Patent Application
20090062572
The invention encompasses processes for the synthesis of O-desmethylvenlafaxine.
Venlafaxine, (±)-1-[2-(Dimethylamino)-1-(4-methoxyphenyl)ethyl]cyclohexanol is the first of a class of anti-depressants. Venlafaxine acts by inhibiting re-uptake of norepinephrine and serotonin, and is an alternative to the tricyclic anti-depressants and selective re-uptake inhibitors. Venlafaxine has the following chemical formula, Formula I:
O-desmethylvenlafaxine, 4-[2-(dimethylamino)-1-(1-hydroxycyclohexyl)ethyl]phenol, is reported to be a metabolite of venlafaxine and has been reported to inhibit norepinephrine and serotonin uptake. See Klamerus, K. J. et al., “Introduction of the Composite Parameter to the Pharmacokinetics of Venlafaxine and its Active O-Desmethyl Metabolite,” J. Clin. Pharmacol. 32:716-724 (1992). O-desmethylvenlafaxine has the following chemical formula, Formula II:
Processes for the synthesis of O-desmethylvenlafaxine, comprising a step of demethylation of the methoxy group of venlafaxine, are described in U.S. Pat. Nos. 7,026,508 and 6,689,912, and in U.S. publication No. 2005/0197392.
The synthesis disclosed in the above references is performed according to the following scheme:
Wherein “MBC” refers to methyl benzyl cyanide, “CMBC” refers to cyclohexyl methylbenzyl cyanide, “DDMV” refers to didesmethyl venlafaxine, and “ODV” refers to O-desmethylvenlafaxine.
However, the processes disclosed in the above US patents and US patent applications all remain problematic when applied to industrial scale production. Further, the process disclosed in US Application Publication No. 2005/0197392 uses lithiumdiphenyl phosphine, a compound which handling and use in industrial scale processes is extremely dangerous. Also, the process disclosed in U.S. Pat. No. 6,689,912 uses methanol as a solvent, which use is problematic when traces of methanol remain and in subsequent process steps when high temperatures are applied.
There is a need in the art for a new synthetic route for obtaining O-desmethylvenlafaxine, using a precursor of venlafaxine to obtain O-desmethylvenlafaxine rather than by preparing venlafaxine and subsequently demethylating venlafaxine to obtain O-desmethyl venlafaxine.
In one embodiment, there is provided cyclohexylbenzylcyanide (COBC) of the formula:
In another embodiment, the present invention provides a process for preparing cyclohexylbenzylcyanide (COBC) comprising reacting hydroxybenzylcyanide (OBC) with cyclohexanone, preferably the reaction comprises combining OBC, an organic solvent, preferably a dry organic solvent, a base and cyclohexanone.
In another embodiment, the present invention provides a process for obtaining cyclohexylbenzylcyanide (COBC) comprising reacting hydroxybenzylcyanide (OBC) with cyclohexanone in the presence of a phase transfer catalyst and a base.
In another embodiment, the present invention provides a process for obtaining O-desmethylvenlafaxine comprising preparing COBC as described above, and further converting the COBC to O-desmethylvenlafaxine.
In another embodiment, the present invention provides a process for preparing tridesmethyl venlafaxine (TDMV) comprising: reducing COBC, preferably the step of reducing COBC comprises combining COBC, a reducing agent, an organic solvent and a Lewis acid catalyst, preferably boron trifluoride (BF3), to create a reaction mixture, optionally followed by recovery of the TDMV from the reaction mixture.
In another embodiment, the present invention provides a process for obtaining O-desmethylvenlafaxine comprising preparing TDMV as described above, and further converting the TDMV to O-desmethylvenlafaxine.
In another embodiment, the present invention provides a process for preparing O-desmethylvenlafaxine comprising: reacting hydroxybenzylcyanide (OBC) with cyclohexanone, preferably the step of reacting with cyclohexanone comprises combining OBC, an organic solvent, a base and cyclohexanone; reducing COBC, preferably the step of reducing COBC comprises combining a reducing agent, an organic solvent and a Lewis acid catalyst, preferably boron trifluoride (BF3), to create a reaction mixture; optionally recovering TDMV from the reaction mixture and converting the TDMV to O-desmethylvenlafaxine.
In another embodiment, the present invention provides a process for preparing O-desmethylvenlafaxine comprising: providing a mixture of hydroxybenzylcyanide (OBC), a phase transfer catalyst, a base and cyclohexanone, to obtain COBC; reducing COBC, preferably the step of reducing COBC comprises combining a reducing agent, an organic solvent and a Lewis acid catalyst, preferably boron trifluoride (BF3), to create a reaction mixture; optionally recovering TDMV from the reaction mixture and converting the TDMV to O-desmethylvenlafaxine.
In another embodiment, the present invention provides a process of preparing O-desmethyl venlafaxine (ODV) comprising combining hydroxybenzylcyanid (OBC) with a protecting reagent to obtain a hydroxyl protected hydroxybenzylcyanide (POBC), converting POBC to hydroxy protected O-desmethylvenlafaxine (PODV), and deprotecting PODV to form ODV.
In yet another embodiment there is provided a hydroxyl protected hydroxybenzylcyanide (POBC). Also provided is a process of preparing POBC from hydroxybenzyl cyanide (OBC).
In another embodiment there is provided a hydroxyl protected cyclcohexylbenzylcyanide (PCOBC). Also provided is a process of preparing PCOBC.
In another embodiment there is provided a hydroxyl protected tridesmethyl venlafaxine (PTDMV). Also provided is a process of preparing PTDMV).
In another embodiment there is provided a hydroxyl protected O-desmethyl venlafaxine (PODV).
In yet other embodiments of the invention each of the other embodiments provide one of each of the following compounds in isolated form: cyclohexylbenzylcyanide (COBC), hydroxyl protected 4-hydroxybenzylcyanide (POBC), hydroxyl protected cyclohexylbenzylcyanide (PCOBC), hydroxyl protected tridesmethyl venlafaxine (PTDMV), and hydroxyl protected O-desmethyl venlafaxine (PODV).
In one embodiment of the invention there is provided a cyclohexylbenzylcyanide compound COBC of the following formula
COBC may be obtained by any of the processes described below. Preferably, COBC is substantially pure, preferably at least 95% pure, more preferably at least 99% pure.
The invention encompasses a synthetic route for obtaining O-desmethylvenlafaxine, from hydroxybenzylcyanide (OBC) and cyclohexylbenzylcyanide (COBC). As used herein, hydroxybenzylcyanide or OBC refers to the compound 4-hydroxybenzylcyanide and cyclohexylbenzylcyanide or COBC refers to the compound 4-[1-cyano-1-(1-hydroxycyclohexyl)methyl]phenol.
As used herein, the term “reduced pressure” refers to a pressure less than atmospheric pressure. As used herein, the term “substantially pure” means a compound of very high purity as is understood by one of skill in the art, such as a purity of about 95%, or greater, as determined, for example, by HPLC area percent. As used herein the term “room temperature” or “RT” means the ambient temperature of an typical laboratory, which is usually about that of Standard Temperature and Pressure (STP). As used herein, an “isolated” compound means the compound has been separated from the reaction mixture in which it was formed.
In the process of the invention, the intermediate hydroxybenzylcyanide (OBC) is condensed with cyclohexanone to form the intermediate (hydroxy)cyclohexylbenzylcyanide (COBC). Further, the cyano group on the COBC is subjected to reduction, to form the intermediate tridesmethyl venlafaxine (TDMV) which is then subjected to selective alkylation to produce O-desmethylvenlafaxine (ODV).
Alternatively, a protected hydroxybenzylcyanide (POBC) intermediate is condensed with cyclohexanone to form the protected intermediate (hydroxy)cyclohexylbenzylcyanide (PCOBC). Further, the cyano group on the PCOBC is subjected to reduction, to form the protected intermediate tridesmethyl venlafaxine (PTDMV) which is then subjected to selective alkylation to produce O-desmethylvenlafaxine (ODV).
The two pathways are as described in the following scheme:
wherein X is a hydroxyl protecting group.
In one embodiment, the present invention provides a process for preparing cyclohexylbenzylcyanide (COBC) comprising reacting hydroxybenzylcyanide (OBC) with cyclohexanone, preferably in the presence of an organic solvent and/or a base. The organic solvent is preferably a “dry organic solvent.” As used herein the term “dry organic solvent” refers to an organic solvent that is essentially free of water such that the amount of residual water, if detectable, does not interfere with the reaction (e.g. by destroying catalysts) in a manner that prevents the benefits of the present invention from being realized. Such dry organic solvent useful in the process of the present invention preferably comprises less about 1% by weight, more preferably less than about 0.1% by weight water, such as about 0.05% by weight to about 0.1% by weight of water.
A suitable organic solvent is selected from the group consisting of: ethers, polar aprotic solvents, aromatic hydrocarbons, and alcohols, acetonitrile, and mixtures thereof. More preferably, the ethers contain 2-8 carbon atoms, more preferably 4-8 carbon atoms, or are selected from the group consisting of: diisopropyl ether, diethyl ether, dioxane, tetrahydrofuran (THF); preferably, the polar aprotic solvents are selected from the group consisting of dimethylformamide (DMF), dimethylacetamide (DMA) and dimethylsulfoxide (DMSO); and the aromatic hydrocarbons are selected from the group consisting of toluene, xylene, and benzene; preferably the aromatic hydrocarbons contain 6-14 carbon atoms, more preferably from 6-10 carbon atoms, even more preferably toluene, xylene or benzene; preferably, the alcohols contain 1-6 carbon atoms, more preferably 1-4 carbon atoms or are selected from the group consisting of methanol, ethanol, isopropanol (IPA), and butanol. Most preferably, the organic solvent is selected from the group consisting of: tetrahydrofuran (THF), dimethylformamide (DMF), dimethylacetamide (DMA) and dimethylsulfoxide (DMSO). Preferably, the organic solvent is a dry organic solvent.
The organic solvent can be employed as such, or it can be employed in mixture with another organic solvent such as methanol or toluene.
Preferably, the cyclohexanone is present in an amount of about 1 to about 2 moles per mole of OBC, more preferably from about 1.1 mole to about 1.5 mole per mole of OBC.
Preferably, the base is an inorganic base. More preferably, the inorganic base is an alkali metal base. A suitable base for use in the process of the present invention is selected from the group consisting of: lithium diisopropyl amide (LDA), lithium bis(trimethyl silyl) amide (LiN[(CH3)3Si]2), sodium hydroxide (NaOH), potassium hydroxide (KOH), lithium hydroxide (LiOH), cesium hydroxide (CsOH), sodium hydride (NaH), potassium hydride (KH), cesium hydride (CsH), potassium tert butoxide (t-BuOK), lithium tert butoxide (t-BuOLi), butyl lithium (BuLi) and sodium methoxide (NaOMe). When the organic solvent is tetrahydrofuran (THF), the base is preferably lithium diisopropyl amide (LDA), and when the organic solvent is a polar aprotic solvent, such as for example DMSO, the base is preferably sodium methoxide (NaOMe).
Preferably, the base is present in an amount of about 1 to about 5 moles per mole of OBC, more preferably in an amount of about 1.5 to about 3.5 moles per mole of OBC, even more preferably the amount is from about 2 to about 3 moles per mole of OBC.
In one embodiment of the invention, a solution or a slurry of hydroxybenzylcyanide (OBC) and an organic solvent may be first combined with a base, followed by combining the obtained reaction mixture with cyclohexanone, to obtain COBC. The initial reaction mixture may be cooled prior to adding cyclohexanone, preferably cooling is to a temperature of about −50° C. to about −80° C., preferably about −65° C. Preferably, cyclohexanone is added to the reaction mixture in a dropwise manner.
After combining the reaction mixture with cyclohexanone, the mixture may be further maintained, preferably at a constant temperature of about −40° C. to about 35° C., preferably with stirring, for a sufficient time to obtain a useful amount of COBC, which is generally at least 10 minutes, preferably at least 45 min, more preferably from about 1 hour to an overnight period (about 8 to 18 hours), even more preferably from about 2 hours to about 5 hours.
COBC may be further recovered from the reaction mixture by any method known in the art. In one embodiment, recovery of COBC from the reaction mixture comprises the steps of extracting COBC from the reaction mixture, preferably with ethylacetate, washing the obtained organic layer, preferably with a saturated ammonium chloride solution and brine, and evaporating the solvent, preferably under reduced pressure, to obtain crude COBC. Such recovery may further comprise the steps of slurrying the crude COBC in a chlorinated hydrocarbon, preferably methylene chloride, filtering the slurry, washing the solid with methylene chloride, and drying to obtain substantially pure COBC.
In another embodiment, the present invention provides a process for obtaining cyclohexylbenzylcyanide (COBC) from a mixture of hydroxybenzylcyanide (OBC), a phase transfer catalyst, a base and cyclohexanone.
Preferably, the phase transfer catalyst is selected from the group consisting of: tetrabutylammonium hydrogensulphate; a tetraalkylammonium halide wherein the alkyl group can be the same or different and contains from 1 to 6, such as for example tetrabutylammonium bromide, tetrabutylammonium chloride, or tetrabutylammonium iodide; benzyltriethyl ammonium chloride; a quaternary ammonium salt; a quaternary phosphonium salt and a crown ether. More preferably, the phase transfer catalyst is tetrabutylammonium bromide (TBAB).
The base in this embodiment is preferably an inorganic base. Suitable inorganic bases are, for example, metal oxides and metal carbonates. Preferably, the inorganic base is selected from the group consisting of: NaOH, KOH, LiOH, CsOH, K2CO3, Na2CO3, and Cs2CO3. Other bases suitable for use in the process of the invention are, for example, metal alkanoxides such as sodium methoxide (NaOMe) or sodium ethanoxide (NaOEt). Preferably, the base is present in an amount of about 0.5 to about 3 mole per mole of OBC, more preferably from about 1 mole to about 2 mole per mole of OBC.
Preferably, the cyclohexanone is present in an amount of about 1 to about 2 moles per mole of OBC, more preferably from about 1.1 mole to about 1.5 mole per mole of OBC.
The reaction may occur with or without the presence of an organic solvent or water. Preferably, the reaction occurs in the presence of water.
Preferably, the reaction mixture is maintained, preferably with stirring, for a sufficient period of time to obtain a useful amount of COBC. A sufficient period of time may be from about 1 hour to about 24 hours, preferably an overnight period (about 8 to about 18 hours). One of ordinary skill in the art could easily monitor the reaction to determine whether a sufficient period of time has elapsed.
The present invention also provides hydroxyl protected hydroxybenzylcyanide (POBC) of the following formula:
wherein X is a hydroxyl protecting group. The hydroxyl protecting group may be removed by deprotection.
The hydroxyl group on the 4-hydroxybenzylcyanide (OBC) may be prepared by a process comprising combining OBC with a protecting reagent to form a reaction mixture, optionally in an organic solvent and in the presence of a catalyst, a base or both, to obtain the hydroxyl protected POBC.
A suitable protecting agent can be any known hydroxyl protecting agent. Suitable hydroxyl protecting groups are listed in T. W. Greene, Protecting Groups in Organic Synthesis, (2nd Ed.), which is incorporated herein by reference. Preferably, the hydroxyl protecting group can be a silyl, acetyl, or 3,4-dihydro-2H-puran (DHP). The silyl protecting group is preferably tert-butyldimethylsilyl (TBDMS). The protection reaction may be carried out at any suitable temperature depending on reagent used, preferably the temperature is between about 0° C. to about 100° C., more preferably between about room temperature to about 55° C. A preferred base added to the reaction mixture is selected from the group selected from imidazole, pyridine, triethylamine, lutidine, and dimethylaminopyridine. A catalyst may be added to the mixture, such as for example Pyridinium p-toluene sulfonate (PPTS).
Preferably, POBC is substantially pure, preferably at least 95% pure, more preferably at least 99% pure.
The present invention also provides hydroxyl protected cyclohexylbenzylcyanide (PCOBC). of the following formula:
wherein X is as described above. Preferably, PCOBC is substantially pure, preferably at least 95% pure, more preferably at least 99% pure.
In another embodiment, the present invention provides a process for preparing a hydroxyl protected COBC (PCOBC), according to the processes for preparing COBC, wherein the starting material 4-hydroxybenzylcyanide (OBC) is a hydroxyl protected OBC (POBC) as described in the scheme above.
In another embodiment, the present invention provides a process for obtaining O-desmethylvenlafaxine comprising preparing COBC or PCOBC in any of the methods described above, and further converting them to O-desmethylvenlafaxine.
In another embodiment of the process of the present invention O-desmethyl venlafaxine, salts thereof or hydroxyl protected derivatives thereof may be prepared from hydroxybenzylcyanide by first protecting the hydroxyl group on the hydroxybenzylcyanide (OBC). The hydroxyl protected hydroxybenzylcyanide (POBC) may then be condensed with cyclohexanone to obtain a hydroxyl protected cyclohexylbenzylcyanide (PCOBC) which is reduced to form the hydroxyl protected tridesmethyl venlafaxine (PTDMV) and methylated to form a hydroxyl protected O-desmethyl venlafaxine (PODV) as is shown in the schematic above.
The protected POBC may be converted by any of the above processes to a hydroxyl protected PCOBC, which can be reduced to a hydroxyl protected PTDMV by a process described above, and the protected PTDMV may be methylated to obtain the hydroxyl protected PODV. Subsequently, the PODV is preferably deprotected with an appropriate deprotecting agent depending on the protecting group used. Preferably such deprotection agent can be an acid, such as for example methanesulfonic acid.
The present invention also provides a process for preparing tridesmethyl venlafaxine (TDMV). TDMV may be prepared by reducing COBC. Preferably, COBC is combined with a reducing agent in the presence of an organic solvent and/or a Lewis acid catalyst, preferably boron trifluoride (BF3) to create a reaction mixture. TDMV may be further recovered from the reaction mixture.
In one embodiment, a solution of COBC, a reducing agent and an organic solvent are combined with a Lewis acid catalyst to obtain a reaction mixture, followed by recovery of the TDMV from the reaction mixture.
Preferably, the solution of COBC, reducing agent and organic solvent is cooled prior to combining it with a Lewis acid catalyst. A preferred temperature to which the mixture is cooled is to a temperature of less than about 10° C., more preferably from about −10° C. to about 10° C.
A preferred Lewis acid catalyst is boron trifluoride (BF3). When BF3 is used, it is preferably added as a complex in ether (BF3Et2O), or else the complex may be formed in situ.
In some embodiments, COBC may be prepared by precipitation from a mixture of hydroxybenzylcyanide (OBC), an organic solvent, a base and cyclohexanone; or from a mixture of hydroxybenzylcyanide (OBC), a phase transfer catalyst, a base and cyclohexanone.
Preferably, the reducing agent is selected from the group consisting of: sodium borohydride (NaBH4), lithium borohydride (LiBH4), lithium aluminum hydride (LiAlH4), L-selectride (lithium tri-sec-butylborohydride), and borane. More preferably, the reducing agent is NaBH4.
Alternatively, the reduction can be performed by hydrogenation in the presence of a catalyst, e.g. Ni, Co, Pd/C, or Pt catalyst.
Preferably, the organic solvent is a dry organic solvent. The organic solvent is as described above. More preferably, the organic solvent is THF.
Preferably, the reducing agent is present in an amount of about 1 to about 10 moles per mole of COBC, more preferably in an amount of about 4 to about 10 moles per mole of COBC. A preferred amount of the Lewis acid catalyst, such as BF3, is an amount of about 1 to about 5 moles per mole of COBC, more preferably from about 2 to about 3 mole per mole of COBC.
The reaction mixture in the process of the present invention may be maintained, preferably at a constant temperature, such as at room temperature, preferably while stirring, for a sufficient period of time to obtain TDMV. A preferred period of time is from about 1 hour to about 24 hours, more preferably from about 3 hours to about 12 hours, even more preferably, from about 8 hours to about 10 hours.
TDMV may then be recovered from the reaction mixture by any method known in the art. In one embodiment, recovery of TDMV from the reaction mixture comprises the steps of basifying and optionally extracting TDMV from the reaction mixture, preferably with ethylacetate, washing the obtained organic solution, preferably with water and/or brine, and drying to obtain TDMV, preferably by evaporating the solvent for example under reduced pressure.
The present invention also provides the hydroxyl protected tridesmethyl venlafaxine (PTDMV) of the following formula:
wherein X is as described above. Preferably, PCOBC is substantially pure, preferably at least 95% pure, more preferably at least 99% pure.
In another embodiment, the present invention provides a process for preparing hydroxyl protected tridesmethyl venlafaxine (PTDMV), according to the preparation of TDMV, wherein the starting material the hydroxyl protected PCOBC as described above.
In another embodiment, the present invention provides a process for preparing O-desmethylvenlafaxine comprising preparing TDMV or PTDMV as described above, and further converting them to O-desmethylvenlafaxine.
The conversion of TDMV to O-desmethylvenlafaxine can be performed, for example as described in co-pending U.S. patent application Ser. No. ______, filed Jul. 26, 2007, entitled “Processes for the Synthesis of O-Desmethylvenlafaxine” (Atty Docket No 1662/03304), which is incorporated herein by reference. For example, TDMV may be combined with an organic solvent and a methylating agent to form a mixture, and recovering the O-desmethylvenlafaxine from the mixture. Also, TDMV may be subjected to selective reductive amination to produce O-desmethylvenlafaxine (“ODV”). PTDMV is converted to PO-desmethylvenlafaxine in a similar manner.
In another embodiment, the present invention provides a process for preparing O-desmethylvenlafaxine comprising: reacting hydroxybenzylcyanide (OBC) with cyclohexanone, preferably the step of reacting with cyclohexanone comprises combining OBC, an organic solvent, a base and cyclohexanone; reducing COBC, preferably the step of reducing COBC comprises combining a reducing agent, an organic solvent and boron trifluoride (BF3) to create a reaction mixture; recovering TDMV from the reaction mixture and converting the TDMV to O-desmethylvenlafaxine.
In another embodiment, the present invention provides a process for preparing O-desmethylvenlafaxine comprising: providing a mixture of hydroxybenzylcyanide (OBC), a phase transfer catalyst, a base and cyclohexanone, to obtain COBC; reducing COBC, preferably the step of reducing COBC comprises combining a reducing agent, an organic solvent and boron trifluoride (BF3) to create a reaction mixture; recovering TDMV from the reaction mixture and converting the TDMV to O-desmethylvenlafaxine.
In another embodiment of the present invention a hydroxyl protected O-desmethyl venlafaxine (PODV) may be prepared by any of the above processes wherein the starting material is a hydroxyl protected intermediate as described above. The present invention also provides the hydroxyl protected O-desmethyl venlafaxine (PODV).
The O-desmethyl venlafaxine prepared by any of above process can be prepared in the form of a salt, preferably a succinate salt.
Having described the invention with reference to certain preferred embodiments, other embodiments will become apparent to one skilled in the art from consideration of the specification. The invention is further defined by reference to the following examples describing in detail the synthesis of the compound COBC, tridesmethyl venlafaxine and further their conversion to O-desmethylvenlafaxine. It will be apparent to those skilled in the art that many modifications, both to materials and methods, may be practiced without departing from the scope of the invention.
1.0 ml/min
Mobile phase composition and flow rate may be varied in order to achieve the required system suitability.
Weigh accurately about 10 mg of sample in a 20 ml amber volumetric flask. Dissolve with eluent A.
Inject the sample solutions into the chromatograph, continuing the chromatogram of sample up to the end of the gradient. Determine the areas for each peak in each solution using a suitable integrator.
Impurity Profile Determination
A 100 ml, three necked flask equipped with Nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and THF (15 ml). This solution was cooled to −78° C. and LDA (2M in THF, 16.5 ml, 33 mmol) was added slowly, keeping temperature under −65° C. A white solid precipitated during LDA addition. After the end of the addition, the mixture was stirred for 30 minutes. Cyclohexanone (1.62 g, 16.5 mmol) was then added, and the mixture continued in the same conditions for 5 hours. The reaction was quenched by pouring it into 100 ml of a saturated ammonium chloride solution containing ice.
The product was extracted to EtOAc (3×30 ml). The organic layer was washed with a saturated ammonium chloride solution and brine. Finally the solvent was evaporated under reduced pressure to get 3.5 g of a mixture of OBC (30%) and COBC (60%) (Yield=60%).
This mixture was suspended in 10 ml methylene chloride, where a solid precipitated. The slurry was stirred at room temperature for 2 hours, the solid filtered, washed with methylene chloride and vacuum dried at room temperature, to get 1.9 g COBC (purity 99% by HPLC area, yield=55%).
A 100 ml, three necked flask equipped with Nitrogen inlet, thermometer and magnetic stirrer was charged with OBC (5 g, 37.5 mmol) and DMSO (5 ml). The contents of the flask were stirred to complete dissolving (brown color). KOH (3.2 g, 56 mmol) was added and the reaction mixture stirred vigorously (exothermic).
Cyclohexanone (5.52 g, 56 mmol) was then added dropwise. The reaction was quenched with HCl 5% and methylene chloride was added. The layers were separated and a solid precipitated. The solid was then filtered under reduced pressure and washed with a small amount of methylene chloride to yield 3.2 g of COBC.
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol), toluene (15 ml) and DMF (2 ml). The reaction mixture was stirred at about room temperature (RT) until dissolution was complete and NaH (1.2 g, 30 mmol) was added. Cyclohexanone (1.7 g, 17.3 mmol) was then added dropwise. The reaction was stirred at RT for an additional 1 hr to get 21% COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol), THF (30 ml) and DMF (2 ml). The reaction mixture was stirred at RT until dissolution was complete and t-BuOK (3.3 g, 30 mmol) was added. Cyclohexanone (1.65 g, 16.8 mmol) was then added dropwise and the reaction was stirred at RT for an additional 3.5 hrs to get 19% COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol), THF (15 ml) and DMF (2 ml). The mixture was stirred at RT until complete dissolution and NaH (1.2 g, 30 mmol) was added. Cyclohexanone (1.7 g, 17.3 mmol) was then added dropwise and the reaction was stirred at RT for and additional 2 hrs to get 34% COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) MeOH (15 ml) and DMF (2 ml). The reaction mixture was stirred at RT until complete dissolution and NaOCH3 (1.7 g, 30 mmol) was added. Cyclohexanone (1.7 g, 17.3 mmol) was then added dropwise and the reaction was stirred at RT overnight to obtain 30% COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol), MeOH (10 ml) and DMSO (10 ml). The reaction mixture was stirred at RT until complete dissolution and NaOCH3 (1.7 g, 30 mmol) was added. Cyclohexanone (1.7 g, 17.3 mmol) was added dropwise. The reaction was stirred at RT overnight to obtain 32% COBC (% area HPLC).
A 100 ml, three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and DMSO (10 ml). The reaction mixture was stirred at RT until complete dissolution and NaOCH3 (2.65 g, 47 mmol) was added. Cyclohexanone (2 g, 20.37 mmol) was then added dropwise. The reaction was stirred at RT 10 min to get 43% COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and DMSO (10 ml). The reaction mixture was stirred at RT until complete dissolution and NaOCH3 (1 g, 17.6 mmol) was added. Cyclohexanone (2 g, 20.37 mmol) was then added dropwise. The reaction was stirred at RT 45 min to get 55% of COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and DMSO (10 ml). The reaction mixture was stirred at RT until complete dissolution and LiOH (1 g, 23.8 mmol) was added. Cyclohexanone (2 g, 20.37 mmol) was then added dropwise. The reaction was stirred at RT 8.5 hrs to get 35% of COBC (% area HPLC).
A 100 ml three necked flask equipped with, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol), cyclohexanone (1.7 g, 17.3 mmol), TBAB (0.26 g) and NaOH (6 ml 10%). The reaction was stirred at RT overnight to get 44% COBC (HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and THF (15 ml). The reaction mixture was stirred at RT until complete dissolution and t-BuOLi (2 g, 25 mmol) was added. Cyclohexanone (2 g, 20.37 mmol) was then added dropwise. The reaction was stirred at RT 45 min to get 19% COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet, thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol), THF(15 ml) and DMF (1.5 ml). The reaction mixture was stirred at RT until complete dissolution and t-BuOLi (2.5 g, 30 mmol) was added. Cyclohexanone (2 g, 20.37 mmol) was then added dropwise. The reaction was stirred at RT 1.15 hr to get 23.5% COBC (% area HPLC).
A 100 ml three necked flask equipped with thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and cyclohexanone (2 g, 20.37 mmol), TBAB (0.5 g) and NaOH (13 ml 10%) were added. The reaction was stirred at RT overnight to get 40% COBC (% area HPLC).
A 100 ml three necked flask equipped with thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and cyclohexanone (2.2 g, 22.4 mmol). Water (10 ml), TBAB (0.3 g) and KOH (1.9 g, 30.5 mmol) were then added. The reaction was stirred at RT overnight to get 39% COBC (% area HPLC).
A 100 ml three necked flask equipped with thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol) and cyclohexanone (2.2 g, 22.4 mmol). Water (10 ml), TBAB(0.3 gr) and LiOH (2 g, 47.6 mmol) were then added. The reaction was stirred at RT overnight to get 39% COBC (% area HPLC).
A 100 ml three necked flask equipped with thermometer and mechanical stirrer was charged with OBC (2 g, 15 mmol), DMA (10 ml) and LiOH (2 g, 47.7 mmol). Cyclohexanone (2.2 g, 22.4 mmol) was then added dropwise. The reaction mixture was stirred at RT overnight to get 10% COBC (% area HPLC).
A 100 ml three necked flask equipped with nitrogen inlet thermometer and mechanical stirrer was charged with COBC (2 g, 8.64 mmol), MeOH (50 ml) and CoCl anhydrous (2.25 g, 17.32 mmol). The resulting solution was cooled to −10° C. with an ice-bath. NaBH4 (3.35 g, 88.62 mmol) was added portionwise at this temperature. The ice-bath was removed one hour after the end of addition.
The reaction mixture was stirred 3 hours at room temperature and then quenched with 10% HCl. MeOH was removed under reduced pressure and the aqueous phase was basified with ammonium hydroxide (25%) and extracted with EtOAc. The organic phase was washed with water, brine, dried over Na2SO4 and evaporated under reduced pressure to get 0.4 g of TDMV.
A 100 ml three necked flask equipped with nitrogen inlet thermometer and mechanical stirrer was charged with NaBH4 (1.2 g, 31.74 mmol) THF (10 ml). This solution was cooled to 10° C. with an ice-bath. BF3Et2O (3.95 g, 27.86 mmol) and COBC (2 g, 8.64 mmol) were then added. The reaction mixture was stirred at room temperature overnight.
The reaction mixture was quenched with formic acid and water. The organic phase was basified with NaOH (25%), washed with water and evaporated under reduced pressure to get TDMV.
TDMV (0.5 g, 2.12 mmol) was suspended in CH2Cl2. Methyl iodide (0.26 ml, 4.3 mmol) and triethylamine (0.66 ml, 4.73 mmol) were added. The reaction mixture was stirred under nitrogen atmosphere at room temperature for 6 hours. At this stage methyl iodide (0.5 ml) and NEt3 (1.2 ml) were added. The addition caused the temperature to rise. After 16 hours, HPLC analysis indicated the presence of ODV.
OBC (0.5 g, 3.7 mmol) was dissolved at room temperature in 3,4-dihydro-2H-pyran (DHP) (approx. 2 ml) under N2. Pyridinium p-toluene sulfonate (PPTS, catalytic amount) was added and heated to 55° C. for 45 min. The end of reaction was determined by TLC (eluent EtOAc:Hex 1:1). The product was extracted in EtOAc, washed with brine and dried over MgSO4. A pale yellow powder was obtained (0.74 g, purity=98% by area % of HPLC, yield=91%)
OBC (5 g, 37 mmol), 11 g of TBDMS-Cl, 12 g of imidazole and 25 ml of CH2Cl2 were stirred together for 2 hours at ambient temperature under N2 atmosphere. The product was washed with brine, a 10% aqueous solution of citric acid, brine and dried over MgSO4. After removal of the solvent 4 g of product was obtained.
OBC-DHP (0.74 g, 3.4 mmol), cyclohexanone (0.5 g), TBAB (0.15 g) and a 10% aqueous solution of NaOH (4 ml) were mixed and stirred at room temperature, forming two phases. After 30 minutes of stirring, the organic phase was analyzed by HPLC, containing 46% COBC-DHP and 48% unreacted OBC-DHP.
OBC-DHP (3.25 g, 15 mmol) was dissolved in dry THF under N2 and cooled to −80° C. LDA 2M in THF/heptane/ethyl benzene (8 ml, 16 mmol) was added dropwise, keeping the temperature under −60° C. The mixture was stirred at −80° C. for 30 minutes. Cyclohexanone (1.65 g, 16.5 mmol) was added dropwise. After 1 hour stirring a sample was analyzed by HPLC, containing 41% COBC-DHP and 42% unreacted OBC-DHP.
A 100 ml three necked flask equipped with nitrogen inlet thermometer and mechanical stirrer is charged with PCOBC (8.64 mmol), MeOH (50 ml) and CoCl anhydrous (17.32 mmol). The resulting solution is cooled to −10° C. with an ice-bath. NaBH4 (88.62 mmol) is added portionwise at this temperature. The ice-bath is removed one hour after the end of addition.
The reaction mixture is stirred 3 hours at room temperature and then quenched with 110% HCl. MeOH is removed under reduced pressure and the aqueous phase is basified with ammonium hydroxide (25%) and extracted with EtOAc. The organic phase is washed with water, brine, dried over Na2SO4 and evaporated under reduced pressure to get PTDMV.
A 100 ml three necked flask equipped with nitrogen inlet thermometer and mechanical stirrer is charged with NaBH4 (31.74 mmol) and THF (10 ml). This solution is cooled to 10° C. with an ice-bath. BF3Et2O (27.86 mmol) and PCOBC (8.64 mmol) are then added. The reaction mixture is stirred at room temperature overnight.
The reaction mixture is quenched with formic acid and water. The organic phase is basified with NaOH (25%), washed with water and evaporated under reduced pressure to get PTDMV.
P-TDMV (2.12 mmol) is suspended in CH2Cl2. Methyl iodide (4.3 mmol) and triethylamine (4.73 mmol) are added. The reaction mixture is stirred under nitrogen atmosphere at room temperature for 6 hours. At this stage methyl iodide (0.5 ml) and NEt3 (1.2 ml) are added. After 16 hours, HPLC analysis indicated the presence of PODV.
PODV (2.12 mmol) is suspended in THF in presence of methanesulfonic acid (6 mmol). The reaction is stirred at ambient temperature overnight. To the mixture so-obtained is first added EtOAc and the organic phase is washed with brine, Na2CO3 saturated and water. The organic phase is then concentrated under reduced pressure to get ODV.
The present application claims the benefit of the following U.S. Provisional Patent Application Nos. 60/833,616, filed Jul. 26, 2006; 60/837,879, filed Aug. 14, 2006; 60/849,216, filed Oct. 3, 2006; 60/843,998, filed Sep. 11, 2006; 60/849,255, filed Oct. 3, 2006; 60/906,639, filed Mar. 12, 2007; and 60/906,879, filed Mar. 13, 2007. The contents of these applications are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 60833616 | Jul 2006 | US | |
| 60837879 | Aug 2006 | US | |
| 60849216 | Oct 2006 | US | |
| 60843998 | Sep 2006 | US | |
| 60849255 | Oct 2006 | US | |
| 60906639 | Mar 2007 | US | |
| 60906879 | Mar 2007 | US |
