents including but not limited to: C1-C8 alkanols, such as ethanol; acetonitrile; N,N-di(C1-C4)alkylacylamides, such as N,N-dimethylformamide (DMF) and N,N-dimethylacetamide (DMAc); hexamethylphosphoramide; N-methylpyrrolidone; pyridine; esters, such as (C1-C8)alkyl acetates, ethoxydiglycol acetate, dimethyl glutarate, dimethyl maleate, dipropyl oxalate, ethyl lactate, benzyl benzoate, butyloctyl benzoate and ethylhexyl benzoate; ketones, such as acetone, ethyl ketone, methyl ethyl ketone (2-butanone) and methyl isobutyl ketone; ethers, such as tetrahydrofuran (THF), 2-methyltetrahydrofuran (2-MeTHF) and 1,2-dimethoxyethane; 1,3-dioxolane; dimethylsulfoxide (DMSO); and, dichloromethane (DCM).
The method may be performed at temperatures between approximately 0 and 100° C., with temperatures between 20 and 80° C. being preferred. The solvent used, the catalyst used and the temperature of the reaction will be determinative of the reaction time: a duration of from 5 to 200 hours may be required.
The progress of the above reaction may be monitored by known techniques of which mention may be made of 1H NMR, Fourier Transform Infrared Spectroscopy, Ultra Performance Liquid Chromatography (UPLC) or thin layer chromatography (TLC). Upon completion of the reaction, the obtained mixture is filtered to remove solids: the solvent is removed from the filtrate to obtain the crude product (IC).
The crude product (IC) may be used in the subsequent step of the process or, alternatively, the relevant compound may be purified using methods known in the art, including but not limited to solvent extraction, filtration and chromatography.
For completeness, an exemplary method of synthesis of the compound of Formula IC is provided in Zhao S. et al. Renewable Epoxy Thermosets from Fully Lignin-Derived Triphenols, ACS Sustainable Chem. Eng. 6:7600-7608 (2018).
Resveratol is a stilbenoid, a type of natural phenol and a phytoalexin produced by several plants in response to injury or when the plant is under attack by pathogens, such as bacteria or fungi. Important sources of resveratrol, from which the compound may be extracted, include the skins of grapes, blueberries, raspberries, mulberries and peanuts.
In the description below, reference will be made to the appended drawings in which:
The individual steps of the processes as defined above will be discussed in more detail herein below. If a chemical compound is referred to using both a chemical structure and a chemical name, and an ambiguity exists between the structure and the name, the structure predominates.
This process embodiment is characterized in that the compound of formula VI is formed from a compound of formula I via an allyl functional intermediate (III). In the description of this embodiment below, where reference is made to Formulae I, III, V and VI, this is intended to denote, respectively, each of IA-ID, IIIA-IIID, VA-VD and VIA-VID.
In this step of the described process, depicted in
X—(R1)—C(R2)═CH2
In most cases, allyl chloride (X=Cl) is favoured because of lower cost, but the allyl bromides and allyl iodides may be more reactive, particularly in the case of high molecular weight allyl compounds. In an initial statement of preference, it is preferred that: R° is a C1-C4 alkyl; R1 is an C1-C18 alkylene group, C2-C18 oxyalkylene group or C2-C18 thioalkylene group; and, R2 is H or Me. In particular, it is preferred that: R° is a C1-C2 alkyl; R1 is an unsubstituted C1-C12 alkylene group; and, R2 is H or Me. In important embodiments: R1 is an unsubstituted C1-C4 alkylene group; and, R2 is H or Me.
Exemplary primary allyl halides in accordance with Formula II include: 3-chloro-1-propene (allyl chloride); 3-bromoprop-1-ene (allyl bromide); 3-iodoprop-1-ene (allyl iodide); 3-chloro-2-methyl-1-propene (methallyl chloride); 3-bromo-2-methyl-1-propene (methallyl bromide); 3-iodo-2-methyl-1-propene (methallyl iodide); 4-chloro-but-1-ene; 4-bromo-but-1-ene; 4-iodo-but-1-ene; 5-chloropent-1-ene; 5-bromopent-1-ene; 5-iodopent-1-ene; 6-chlorohex-1-ene; 6-bromohex-1-ene; 6-iodohex-1-ene; 7-chlorohept-1-ene; 7-bromohept-1-ene; 7-iodohept-1-ene; 8-chlorooct-1-ene; 8-bromooct-1-ene; 8-iodooct-1-ene; 10-chlorodec-1-ene; 10-bromodec-1-ene; 10-iododec-1-ene; 12-chlorododec-1-ene; 12-bromododec-1-ene; and, 12-iododoc-1-ene. Of the primary allyl halides, a preference for the use of 3-chloro-1-propene (allyl chloride); 3-bromoprop-1-ene (allyl bromide); 3-iodoprop-1-ene (allyl iodide) may be noted, and a particular preference for the use of 3-bromoprop-1-ene is acknowledged.
Exemplary further reactants in accordance with Formula Il include: methyl prop-2-enyl carbonate; ethyl prop-2-enyl carbonate; prop-2-enyl propyl carbonate; n-butyl prop-2-enyl carbonate; methyl 2-methylprop-2-enyl carbonate; and, ethyl 2-methylprop-2-enyl carbonate. Of these reactants, a preference may be noted for the use of methyl prop-2-enyl carbonate or ethyl prop-2-enyl carbonate.
It is intended that each hydroxyl group in the compound of Formula I be subjected to allylation and, as such, the primary allyl compound (II) should be present in at least a stoichiometric equivalent amount to the number of moles of said hydroxyl groups. The reaction mixture may, in particular, include said primary allyl compound (II) at a molar equivalency of from 1 to 2 relative to the number of moles of the hydroxyl groups of Formula I. Preferably, the allyl compound (II) is reacted at a molar equivalency of from 1.2 to 1.8 relative to the number of moles of the hydroxyl groups of Formula I.
The base which is present will react with the halogen acid liberated in the reaction and therefore should be present in at least the stoichiometric amount from that reaction. The reaction is operable in the presence of excess base however and therefore the base may be present in the reaction mixture in an amount of from 1 to 5 molar equivalents to the amount of compound (I). It is preferred that the base is present in an amount of from 1.5 to 3 molar equivalents or from 1.5 to 2.5 molar equivalents to the amount of compound (I).
Without intention to limit the present invention, the base should desirably consist of at least one compound selected from alkali metals, alkaline earth metals, alkali metal (C1-C4) alkoxides, alkaline earth metal (C1-C4) alkoxides, alkali metal carbonates, alkaline earth metal carbonates, alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal hydrides and alkaline earth metal hydrides. A preference for the use of at least one of potassium carbonate, sodium carbonate and calcium carbonate is noted.
In certain embodiments, the addition of a neutral alkali metal salt to the reaction mixture can have a positive effect on the yield of the allyation product. Exemplary alkali metal salts include: sulfates; sulfites; sulfides; halides; nitrates; nitrites; cyanides; borates; phosphates; monohydrogen phosphates; dihydrogen phosphates; phosphites; acid phosphites; and, carboxylates, such as acetates, formates, propionates, oxalates, tartrates, succinates, maleates and adipates.
A small amount of the neutral alkali metal salt—for instance from 0.01 to 0.05 moles per mole of compound (I)—will have a yield-enhancing effect. The amount of said neutral salt should not however exceed the amount of basic catalyst included in the reaction mixture.
This step is still further performed in the presence of inert aprotic solvent. Examples of suitable aprotic solvents, which may be used alone or in combination, include but are not limited to: pentane; hexane; heptanes; cyclopentane; cyclohexane; cycloheptane; dimethylether; chloroform; dimethyl carbonate; ethylmethyl carbonate; diethyl carbonate; toluene; o-xylene; m-xylene; p-xylene; ethylbenzene; 2-propylbenzene (cumene); 2-isopropyltoluene (o-cymol); 3-isopropyltoluene (m-cymol); 4-isopropyltoluene (p-cymol); 1,3,5-trimethylbenzene (mesitylene); acetonitrile; N,N-di(C1-C4)alkylacylamides, such as N,N-dimethylformamide (DMF) and N,N-dimethylacetamide (DMAc); hexamethylphosphoramide; N-methylpyrrolidone; pyridine; esters, such as (C1-C8)alkyl acetates, ethoxydiglycol acetate, dimethyl glutarate, dimethyl maleate, dipropyl oxalate, ethyl lactate, benzyl benzoate, butyloctyl benzoate and ethylhexyl benzoate; ketones, such as acetone, ethyl ketone, methyl ethyl ketone (2-butanone) and methyl isobutyl ketone; ethers, such as tetrahydrofuran (THF), 2-methyltetrahydrofuran (2-MeTHF) and 1,2-dimethoxyethane; 1,3-dioxolane; dimethylsulfoxide (DMSO); and, dichloromethane (DCM).
Whilst it is not critical, it is preferred that the reaction of this step be performed under anhydrous conditions. Where necessary, exposure to atmospheric moisture may be avoided by providing the reaction vessel with an inert, dry gaseous blanket. Whilst dry nitrogen, helium and argon may be used as blanket gases, precaution should be used when common nitrogen gases are used as a blanket, because such nitrogen may not be dry enough on account of its susceptibility to moisture entrainment; the nitrogen may require an additional drying step before use herein.
The reaction need not be performed under reflux conditions but it is preferred to do so. Where reflux conditions are not used, the performance of the reaction at room temperature is not actually precluded but the use of elevated temperatures, for example at least 50° C. or at least 75° C., can drive the reaction. For an exothermic reaction, some cooling might however be required as the reaction progresses.
The process pressure is not critical: as such, the reaction can be run at sub-atmospheric, atmospheric, or super-atmospheric pressures but pressures at or slightly above atmospheric pressure are preferred. Mention in this regard may be made of pressures of from 50 to 200 kPa, for example from 100 to 200 kPa.
The progress of the above reaction may be monitored by known techniques of which mention may be made of 1H NMR, Fourier Transform Infrared Spectroscopy, Ultra Performance Liquid Chromatography (UPLC) or thin layer chromatography (TLC). Upon completion of the reaction, the obtained mixture is filtered to remove solids: the solvent is removed from the filtrate to obtain the crude product.
The crude product may be used in the subsequent step of the process or, alternatively, the relevant compound may be purified using methods known in the art, including but not limited to solvent extraction, filtration and chromatography.
In this step, depicted in
R3—C(50 O)—SH (IV)
Exemplary thiol acids include: thioacetic acid; thiopropionic acid; thiobutyric acid; thioisobutyric acid; thiocinnamic acid (3-phenylprop-2-enethioic S-acid); thiobenzoic acid; 2-methyl-thiobenzoic acid; 3-methyl-thiobenzoic acid; 4-methyl-thiobenzoic acid; 2,4-dimethyl-thiobenzoic acid; and, 3,5-dimethyl-thiobenzoic acid. A particular preference for the use of thioacetic acid or thiobenzoic acid may be mentioned.
Where it is intended that the thiol-ene should occur at each allyl group, the thiol acid (IV) should be present in the reaction mixture in at least a stoichiometric equivalent amount to the moles of said allyl groups. The reaction mixture may, in this instance, include said thiol acid (IV) at a molar equivalency of from 1 to 2 moles relative to said allyl groups. Preferably, the amount of thiol acid (IV) is within the range from 1.2 to 1.8 moles per mole of allyl groups.
Where the reactant includes more than one allyl group, the partial conversion of these groups may occur by using a sub-stoichiometric amount of thiol acid (IV) relative to the total number of moles of said allyl groups.
The skilled artisan will be aware that the reaction of thiol and -ene groups can occur under exposure to actinic irradiation and thus catalysts or accelerators may not strictly be required for this step of the process. However, this does not preclude the use in this step of a Michael addition catalyst, which herein refers to a compound capable of promoting a Michael addition reaction between the thiol acid and compounds of Formula III having terminal C═C unsaturation. Michael addition catalysts may be employed in an amount of from 0 to 5 wt. %, for example from 0.05 to 2 wt. %, based on the weight of said thiol acid.
Conventionally, Michael addition catalysts include amine-based catalysts, base catalysts and organometallic catalysts, which types may be used alone or in combination. Exemplary amine-based catalysts include: proline; triazabicyclodecene (TBD); diazabicycloundecene (DBU); hexahydro methyl pyrimido pyridine (MTBD); diazabicyclononane (DBN); tetramethylguanidine (TMG); and, triethylenediamine (TED, 1,4-diazabicyclo[2.2.2]octane). Examples of the base catalysts include: sodium methoxide; sodium ethoxide; potassium t-butoxide; potassium hydroxide; sodium hydroxide; sodium metal; lithium diisopropylamide (LDA); and, butyllithium. Exemplary organometallic catalysts include: ruthenium catalysts such as (cyclooctadiene) (cyclooctatriene) ruthenium and ruthenium hydride; iron catalysts such as iron (III) chloride and iron acetylacetonate; nickel catalysts such as nickel acetylacetonate, nickel acetate and nickel salicylaldehyde; copper catalysts; palladium catalysts; scandium catalysts; lanthanum catalysts; ytterbium catalysts; and, tin catalysts.
Whilst the thiol-ene reaction can be performed under Michael addition catalysis, these reactions can also be initiated by a free radical generating thermal initiator or a free radical photoinitiator. In this embodiment, the reaction mixture of this step may include from 0.1 to 1 wt. %, for example from 0.1 to 0.5 wt. % of at least one free radical initiator, based on the weight of said thiol acid.
Typically, free radical photoinitiators are divided into those that form radicals by cleavage, known as “Norrish Type I”, and those that form radicals by hydrogen abstraction, known as “Norrish Type II”. The Norrish Type Il photoinitiators require a hydrogen donor, which serves as the free radical source: as the initiation is based on a bimolecular reaction, the Norrrish Type II photoinitiators are generally slower than Norrish Type I photoinitiators which are based on the unimolecular formation of radicals. On the other hand, Norrish Type II photoinitiators possess better optical absorption properties in the near-UV spectroscopic region. The skilled artisan should be able to select an appropriate free radical photoinitiator based on the radiation being employed and the sensitivity of the photoinitiator(s) at that wavelength.
Preferred free radical photoinitiators are those selected from the group consisting of: benzoylphosphine oxides; aryl ketones; benzophenones; hydroxylated ketones; 1-hydroxyphenyl ketones; ketals; and, metallocenes. For completeness, the combination of two or more of these photoinitiators is not precluded in the present invention.
Particularly preferred free radical photoinitiators are those selected from the group consisting of: benzoin dimethyl ether; 1-hydroxycyclohexyl phenyl ketone; benzophenone; 4-chlorobenzophenone; 4-methylbenzophenone; 4-phenylbenzophenone; 4,4′-bis(diethylamino) benzophenone; 4,4′-bis(N,N′-dimethylamino) benzophenone (Michler's ketone); isopropylthioxanthone; 2-hydroxy-2-methylpropiophenone (Daracur 1173); 2-methyl-4-(methylthio)-2-morpholinopropiophenone; methyl phenylglyoxylate; methyl 2-benzoylbenzoate; 2-ethylhexyl 4-(dimethylamino)benzoate; ethyl 4-(N,N-dimethylamino)benzoate; phenylbis (2,4,6-trimethylbenzoyl)phosphine oxide; diphenyl (2,4,6-trimethylbenzoyl)phosphine oxide; and, ethyl phenyl (2,4,6-trimethylbenzoyl)phosphinate. Again, for surety, the combination of two or more of these photoinitiators is not precluded.
Where the reaction mixture of step b) comprises a free radical photoinitiator, irradiation of the reaction mixture generates the active species from the photoinitiator(s) which initiates the reactions. Once that species is generated, the chemistry is subject to the same rules of thermodynamics as any chemical reaction: the reaction rate may be accelerated by heat.
The energy source used to initiate the reaction of this embodiment of step b) will emit at least one of ultraviolet (UV) radiation, infrared (IR) radiation, visible light, X-rays, gamma rays, or electron beams (e-beam). The reaction may typically be activated in less than 2 minutes, and commonly between 0.1 and 100 seconds—for instance between 3 and 12 seconds—when irradiated using commercial curing equipment.
Irradiating ultraviolet light should typically have a wavelength of from 150 to 600 nm and preferably a wavelength of from 200 to 450 nm. Useful sources of UV light include, for instance, extra high-pressure mercury lamps, high pressure mercury lamps, medium pressure mercury lamps, low intensity fluorescent lamps, metal halide lamps, microwave powered lamps, xenon lamps, UV-LED lamps and laser beam sources such as excimer lasers and argon-ion lasers.
Where an e-beam is utilized to initiate the reaction, standard parameters for the operating device may be: an accelerating voltage of from 0.1 to 100 keV; a vacuum of from 10 to 10−3 Pa; an electron current of from 0.0001 to 1 ampere; and, power of from 0.1 watt to 1 kilowatt.
The amount of radiation necessary to sufficiently initiate the reaction will depend on a variety of factors including the angle of exposure to the radiation and the volume of the reaction mixture. Broadly, however, an applied dosage of from 5 to 5000 mJ/cm2 may be cited as being typical: applied dosages of from 50 to 500 mJ/cm2, such as from 50 to 200 mJ/cm2 may be considered highly effective.
As would be recognized by the skilled artisan, photosensitizers can be incorporated into the reaction mixture to improve the efficiency with which a photoinitiator uses the energy delivered. The term “photosensitizer” is used in accordance with its standard meaning to represent any substance that either increases the rate of photoinitiated polymerization or shifts the wavelength at which polymerization occurs. Photosensitizers should be used in an amount of from 0 to 25 wt. %, based on the weight of said free radical photoinitiator.
In lieu of using a free radical photoinitiator, radical generating thermal initiators may be employed in this step. Organic peroxides represent one exemplary class thereof: such organic peroxides may be selected, for example, from: cyclic peroxides; diacyl peroxides; dialkyl peroxides; hydroperoxides; peroxycarbonates; peroxydicarbonates; peroxyesters; and, peroxyketals.
While certain peroxides—such as dialkyl peroxides—have been disclosed as useful initiators in inter alia U.S. Pat. No. 3,419,512 (Lees) and U.S. Pat. No. 3,479,246 (Stapleton) and indeed may have utility herein, hydroperoxides represent a preferred class of initiator. Further, whilst hydrogen peroxide itself may be used, the most desirable polymerization initiators are the organic hydroperoxides. For completeness, included within the definition of hydroperoxides are materials such as organic peroxides or organic peresters which decompose or hydrolyze to form organic hydroperoxides in situ: examples of such peroxides and peresters are cyclohexyl and hydroxycyclohexyl peroxide and t-butyl perbenzoate, respectively.
In an embodiment of the invention, the radical generating thermal initiator comprises or consists of at least one hydroperoxide compound represented by the formula:
RpOOH
As exemplary peroxide initiators, which may be used alone or in combination, there may be mentioned: cumene hydroperoxide (CHP); para-menthane hydroperoxide; t-butyl hydroperoxide (TBH); t-butyl perbenzoate; t-butyl peroxy pivalate; di-t-butyl peroxide; t-butyl peroxy acetate; t-butyl peroxy-2-hexanoate; t-amyl hydroperoxide; 1,2,3,4-tetramethylbutyl hydroperoxide; benzoyl peroxide; dibenzoyl peroxide; 1,3-bis(t-butylperoxyisopropyl) benzene; diacetyl peroxide; butyl 4,4-bis(t-butylperoxy) valerate; p-chlorobenzoyl peroxide; t-butyl cumyl peroxide; di-t-butyl peroxide; dicumyl peroxide; 2,5-dimethyl-2,5-di-t-butylperoxyhexane; 2,5-dimethyl-2,5-di-t-butyl-peroxyhex-3-yne; and, 4-methyl-2,2-di-t-butylperoxypentane.
Without intention to limit the present disclosure, a further exemplary class of radical generating thermal initiators suitable for use in this reaction step are azo polymerization initiators, selected for example from: azo nitriles; azo esters; azo amides; azo amidines; azo imidazoline; and, macro azo initiators.
As representative examples of suitable azo polymerization initiators there may be mentioned: 2,2′-azobis(2-methylbutyronitrile); 2,2′-azobis(isobutyronitrile) (AIBN); 2,2′-azobis(2,4-dimethylvaleronitrile); 2,2′-azobis(4-methoxy-2,4-dimethylvaleronitrile); 1,1′-azobis(cyclohexane-1-carbonitrile); 4,4′-azobis(4-cyanovaleric acid); dimethyl 2,2′-azobis(2-methylpropionate); 2,2′-azobis[2-methyl-N-(2-hydroxyethyl)propionamide]; 2,2′-azobis(N-butyl-2-methylpropionamide); 2,2′-azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride; 2,2′-azobis[2-(2-imidazolin-2-yl)propane]; 2,2′-azobis(2-methylpropionamidine)dihydrochloride; 2,2′-azobis[N-(2-carboxyethyl)-2-methylpropionamidine]tetrahydrate; 4,4-azobis(4-cyanovaleric acid), polymer with alpha, omega-bis(3-aminopropyl)polydimethylsiloxane (VPS-1001, available from Wako Pure Chemical Industries, Ltd.); and, 4,4′-azobis(4-cyanopentanoicacic)·polyethyleneglycol polymer (VPE-0201, available from Wako Pure Chemical Industries, Ltd.).
Redox free radical initiators are a combination of an oxidizing agent and a reducing agent and may also have utility in in step b) based on the thiol-ene. Suitable oxidizing agents may be selected from the group consisting of cyclic peroxides, diacyl peroxides, dialkyl peroxides, hydroperoxides, peroxycarbonates, peroxydicarbonates, peroxyesters and peroxyketals. The corresponding reducing agent may be selected from the group consisting of: alkali metal sulfites; alkali metal hydrogensulfites; alkali metal metabisulfites; formaldehyde sulfoxylates; alkali metal salts of aliphatic sulfinic acids; alkali metal hydrogensulfides; salts of polyvalent metals, in particular Co(II) salts and Fe(II) salts such iron(II) sulfate, iron(II) ammonium sulfate or iron(II) phosphate; dihydroxymaleic acid; benzoin; ascorbic acid; and, reducing saccharides, such as sorbose, glucose, fructose and/or dihydroxyacetone.
Step b) may be performed at a temperature of from 5 to 150° C., with a temperature in the range from 20 to 100° C. being more typical. The complete reaction may be accomplished in as little as one hour but, at lower reaction temperatures, as long as 24 hours may be required. Since the reaction is heterogeneous, agitation throughout the course of the reaction is important to maintain good physical contact between the reactant and to improve the reaction rate. Any means of agitation may be used.
The process pressure in step b) is not critical: as such, the reaction can be run at sub-atmospheric, atmospheric, or super-atmospheric pressures but pressures at or slightly above atmospheric pressure are preferred. Mention in this regard may be made of pressures of from 50 to 200 kPa, for example from 100 to 200 kPa.
The progress of the above reaction may be monitored by known techniques of which mention may be made of 1H NMR, Fourier Transform Infrared Spectroscopy, Ultra Performance Liquid Chromatography (UPLC) or thin layer chromatography (TLC). Upon completion of the reaction, the unreacted thiol acid (IV) may be removed under reduced pressure to yield the crude thioester (V).
That crude product may be used in the subsequent step of the process or, alternatively, the relevant compound may be purified using methods known in the art, including but not limited to solvent extraction, filtration and chromatography.
In this step of the process, depicted in
In this embodiment, said acid or base catalyst should be present in the reaction mixture in an amount of from 0.05 to 0.25 moles per mole of said thioester (IV). As regards, acid-based hydrolysis, common acids include H2SO4 and HCl. For base-catalysed hydrolysis, organic base catalysts are preferred of which non-limiting examples include: pyridine; dimethylaminopyridine (DMAP); proline; triazabicyclodecene (TBD); diazabicycloundecene (DBU); hexahydro methyl pyrimido pyridine (MTBD); diazabicyclononane (DBN); tetramethylguanidine (TMG); and, triethylenediamine (TED, 1,4-diazabicyclo[2.2.2]octane).
The nucleophilic species (H) in the hydrolysis may be water. However, it is preferred that the nucleophile is a C1-C4 alkanol: a particular preference for the use of methanol (MeOH) may be noted. Wherein a C1-C4 alkanol is used the reaction products will be the thiol (VI) and a C1-C4 alkyl ester. That aside, nucleophile (H) should be present in at least a stoichiometric amount to the number of moles of thioester groups of compound (IV). An excess of the nucleophile may serve to drive the reaction to completion.
Whilst not strictly required, the described reaction of this step c) may be carried out in the presence of an inert aprotic solvent. The use of ether solvents is preferred of which mention may be made of: tetrahydrofuran (THF); 2-methyltetrahydrofuran (2-MeTHF); 1,2-dimethoxyethane; and, 1,3-dioxolane.
The reaction need not be performed under reflux conditions but it is preferred to do so. Where reflux conditions are not used, the performance of the reaction at room temperature is not actually precluded but the use of elevated temperatures, for example at least 50° C. or at least 75° C., can drive the reaction. Such elevated temperatures may indeed be required for acid-catalysed hydrolysis.
The process pressure is not critical: as such, the reaction can be run at sub-atmospheric, atmospheric, or super-atmospheric pressures but pressures at or slightly above atmospheric pressure are preferred. Mention in this regard may be made of pressures of from 50 to 200 kPa, for example from 100 to 200 kPa.
The progress of the above reaction may be monitored by known techniques of which mention may be made of 1H NMR, Fourier Transform Infrared Spectroscopy, Ultra Performance Liquid Chromatography (UPLC) or thin layer chromatography (TLC). Upon completion of the reaction, the reaction mixture may be concentrated under evaporative conditions—to remove excess water, C1-C4 alkanol and/or solvent—to yield the crude polythiol (VI). That crude product may be purified using methods known in the art, including but not limited to solvent extraction, filtration and chromatography.
In this process embodiment, the intermediate compound of Formula VB, VC or VD is synthesized in a single step (a) from, respectively, the compound of Formula IB, IC or ID.
In this step of the described process, depicted in
In most cases, the chloride (Y=Cl) is favoured because of lower cost, but the bromides and iodides may be more reactive, particularly in the case of high molecular weight compounds. In an initial statement of preference, it is preferred that R1 is an C1-C18 alkylene group, C2-C18 oxyalkylene group or C2-C18 thioalkylene group. More particularly, it is preferred that: R1 is an unsubstituted C1-C12 alkylene group; R2 is H or Me; and, R3 is C1-C4 alkyl, Co aryl, C7-C18 alkylaryl or C7-C18 aralkyl. In important embodiments: R1 is an unsubstituted C1-C4 alkylene group; R2 is H or Me; and, R3 is a C1-C4 alkyl.
Exemplary thiolate esters in accordance with formula VII include: S-(3-chloropropyl)ethanethioate; S-(3-bromopropyl)ethanethioate; and, S-(3-iodopropyl)ethanethioate.
It is intended that each hydroxyl group in the compound of Formula I be subjected to substitution and, as such, the thiolate ester compound (VII) should be present in at least a stoichiometric equivalent amount to the number of moles of said hydroxyl groups. The reaction mixture may, in particular, include said thiolate ester compound (VII) at a molar equivalency of from 1 to 2 relative to the number of moles of the hydroxyl groups of Formula I. Preferably, the thiolate ester compound (VII) is reacted at a molar equivalency of from 1.2 to 1.8 relative to the number of moles of the hydroxyl groups of Formula I.
The base which is present will react with the halogen acid liberated in the reaction and therefore should be present in at least the stoichiometric amount from that reaction. The reaction is operable in the presence of excess base however and therefore the base may be present in the reaction mixture in an amount of from 1 to 5 molar equivalents to the amount of compound (I). It is preferred that the base is present in an amount of from 1.5 to 3 molar equivalents or from 1.5 to 2.5 molar equivalents to the amount of compound (I).
Without intention to limit the present invention, the base should desirably consist of at least one compound selected from alkali metals, alkaline earth metals, alkali metal (C1-C4)alkoxides, alkaline earth metal (C1-C4) alkoxides, alkali metal carbonates, alkaline earth metal carbonates, alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal hydrides and alkaline earth metal hydrides. A preference for the use of at least one of potassium carbonate, sodium carbonate and calcium carbonate is noted.
In certain embodiments, the addition of a neutral alkali metal salt to the reaction mixture can have a positive effect on the yield of the thioester reaction product (V). Exemplary alkali metal salts include: sulfates; sulfites; sulfides; halides; nitrates; nitrites; cyanides; borates; phosphates; monohydrogen phosphates; dihydrogen phosphates; phosphites; acid phosphites; and, carboxylates, such as acetates, formates, propionates, oxalates, tartrates, succinates, maleates and adipates.
A small amount of the neutral alkali metal salt—for instance from 0.01 to 0.05 moles per mole of compound (I)—will have a yield-enhancing effect. The amount of said neutral salt should not however exceed the amount of basic catalyst included in the reaction mixture.
This step is still further performed in the presence of inert aprotic solvent. Examples of suitable aprotic solvents, which may be used alone or in combination, include but are not limited to: pentane; hexane; heptanes; cyclopentane; cyclohexane; cycloheptane; dimethylether; chloroform; dimethyl carbonate; ethylmethyl carbonate; diethyl carbonate; toluene; o-xylene; m-xylene; p-xylene; ethylbenzene; 2-propylbenzene (cumene); 2-isopropyltoluene (o-cymol); 3-isopropyltoluene (m-cymol); 4-isopropyltoluene (p-cymol); 1,3,5-trimethylbenzene (mesitylene); acetonitrile; N,N-di(C1-C4)alkylacylamides, such as N,N-dimethylformamide (DMF) and N,N-dimethylacetamide (DMAc); hexamethylphosphoramide; N-methylpyrrolidone; pyridine; esters, such as (C1-C8)alkyl acetates, ethoxydiglycol acetate, dimethyl glutarate, dimethyl maleate, dipropyl oxalate, ethyl lactate, benzyl benzoate, butyloctyl benzoate and ethylhexyl benzoate; ketones, such as acetone, ethyl ketone, methyl ethyl ketone (2-butanone) and methyl isobutyl ketone; ethers, such as tetrahydrofuran (THF), 2-methyltetrahydrofuran (2-MeTHF) and 1,2-dimethoxyethane; 1,3-dioxolane; dimethylsulfoxide (DMSO); and, dichloromethane (DCM).
Whilst it is not critical, it is preferred that the reaction of this step be performed under anhydrous conditions. Where necessary, exposure to atmospheric moisture may be avoided by providing the reaction vessel with an inert, dry gaseous blanket. Whilst dry nitrogen, helium and argon may be used as blanket gases, precaution should be used when common nitrogen gases are used as a blanket, because such nitrogen may not be dry enough on account of its susceptibility to moisture entrainment; the nitrogen may require an additional drying step before use herein.
The reaction need not be performed under reflux conditions but it is preferred to do so. Where reflux conditions are not used, the performance of the reaction at 0° C. is not actually precluded but the use of elevated temperatures, for example at least 50° C. or at least 75° C., can drive the reaction. For an exothermic reaction, some cooling might however be required as the reaction progresses.
The process pressure in step a) is not critical: as such, the reaction can be run at sub-atmospheric, atmospheric, or super-atmospheric pressures but pressures at or slightly above atmospheric pressure are preferred. Mention in this regard may be made of pressures of from 50 to 200 kPa, for example from 100 to 200 kPa.
The progress of the above reaction may be monitored by known techniques of which mention may be made of 1H NMR, Fourier Transform Infrared Spectroscopy, Ultra Performance Liquid Chromatography (UPLC) or thin layer chromatography (TLC). Upon completion of the reaction, excess base present in the reaction mixture may be quenched using an appropriate acid, such as hydrochloric acid. Moreover, the inert aprotic solvent may be removed under reduced pressure.
The crude product (VB, VC or VD) may then be separated from the reaction obtained mixture and may be used per se in the subsequent step of the process. Alternatively, the relevant compound may be purified using methods known in the art, including but not limited to solvent extraction, filtration and chromatography.
This step of the process—in which the thioester of formula VB, VC or VD is deprotected to yield, respectively, the corresponding polythiol (VIB, VIC or VID)—is equivalent to step c) as described above and is depicted in
In this process embodiment, the intermediate compound of Formula VA is formed from the compound of Formula IA in a two stage-process, as depicted in
In this step of the described process, depicted in
In most cases, the chloride (Y=Cl) is favoured because of lower cost, but the bromides and iodides may be more reactive, particularly in the case of high molecular weight compounds. In an initial statement of preference, it is preferred that R1 is an C1-C18 alkylene group, C2-C18 oxyalkylene group or C2-C18 thioalkylene group. More particularly, it is preferred that: R1 is an unsubstituted C1-C12 alkylene group; R2 is H or Me; and, R3 is C1-C4 alkyl, C6 aryl, C7-C18 alkylaryl or C7-C18 aralkyl. In important embodiments: R1 is an unsubstituted C1-C4 alkylene group; R2 is H or Me; and, R3 is a C1-C4 alkyl.
Exemplary thiolate esters in accordance with formula VII include: S-(3-chloropropyl)ethanethioate; S-(3-bromopropyl)ethanethioate; and, S-(3-iodopropyl)ethanethioate.
It is intended that each hydroxyl group in the compound of Formula IA be subjected to substitution and, as such, the thiolate ester compound (VII) should be present in at least a stoichiometric equivalent amount to the number of moles of said hydroxyl groups. The reaction mixture may, in particular, include said thiolate ester compound (VII) at a molar equivalency of from 1 to 2 relative to the number of moles of the hydroxyl groups of Formula I. Preferably, the thiolate ester compound (VII) is reacted at a molar equivalency of from 1.2 to 1.8 relative to the number of moles of the hydroxyl groups of Formula I.
The base which is present will react with the halogen acid liberated in the reaction and therefore should be present in at least the stoichiometric amount from that reaction. The reaction is operable in the presence of excess base however and therefore the base may be present in the reaction mixture in an amount of from 1 to 5 molar equivalents to the amount of compound (I). It is preferred that the base is present in an amount of from 1.5 to 3 molar equivalents or from 1.5 to 2.5 molar equivalents to the amount of compound (I).
Without intention to limit the present invention, the base should desirably consist of at least one compound selected from alkali metals, alkaline earth metals, alkali metal (C1-C4)alkoxides, alkaline earth metal (C1-C4) alkoxides, alkali metal carbonates, alkaline earth metal carbonates, alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal hydrides and alkaline earth metal hydrides. A preference for the use of at least one of potassium carbonate, sodium carbonate and calcium carbonate is noted.
In certain embodiments, the addition of a neutral alkali metal salt to the reaction mixture can have a positive effect on the yield of the thioester reaction product (V). Exemplary alkali metal salts include: sulfates; sulfites; sulfides; halides; nitrates; nitrites; cyanides; borates; phosphates; monohydrogen phosphates; dihydrogen phosphates; phosphites; acid phosphites; and, carboxylates, such as acetates, formates, propionates, oxalates, tartrates, succinates, maleates and adipates.
A small amount of the neutral alkali metal salt—for instance from 0.01 to 0.05 moles per mole of compound (I)—will have a yield-enhancing effect. The amount of said neutral salt should not however exceed the amount of basic catalyst included in the reaction mixture.
This step is still further performed in the presence of inert aprotic solvent. Examples of suitable aprotic solvents, which may be used alone or in combination, include but are not limited to: pentane; hexane; heptanes; cyclopentane; cyclohexane; cycloheptane; dimethylether; chloroform; dimethyl carbonate; ethylmethyl carbonate; diethyl carbonate; toluene; o-xylene; m-xylene; p-xylene; ethylbenzene; 2-propylbenzene (cumene); 2-isopropyltoluene (o-cymol); 3-isopropyltoluene (m-cymol); 4-isopropyltoluene (p-cymol); 1,3,5-trimethylbenzene (mesitylene); acetonitrile; N,N-di(C1-C4)alkylacylamides, such as N,N-dimethylformamide (DMF) and N,N-dimethylacetamide (DMAc); hexamethylphosphoramide; N-methylpyrrolidone; pyridine; esters, such as (C1-C8)alkyl acetates, ethoxydiglycol acetate, dimethyl glutarate, dimethyl maleate, dipropyl oxalate, ethyl lactate, benzyl benzoate, butyloctyl benzoate and ethylhexyl benzoate; ketones, such as acetone, ethyl ketone, methyl ethyl ketone (2-butanone) and methyl isobutyl ketone; ethers, such as tetrahydrofuran (THF), 2-methyltetrahydrofuran (2-MeTHF) and 1,2-dimethoxyethane; 1,3-dioxolane; dimethylsulfoxide (DMSO); and, dichloromethane (DCM).
Whilst it is not critical, it is preferred that the reaction of this step be performed under anhydrous conditions. Where necessary, exposure to atmospheric moisture may be avoided by providing the reaction vessel with an inert, dry gaseous blanket. Whilst dry nitrogen, helium and argon may be used as blanket gases, precaution should be used when common nitrogen gases are used as a blanket, because such nitrogen may not be dry enough on account of its susceptibility to moisture entrainment; the nitrogen may require an additional drying step before use herein.
The reaction need not be performed under reflux conditions but it is preferred to do so. Where reflux conditions are not used, the performance of the reaction at 0° C. is not actually precluded but the use of elevated temperatures, for example at least 50° C. or at least 75° C., can drive the reaction. For an exothermic reaction, some cooling might however be required as the reaction progresses.
The process pressure in step aa) is not critical: as such, the reaction can be run at sub-atmospheric, atmospheric, or super-atmospheric pressures but pressures at or slightly above atmospheric pressure are preferred. Mention in this regard may be made of pressures of from 50 to 200 kPa, for example from 100 to 200 kPa.
The progress of the above reaction may be monitored by known techniques of which mention may be made of 1H NMR, Fourier Transform Infrared Spectroscopy, Ultra Performance Liquid Chromatography (UPLC) or thin layer chromatography (TLC). At the completion of the reaction, the crude product (Formula VIII) may be used per se in the subsequent step of the process. In the alternative, the product may be separated from the reaction mixture and may be purified using methods known in the art, including but not limited to solvent extraction, filtration and chromatography. Such separation and purification should be preceded by the quenching of the reaction mixture using an appropriate acid, such as hydrochloric acid, and removal of the inert aprotic solvent under reduced pressure.
In this step, the intermediate allyl functional compound (VIIIA) of step aa) is reacted with a thiol acid (IV) to yield the thioester of Formula VA. The reactant thiol acid (IV) has the general formula:
R3—C(50 O)—SH (IV)
The reaction conditions described in step b) herein above are applicable to this reaction step bb) and will not be repeated here for the sake of conciseness.
This step of the process—in which the thioester (VA) is deprotected to yield the corresponding polythiol (VIA)—is equivalent to step c) as described above and is depicted in
In accordance with exemplary but non-limiting embodiments of the present invention, there are provided compounds represented by the Formula VIAa, VIBa and VICa below:
In accordance with the above described reaction steps, these compounds may be formed from Compounds IA, IB and IC:
The polythiol compounds of the present disclosure are considered to be versatile and thereby have a plethora of uses. It is certainly anticipated that the thiol compounds per se may find utility as a curative or otherwise reactive component of an one (1K) or two (2K) component curable composition. Such an one (1K) or two (2K) component curable composition may, in particular, be a coating, adhesive or sealant composition. It is also not precluded that the one (1K) or two (2K) composition may be a dual cure composition.
In an important embodiment of the disclosure, the curable composition comprises:
For surety, it is stated that a given thiol reactive compound b) may have more than one different functional group in its structure: it may, for instance, have an epoxide group and a (meth) acrylate group. Exemplary thiol reactive compounds b) include but are not limited to: epoxide compounds; ethylenically unsaturated compounds; epoxy (meth) acrylate compounds having at least one (meth) acrylate group and at least one epoxide group; and, polyisocyanates. As regards ethylenically unsaturated groups, note may be made of the instructive reference Hoyle et al. Thiol-Enes: Chemistry of the Past with Promise for the Future J. Polym. Sci. A Polym. Chem. 2004, 42:5301 (2004).
No particular limitation is imposed on the number of functional groups (F) possessed by the thiol reactive compound(s): compounds having 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 functional groups may be used, for instance. Moreover, the thiol reactive compound(s) can be a low-molecular-weight substance—possessing a number average molecular weight (Mn) of less than 500 g/mol—or an oligomeric or polymeric substance that has a number average molecular weight (Mn) of at least 500 g/mol. And, of course, mixtures of thiol reactive compounds b) may be used.
The following examples are illustrative of the present invention and are not intended to limit the scope of the invention in any way.
The following commercial compounds are used in the Example:
A suspension of eugenol (9.8 g, 60 mmol), K2CO3 (16.6 g, 120 mmol) and allyl bromide (7.8 mL, 90 mmol) in acetone (140 mL) was stirred at 60° C. for 12 hours. After cooling to ambient temperature, the suspension was filtered through a Celite to remove insoluble solids. The filtrate was concentrated on a rotary evaporator and the obtained crude product was purified by silica gel flash column chromatography eluting with a mixture of cyclohexane (90 wt. %) and ethyl acetate (10 wt. %) to give the allylated product (IIIAa) as a pale yellow liquid in 99% yield.
1H NMR (300 MHz, CDCl3) δ: 6.82 (d, J=8.0 Hz, 1H), 6.75-6.65 (m, 2H), 6.22-5.84 (m, 2H), 5.39 (dq, J=17.2, 1.6 Hz, 1H), 5.27 (dq, J=10.5, 1.4 Hz, 1H), 5.18-5.00 (m, 2H), 4.59 (dt, J=5.4, 1.5 Hz, 2H), 3.87 (s, 3H), 3.34 (dtt, J=6.7, 1.3, 0.6 Hz, 2H).
13C NMR (75 MHz, CDCl3) δ: 149.51, 146.44, 137.75, 133.68, 133.18, 120.44, 117.88, 115.72, 113.73, 112.35, 77.16, 70.13, 55.96, 39.92.
ESI-MS (m/z) calculated for C13H16O2: 204.1144, found: 204.1142.
The above obtained allylated product (IIIAa: 6.1 g, 30 mmol) was reacted with thioacetic acid (7.5 ml, 45 mmol) in the presence of azobisisobutyronitrile (AIBN, 300 mg, 1.8 mmol) at 80° C. for 20 hours. Unreacted thioacetic acid was removed under reduced pressure to give crude dithioester intermediate.
The obtained crude dithioester was hydrolyzed in methanol (83 ml) at 70° C. for 15 hours in the presence of triazabicyclodecene (TBD, 2.4 g, 9.0 mmol). The reaction mixture was concentrated on a rotary evaporator and the residual oil was dissolved in dichloromethane to be washed with water. After drying the organic phase over MgSO4 and removal of volatiles, the desired product (VIAa) was obtained as a yellow liquid in 93%.
1H NMR (300 MHz, CDCl3) δ: 6.87-6.77 (m, 1H), 6.75-6.62 (m, 2H), 4.19-3.97 (m, 2H), 3.84 (s, 3H), 2.81-2.60 (m, 4H), 2.60-2.45 (m, 2H), 2.10 (tt, J=7.0, 6.1 Hz, 2H), 2.00-1.81 (m, 2H), 1.44 (t, J=8.1 Hz, 1H), 1.39-1.31 (m, 1H).
13C NMR (75 MHz, CDCl3) δ: 149.54, 146.58, 134.51, 120.44, 113.76, 112.39, 77.16, 67.21, 55.99, 35.65, 33.99, 33.45, 24.01, 21.43.
ESI-MS (m/z) calculated for C13H20O2S2: 272.0899, found: 272.0897.
A 500 mL two-necked flask equipped with a septum cap and magnetic stirring bar was charged with 200 mL of DMF and gallic acid (60 mmol, 10.21 g). The solution was cooled with an ice bath and potassium carbonate (240 mmol, 33.17 g) was added. After five minutes, allyl bromide (240 mmol, 21.17 ml) was added dropwise using a dropping funnel. The solution was stirred for 30 minutes at 0° C. and then at 25° C. for a period 48 hours. 200 ml of water was added and the aqueous phase was extracted with 3×100 ml of ethyl acetate. The organic phase was washed with 100 mL of brine then dried over MgSO4 and vacuum concentrated. The residue was purified by silica gel chromatography (CH: EtOAc, 90:10) to furnish the product (IIIBa) as a pale yellow liquid (Isolated Yield: 82%).
1H NMR (300 MHz, DMSO-d6) δ: 7.25 (s, 2H), 6.21-5.86 (m, 4H), 5.43 (dq, J=10.0, 1.7 Hz, 2H), 5.39 (q, J=1.8 Hz, 1H), 5.36 (qd, J=1.6, 0.5 Hz, 1H), 5.32-5.27 (m, 2H), 5.26-5.24 (m, 1H), 5.17 (ddt, J=10.4, 1.9, 1.3 Hz, 1H), 4.78 (dt, J=5.4, 1.5 Hz, 2H), 4.63 (dt, J=5.0, 1.6 Hz, 4H), 4.54 (dt, J=5.7, 1.4 Hz, 2H).
13C NMR (75 MHz, DMSO) δ: 164.85, 151.90, 141.13, 134.35, 133.39, 132.61, 124.55, 117.76, 117.35, 117.15, 107.98, 73.15, 69.14, 65.11, 39.52.
ESI-MS (m/z) calculated for C19H22O5: 331.1545, found: 331.1551.
In a first step, Allyl-3,4,5-tris (allyloxy)benzoate (22.3 g, 68 mmol) was reacted with thioacetic acid (29 ml, 408 mmol,) and AIBN (2.23 g, 13.6 mmol,) by stirring the mixture at 80° C. for 20 h. Subsequently, unreacted thioacetic acid was removed under reduced pressure. The compound was extracted with DCM: 3×H2O. The organic phase was separated and dried over MgSO4. Volatiles were removed to obtain the product.
For the second step, the compound was dissolved in 400 ml of dry THF and 1.1 equiv. of Conc. HCl (37.8 g) in 90 ml of dry MeOH was added to the solution. The mixture was degassed for 10 min under Ar and the solution was stirred at 70° C. for 22 h. Finally, the solvent was removed, and tetra-thiol was extracted with DCM: 3×H2O. The organic phase was separated and dried over MgSO4. Volatiles were removed to obtain the final product. Further purification was done doing vacuum distillation at 120° C. with 5×10−2 mbar. The isolated yield was 75%.
1H NMR (300 MHz, CDCl3) δ: 7.28 (s, 2H), 4.42 (t, J=6.2 Hz, 2H), 4.13 (dt, J=10.8, 5.8 Hz, 6H), 2.88-2.60 (m, 8H), 2.08 (dp, J=26.9, 6.6 Hz, 8H), 1.45 (q, J=8.1 Hz, 4H).
13C NMR (101 MHz, CDCl3) δ: 166.15, 152.59, 141.94, 125.32, 108.23, 77.16, 71.12, 67.03, 63.32, 34.40, 33.35, 33.02, 21.38.
ESI-MS (m/z) calculated for C19H30O5S4[M+Na]+: 489.0873, found: 489.0886.
EA: calculated for C19H30O5S4: C, 48.90; H, 6.48; S, 27.48. found: C, 48.02; H, 7.32; S, 26.96.
Under magnetic stirring, vanillin (76.1 g, 1 equiv.) and guaiacol (310.4 g, 5 equiv.) were charged into a 1 L single-necked round-bottom flask. Upon complete dissolution of vanillin, zinc chloride (ZnCl2, 6.8 g, 0.1 equiv.) and p-toluenesulfonic acid (PTSA, 9.5 g, 0.1 equiv.) were added. The mixture was kept in open air at 50° C. for 5 days. The progress of the reaction was monitored by thin-layer chromatography (TLC) plate in ethyl acetate/hexane (v/v=1/1) solution. Next, the mixture was washed with hot water (>70° C.) three times to remove the catalysts (ZnCl2 and PTSA). The unreacted guaiacol was removed and recycled using a rotary evaporator under reduced pressure at 140° C. The received viscous liquid was placed in vacuum oven at 90° C. for 12 hours. The crude product (ICa) was further purified by crystallization in chloroform: the obtained triphenol compound was a red powder (Isolated Yield: 63%). Based on the 1H NMR there is one molecule of chloroform as a crystallization molecule.
1H NMR (300 MHz, DMSO-d6) δ: 8.76 (s, 3H, OH), 6.74-6.60 (m, 6H, Ar—H), 6.44 (dd, J=8.3, 1.9 Hz, 3H, Ar—H), 5.23 (s, 1H, Ar3—CH), 3.65 (s, 9H, —CH3).
13C NMR (75 MHz, CDCl3) δ: 147.21, Ar—C, 144.67, Ar—C, 135.72, Ar—C, 121.19, Ar—C, 115.10, Ar—C, 113.27, Ar—C, 55.58, Ar3—C, 54.66, —CH3, 39.52.
ESI-MS (m/z) calculated for C22H22O6: 382.1410, found: 382.1409.
A suspension of triphenol (15.3 g, 40 mmol), K2CO3 (28.193 g, 204 mmol), and allyl bromide (17.63 mL, 204 mmol) in acetone (250 mL) was stirred at 70° C. for 18 hours. After cooling to ambient temperature, the suspension was filtered through a pad of Celite and washed with acetone. The filtrate was evaporated, and the crude product (IIICa) was purified by layer crystallization in acetone: pentane. The final product was a yellow powder (Isolated yield: 82%).
1H NMR (400 MHz, CDCl3) δ: 6.79 (d, J=8.3 Hz, 3H, Ar—H), 6.66 (d, J=2.1 Hz, 3H, Ar—H), 6.56 (dd, J=8.3, 2.1 Hz, 3H, Ar—H), 6.08 (ddt, J=17.3, 10.7, 5.4 Hz, 3H), 5.39 (dt, J=17.1, 1.5 Hz, 4H, Ar3—CH, —CH2), 5.26 (dq, J=10.5, 1.4 Hz, 3H, —CH), 4.58 (dt, J=5.5, 1.5 Hz, 6H, —CH2), 3.75 (s, 9H, —CH3).
13C NMR (101 MHz, CDCl3) δ: 149.18, Ar—C, 146.47, Ar—C, 137.33, Ar—C, 133.53, Ar—C, 121.34, —CH, 117.95, —CH2, 113.12, Ar—C, 113.00, Ar—C, 77.16, 69.92, —CH2, 55.93, —CH3, 55.51, Ar3—C.
ESI-MS (m/z) calculated for C31H34O6: 502.2349, found: 502.2345.
In a first step, tris (4-(allyloxy)-3-methoxyphenyl) methane (20.1 g, 40 mmol) was reacted with thioacetic acid (20 ml, 180 mmol) and AIBN (1.55 mg, 9.6 mmol) by stirring the mixture at 80° C. for 24 hours. The conversion can be monitored by 1H NMR. Subsequently, unreacted thioacetic acid was removed under reduced pressure. The compound was extracted with DCM: 3×H2O. The organic phase was separated and dried over MgSO4. Volatiles were removed to obtain the intermediate thioester product.
For the second step, the compound was dissolved in 100 ml of dry THF and 1.1 equiv. of concentrated HCl (12.9 g) in 40 ml of dry MeOH was added to the solution. The mixture was degassed for 10 minutes under Ar and the solution was stirred at 60° C. for 14 hours. Finally, the solvent was removed and the trithiol was extracted with DCM: 3×H2O. The organic phase was separated and dried over MgSO4. Volatiles were removed to obtain the final product. Further purification was done doing vacuum distillation at 120° C. with 5×10−2 mbar. The final product was a condensed orange liquid (Isolated yield: 85%).
1H NMR (300 MHz, CDCl3) δ: 6.83-6.74 (m, 3H, Ar—H), 6.66 (d, J=2.1 Hz, 3H, Ar—H), 6.62-6.52 (m, 3H, Ar—H), 5.35 (d, J=2.8 Hz, 1H, Ar3—CH), 4.08 (t, J=6.1 Hz, 6H, —CH2), 3.73 (s, 9H, —CH3), 2.71 (dt, J=8.2, 6.9 Hz, 6H, —CH2), 2.17-1.99 (m, 6H, —CH2), 1.42 (t, J=8.1 Hz, 3H, —SH).
13C NMR (75 MHz, CDCl3) δ: 149.20, Ar—C, 146.66, Ar—C, 137.29, Ar—C, 121.36, Ar—C, 113.25, Ar—C, 113.04, Ar—C, 77.16, 66.34, —CH2, 55.89, —CH3, 55.41, Ar3—CH, 33.31, —CH2, 21.29, —CH2.
ESI-MS (m/z) calculated for C31H40O6S3: 627.1884, found: 627.1888.
In view of the foregoing description and example, it will be apparent to those skilled in the art that equivalent modifications thereof can be made without departing from the scope of the claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 21214445.5 | Dec 2021 | EP | regional |
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/EP2022/082135 | Nov 2022 | WO |
| Child | 18741949 | US |
