WO1995023797A1 - Process for making an epoxide - Google Patents

Process for making an epoxide Download PDF

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Publication number
WO1995023797A1
WO1995023797A1 PCT/US1995/002347 US9502347W WO9523797A1 WO 1995023797 A1 WO1995023797 A1 WO 1995023797A1 US 9502347 W US9502347 W US 9502347W WO 9523797 A1 WO9523797 A1 WO 9523797A1
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WO
WIPO (PCT)
Prior art keywords
formula
epoxide
acetonide
allyl
equivalent
Prior art date
Application number
PCT/US1995/002347
Other languages
French (fr)
Inventor
David Askin
Kan K. Eng
Peter E. Maligres
Paul J. Reider
Kai Rossen
Ralph P. Volante
Veena Upadhyay
Original Assignee
Merck & Co., Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
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Family has litigation
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Priority to UA96103798A priority Critical patent/UA45968C2/en
Priority to SK1122-96A priority patent/SK283067B6/en
Priority to SI9530548T priority patent/SI0748319T1/en
Priority to EP95911105A priority patent/EP0748319B1/en
Priority to HU9602412A priority patent/HU222750B1/en
Priority to JP52294995A priority patent/JP3871705B2/en
Priority to AT95911105T priority patent/ATE210662T1/en
Priority to CA002183976A priority patent/CA2183976C/en
Priority to DK95911105T priority patent/DK0748319T3/en
Priority to NZ281866A priority patent/NZ281866A/en
Priority to RU96120179A priority patent/RU2137769C1/en
Priority to BR9506977A priority patent/BR9506977A/en
Priority to RO96-01750A priority patent/RO117696B1/en
Priority to AU18828/95A priority patent/AU690231B2/en
Priority to MX9603871A priority patent/MX9603871A/en
Priority to DE69524578T priority patent/DE69524578T2/en
Application filed by Merck & Co., Inc. filed Critical Merck & Co., Inc.
Publication of WO1995023797A1 publication Critical patent/WO1995023797A1/en
Priority to FI963452A priority patent/FI120259B/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D263/00Heterocyclic compounds containing 1,3-oxazole or hydrogenated 1,3-oxazole rings
    • C07D263/52Heterocyclic compounds containing 1,3-oxazole or hydrogenated 1,3-oxazole rings condensed with carbocyclic rings or ring systems
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A61P31/12Antivirals
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A61P31/12Antivirals
    • A61P31/14Antivirals for RNA viruses
    • A61P31/18Antivirals for RNA viruses for HIV
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P37/00Drugs for immunological or allergic disorders
    • A61P37/02Immunomodulators
    • A61P37/04Immunostimulants
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D413/00Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms
    • C07D413/02Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms containing two hetero rings
    • C07D413/06Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms containing two hetero rings linked by a carbon chain containing only aliphatic carbon atoms

Definitions

  • the present invention is concerned with a novel intermediate and process for synthesizing compounds which inhibit the protease encoded by human immunodeficiency virus (HIV), and in particular, the compound disclosed and referred to as "Compound J” in EPO 541,168, which published on May 12, 1993, or pharmaceutically acceptable salts thereof.
  • HAV human immunodeficiency virus
  • the instant process involves the preparation of the epoxide intermediate for the production of Compound J, the HIV protease inhibitor depicted above.
  • the process relates to iodohydrin formation of the allyl acetonide via the intermediate iodoiminolactone. Base-induced cyclization of the iodohydrin then forms the epoxide intermediate. The iodohydrin formation proceeds with high diastereoselectivity, and there is a substantial absence of hydrolysis of the amide bond linkage in this process.
  • a retrovirus designated human immunodeficiency virus is the etiological agent of the complex disease that includes progressive destruction of the immune system (acquired immune deficiency syndrome; AIDS) and degeneration of the central and peripheral nervous system.
  • This virus was previously known as LAV, HTLV-III, or ARV.
  • a common feature of retrovirus replication is the extensive post-translational processing of precursor polyproteins by a virally encoded protease to generate mature viral proteins required for virus assembly and function. Inhibition of this processing prevents the production of normally infectious virus. For example, Kohl, N.E. et al., Proc. Nat'l Acad.
  • the nucleotide sequence of HIV shows the presence of a pol gene in one open reading frame [Ratner, L. et ah, Nature, 313, 277 (1985)].
  • Amino acid sequence homology provides evidence that the pol sequence encodes reverse transcriptase, an endonuclease and an HIV protease [Toh, H. et al., EMBO J., 4, 1267 (1985); Power, M.D. et al, Science, 231, 1567 (1986); Pearl, L.H. et al, Nature, 329, 351 (1987)].
  • the end product compounds, including Compound J, that can be made from the novel intermediates and process of this invention are inhibitors of HIV protease, and are disclosed in EPO 541 ,168, which published on May 12, 1993.
  • the acetonide is reacted with (S)- glycidyl tosylate in the presence of strong base LHMDS to form the epoxide (see Scheme BETA). Since both the starting material (S)- glycidyl tosylate and product are epoxides, the acetonide anion reacts also with the product epoxide; therefore, about 20% double addition byproducts after formed, in addition to the product epoxide in 71% yield. After crystallization from MeOH, an additional MTBE recrystallization was required to provide the epoxide free of dimer; consequently the overall isolated yield from the acetonide can range from 56-61%. The formation of double nucleophilic addition products is a problem inherent to the electrophile glycidyl tosylate. The (S)-glycidyl tosylate is also presently the most costly raw material in the synthesis of Compound J.
  • a halohydrin from the allyl acetonide reactant comprising the first step of formation of a halohydrin from the allyl acetonide reactant, followed by the step of base-induced cyclization.
  • An additional first step involves allylation of an acetonide reactant to form the allyl acetonide.
  • the products are useful as intermediates for the synthesis of inhibitors of renin or HIV protease or other proteases.
  • the preferred allylation reagents include allyl halides such as allyl chloride, allyl bromide or allyl iodide, as well as other allyl electrophiles such as allyl methane sulfonate or allyl esters in the presence of a transition metal catalyst.
  • Most preferred allylation reagents include allyl halides such as allyl chloride, allyl bromide, and allyl iodide.
  • preferred bases are strong bases and include amide bases such as the lithium, sodium, potassium or magnesium salts of amines, such as diethylamine, disopropylamine, dicyclohexylamine, piperidine, pyrrolidine, or bistrimethylsilylamine; metal alkyls such as the Ci-6 alkyllithium such as n-, iso-, sec-, and tert- butyllithium, methyl, ethyl, or aryl lithiums such as phenyllithium; Grignard reagents such as methyl ethyl, propyl, or butyl magnesium halide; alkoxides such as the methoxide, ethoxide, isopropoxide, tert- butoxide, tert-amyloxide alkoxides of lithium, sodium, potassium or magnesium.
  • amide bases such as the lithium, sodium, potassium or magnesium salts of amines, such as diethylamine, disopropylamine
  • the most preferred base is lithium hexamethyldisilazide (LHMDS).
  • preferred solvents include ethereal solvents such as THF, DME, MTBE, diethylether, diglyme, or dibutylether; hydrocarbon solvents such as pentane, hexane, heptane, benzene, toluene or ethyl benzene; or other solvents compatible with bases and organometallic reagents such as DMSO, DMPU, NMP, TMU, TMEDA, and crown ethers; and including mixtures of these solvents.
  • ethereal solvents such as THF, DME, MTBE, diethylether, diglyme, or dibutylether
  • hydrocarbon solvents such as pentane, hexane, heptane, benzene, toluene or ethyl benzene
  • other solvents compatible with bases and organometallic reagents such as DMSO, DMPU, NMP, TMU, TMEDA, and crown
  • Most preferred solvents for allylation are ethereal solvents for allylation such as THF, DME, and MTBE.
  • the preferred temperature range for the allylation is -78 °C to +30°C.
  • the incubation period lasts at least 15 minutes and typically up to 3 hours.
  • preferred halogenating reagents include halogens, interhalogen compounds, halonium salts, or hypohalite salts or esters, oxyhalogen salts or acids, halo-amides, halo-ureas, halo- carbamates, halo-sulfonamides, halo-amines, or other halogenated nitrogen compounds, or combinations thereof with either halide salts or phase transfer catalysts or both.
  • Preferred halogenating reagents are hypohalite salts or esters, halo amides, ureas, carbamates, sulfonamides, amines, or other halogenated nitrogen compounds such as N- iodosuccinimide, N-bromosuccinimide with an iodide salt, or N- chlorosuccinimide with an iodide salt.
  • Most preferred halogenating reagents are N-iodosuccinimide, N-bromosuccinimide in combination with an iodide salt, or N-chlorosuccinimide in combination with an iodide salt.
  • Reaction conditions for halohydrin formation are solutions, suspensions, or other biphasic systems containing weak bases such as sodium bicarbonate, calcium carbonate, magnesium hydroxide, basic alumina, neutral alumina, sodium acetate, dibasic sodium phosphate, dibasic potassium phosphate, potassium fluoride, other salts, or water in common organic solvents.
  • Preferred reaction conditions are weak bases such as sodium bicarbonate, basic alumina, potassium fluoride, or water. Most preferred reaction conditions are basic alumina, or sodium bicarbonate.
  • Solvents must be compatible with the reaction conditions and include ethers, aromatic chlorinated hydrocarbons, esters, alcohols, MeCN, DMF, DMPU, or ketones.
  • chlorinated hydrocarbons Preferred are chlorinated hydrocarbons, ethers and esters. Most preferred are dichloromethane, IP AC, EtOAc, DME, and MTBE. Temperature range is between about -40°C and about 100°C, but preferably between about 0 and about 35°C. Incubation lasts at least about 10 minutes and is typically stopped before about 48 hours.
  • Base-induced cyclization to form the epoxide is accomplished by treating the halohydrin with a base.
  • bases for such cyclization include hydroxides and oxides of lithium, sodium, potassium, magnesium, calcium, or tetraalkylammonium; alkoxides such as lithium, sodium, potassium, magnesium, and tetraalkylammonium methoxide, ethoxide, n- and iso-propoxide, n-, iso-, sec-, and tert- butoxide.
  • Suitable bases include tertiary and hindered amines such as triethylamine, DIEA, DBU, DBN, DABCO, methyl morpholine, diisiopropylamine, dicyclohexyl amine, bis trimethyl-silylamine or tetra- methylpiperidine as well as metal amide salts thereof.
  • Most preferred bases are lithium, sodium, potassium, or tetraalkylammonium hydroxides; alkoxides such as lithium, sodium and potassium methoxide, ethoxide, iso-propoxide, or tert-butoxide; or tertiary amines such as DIEA.
  • Alkali hydroxide means LiOH, KOH, or NaOH or mixtures thereof.
  • preferred solvents are ethers, esters, hydrocarbons, aromatic solvents, chlorinated hydrocarbons, ketones, water, alcohols, DMSO, MECN, DMF, or DMPU, or other polar solvents, or mixtures thereof. Most preferred solvents are ethers, esters, alcohols, or polar aprotic solvents.
  • Base-induced cyclization is carried out in a temperature range of between about -40°C and about 100°C. Incubation lasts at least about 10 minutes and is typically stopped before about 48 hours.
  • Hydrocarbon solvents include pentane, hexane, heptane, cyclohexane, methyl-cyclohexane, benzene, toluene and xylene.
  • Aromatics as solvents include benzene, toluene, xylene, and ethyl-benzene.
  • Chlorinated hydrocarbons as solvents include methylene chloride, chloroform, carbontetrachloride, dichloroethane, trichloroethane, tetrachloroethane, trichloroethylene, tetrachloroethylene, chlorobenzene and dichlorobenzene.
  • Ethers as solvents include diethyl ether, dibutylether, tetrahydrof ⁇ ran, dimethoxyethane, diethoxyethane, and MTBE.
  • Esters as solvents include ethyl acetate, IPAC, and ethoxyethyl acetate.
  • Ketones as solvents include acetone, MEK, and MEBK.
  • Alcohols as solvents include methanol, ethanol, propanol, isopropanol, butanol, and methoxyethanol.
  • Polar aprotic solvents as solvents include DMF, DMA, DMSO, DMPU, TMU, NMP and acetonitrile.
  • Tertiary amines as solvents include triethylamine, diisopropyl ethyl amine, pyridine, DABCO, DBU, DBN, penamethyl piperidine, and DMAP.
  • said halogenating agent selected from the group consisting of N-iodosuccinimide, N-bromosuccinimide or N- chlorosuccinimide, the last two of which may be combined with an iodide salt, said solvent selected from the group consisting of dichloromethane, IPAC, EtOAc, DME, and MTBE, said weak base selected from basic alumina or sodium bicarbonate, and
  • allylhalide selected from allyl chloride, allyl bromide and allyl iodide, to give the allyl acetonide of Formula ⁇ ,
  • said halogenating agent selected from the group consisting of N-iodosuccinimide, N-bromosuccinimide or N- chlorosuccinimide, the last two of which may be combined with an iodide salt, said solvent selected from the group consisting of dichloromethane, IPAC, EtOAc, DME, and MTBE, said weak base selected from basic alumina or sodium bicarbonate, and
  • a process of synthesizing the epoxide of Formula I comprises the steps of:
  • the processes and intermediates of this invention are useful for the preparation of end-product compounds that are useful in the inhibition of HIV protease, the prevention or treatment of infection by the human immunodeficiency virus (HIV) and the treatment of consequent pathological conditions such as AIDS.
  • Treating AIDS or preventing or treating infection by HTV is defined as including, but not limited to, treating a wide range of states of HIV infection: AIDS, ARC (AIDS related complex), both symptomatic and asymptomatic, and actual or potential exposure to HIV.
  • the end-product compounds that can be made from the processes and intermediates of this invention are useful in treating infection by HIV after suspected past exposure to HIV by, e.g., blood transfusion, organ transplant, exchange of body fluids, bites, accidental needle stick, or exposure to patient blood during surgery.
  • the end-product HIV protease inhibitors are also useful in the preparation and execution of screening assays for antiviral compounds.
  • end-product compounds are useful for isolating enzyme mutants, which are excellent screening tools for more powerful antiviral compounds.
  • such compounds are useful in establishing or determining the binding site of other antivirals to HIV protease, e.g., by competitive inhibition.
  • the end-product compounds that are made from the processes and intermediates of this invention are commercial products to be sold for these purposes.
  • HIV protease inhibitor compounds that can be made from the intermediates and processes of the instant invention are disclosed in EPO 541,164.
  • HIV protease inhibitory compounds may be administered to patients in need of such treatment in pharmaceutical compositions comprising a pharmaceutical carrier and therapeutically- effective amounts of the compound or a pharmaceutically acceptable salt thereof.
  • EPO 541,164 discloses suitable pharmaceutical formulations, administration routes, salt forms and dosages for the compounds.
  • the compounds of the present invention may have asymmetric centers and occur as racemates, racemic mixtures and as individual diastereomers, or enantiomers with all isomeric forms being included in the present invention.
  • any variable e.g., aryl, heterocycle, R, R , R , n, X, etc.
  • its definition on each occurrence is independent of its definition at every other occurrence.
  • combinations of substituents and/or variables are permissible only if such combinations result in stable compounds.
  • alkyl is intended to include both branched- and straight-chain saturated aliphatic hydrocarbon groups having the specified number of carbon atoms (Me is methyl, Et is ethyl, Pr is propyl, Bu is butyl; t-Bu is tert-butyl); "Halo”, as used herein, means fluoro, chloro, bromo and iodo. As used herein, "aryl” is intended to mean phenyl (Ph) or naphthyl.
  • the acetonide was dissolved in 200 mL THF in a 100 mL 3 neck flask equipped with an addition funnel and degassed by bubbling in nitrogen for 20 min.
  • the mixture was cooled to -25 °C and the allyl bromide was added via a weighed syringe.
  • the LHMDS was transferred to the addition funnel under nitrogen pressure via cannula.
  • the LHMDS was allowed to slowly drop into the magnetically stirred reaction mixture over 20 min.
  • the internal temperature reached -14°C while the cooling bath was at -30°C.
  • the mixture was aged at -20 to -15°C for 30 min. Water (100 mL) and IP AC (100 mL) were added and the temperature rose to 5°C.
  • IPAC Isopropyl acetate
  • the crude allyl acetonide was dissolved in IPAC and stirred with the aqueous sodium bicarbonate and NIS for 17 h. Aqueous sodium bisulfite (38-40%) solution was added and the upper organic phase was separated. The organic phase was washed with 300 mL water and 2 x 100 mL brine. At this point the crude iodohydrin solution in IPAC can be directly taken on to the next step or the solution could be evaporated and crystallized from methylcyclohexane-IPAC to give the iodohydrin as a pale yellow crystalline solid, 13c NMR:, m.p. rotation.
  • the iodohydrin in IPAC was stirred with the lithium hydroxide in water for 3 h at 25-30°C.
  • the upper organic phase was washed with 200 mL water and 200 mL brine and was dried over ca 2 g of magnesium sulfate.
  • the IPAC solution was filtered and evaporated (50-60°C, 100 Torr) down to ca 50 mL when the epoxide began to crystallize.
  • the mixture was allowed to cool to 25°C over 30 min and 75 mL of methylcyclohexane were added in 10 mL portions with stirring over 30 min.
  • the mixture was aged for 1 h and the crystals were filtered off and washed with 2 x 20 mL methylcyclohexane and dried to give 24.10 g (64%) of the epoxide as a white crystalline solid of 99.9 A% purity by HPLC.
  • the mother liquor and washes were evaporated to an oil and dissolved in 40 mL IPAC.
  • the solution was treated with 10 g of Darco G60 carbon for 2 h at 25°C and filtered through a pad of Solkafloc. The filtrate was evaporated down to ca 20 mL and 40 mL of methylcyclohexane were added.
  • the crystalline epoxide was filtered off and washed with 2 x 10 mL methylcyclohexane to afford another 4.96 g (13%) of epoxide 96.2 A% by HPLC.
  • the conversion of the iodohydrin to epoxide may also be accomplished by the addition of 1.7 M potassium- tert-butoxide in THF (0.70 mL, 1.2 mmol) or 5 M potassium hydroxide in methanol (0.24 mL, 1.2 mmol) or DIEA (155 mg, 1.2 mmol) to a solution of the iodohydrin (505 mg, 1.0 mmol) in IPAC (2-3 mL) followed by washing with 2 x 2 mL water and crystallization from methylcyclohexane-IPAC.
  • N-chlorosuccinamide 22.7 g
  • Aqueous sodium bicarbonate (0.5 M) 350 mL
  • Isopropyl acetate (IPAC) 300 mL
  • the NCS and Nal were stirred together in 200 mL of water for 20 min. The mixture turned dark brown then immediately a black solid separated out. The solid dissolved and the color faded to clear yellow with further aging.
  • the crude allyl acetonide was dissolved in IPAC and stirred with the aqueous sodium bicarbonate and the clear yellow solution prepared above for 17 h. Aqueous sodium bisulfite (38-40%) solution was added and the upper organic phase was separated. The organic phase was washed with 300 mL water and 2 x 100 mL brine.
  • the ethyl acetate extract was washed with 5% aqueous NaHC ⁇ 3 (10 L) and water (4 L).
  • the ethyl acetate extract was dried by atmospheric distillation and solvent switched to cyclohexane (total volume of ⁇ 30L).
  • the hot cyclohexane solution was allowed to slowly cool to 25°C to crystallize the product.
  • the resulting slurry was further cooled to 10°C and aged for 1 h.
  • the product was isolated by filtration and the wet cake was washed with cold (10°C) cyclohexane (2 X 800 mL).
  • reaction mixture was stirred at -45 to -40°C for 1 h and then allowed to warm to -25°C over 1 h.
  • the mixture is stirred between -25 to -22°C for 4 h (or until the starting acetonide is 3.0 area %).
  • the residual ethyl acetate solvent was removed by charging 10 L of methanol and collecting 10 L of distillate. The resulting slurry was stirred at 22°C for 1 h, then cooled to 5°C and aged for 0.5 h. The product was isolated by filtration and the wet cake was washed with cold methanol (2 X 250 mL).
  • the mixture was partitioned with ethyl acetate (40 L) and water (3 L). The mixture was agitated and the layers were separated.
  • the HPLC assay yield of 6 in ethyl acetate was 86.5%.
  • the penultimate compound 6 in DMF was directly used in the next step without further purification.
  • the mixture was aged at 68°C until the residual penultimate compound 6 was ⁇ 0.3 area % by HPLC analysis.
  • the mixture was stirred at 68°C for 4 h, then cooled to 25°C and partitioned with ethyl acetate (80 L) and a mixture of 24 L of saturated aqueous NaHC03 and distilled water (14 L). The mixture was agitated at 55°C and the layers were separated. The ethyl acetate layer was washed three times with water (20 L) at 55°C. The washed ethyl acetate layer is concentrated at atmospheric pressure to a final pot volume of 30 L. At the end of the atmospheric concentration, water (560 mL) was added to the hot solution and the mixture was cooled to 55°C and seeded with Compound J monohydrate. The mixture was cooled to 4°C and filtered to collect the product. The product was washed with cold ethyl acetate (2 X 3 L), and dried at house vacuum at 25 °C to afford 2905 g (70.7%) of Compound J monohydrate as a white solid.
  • the carboxylic acid 8 was suspended in 27 L of EtOAc and 120 mL of DMF in a 72 L 3 -neck flask with mechanical stirring under N2 and the suspension was cooled to 2°C. The oxalyl chloride was added, maintaining the temperature between 5 and 8°C.
  • the assay for completion of the acid chloride formation is important because incomplete reaction leads to formation of a bis-tert- butyl oxamide impurity.
  • the reaction mixture was aged at 5°C for 1 h.
  • the resulting slurry was cooled to 0°C and the tert-butylamine was added at such a rate as to keep the internal temperature below 20°C.
  • the mixture was aged at 18°C for an additional 30 min.
  • the precipitated ammonium salts were removed by filtration.
  • the filter cake was washed with 12 L of EtOAc.
  • the combined organic phases were washed with 6 L of a 3% NaHC ⁇ 3 and 2 X 2 L of saturated aq. NaCI.
  • the organic phase was treated with 200 g of Darco G60 carbon and filtered through Solka Flok and the cake was washed with 4 L of EtOAc.
  • the EtOAc solution of 9 was concentrated at 10 mbar to 25% of the original volume. 30 L of 1-propanol were added, and the distillation was continued until a final volume of 20 L was reached.
  • the pyrazine-2-tert-butylcarboxamide 9/1 -propanol solution was placed into the 5 gal autoclave.
  • the catalyst was added and the mixture was hydrogenated at 65°C at 40 psi (3 atm) of H2.
  • the reaction could also be monitored by TLC with EtOAc/MeOH (50:50) as solvent and Ninhydrin as developing agent.
  • Acetonitrile 39 L Water 2.4 L
  • the solution of amine 10 in 1 -propanol was charged to a 100 L flask with an attached batch concentrator.
  • the solution was concentrated at 10 mbar and a temperature ⁇ 25°C to a volume of ca 12 L.
  • the (S)-lO-camphorsulfonic acid was charged over 30 min in 4 portions at 20°C. The temperature rose to 40°C after the CSA was added. After a few minutes a thick white precipitate formed. The white slurry was heated to 76°C to dissolve all the solids, the slightly brown solution was then allowed to cool to 21 °C over 8 h.
  • the ee of the material was 95% according to the following chiral HPLC assay: an aliquot of 11 (33 mg) was suspended in 4 mL of EtOH and 1 mL of Et3N. Boc2 ⁇ (11 mg) was added and the reaction mixture was allowed to age for 1 h. The solvent was completely removed in vacuo, and the residue was dissolved in ca. 1 mL of EtOAc and filtered through a Pasteur pipet with Si ⁇ 2, using EtOAc as eluent. The evaporated product fractions were redissolved in hexanes at ca. 1 mg/mL.
  • the chiral assay was carried out using the same system as in the previous step.
  • the solution was then concentrated to ca. 10 L at an intemal temperature of ⁇ 20°C in a batch-type concentrator under 10 mbar vacuum.
  • the solvent switch was completed by slowly bleeding in 20 L of EtOAc and reconcentrating to ca 10 L.
  • the reaction mixture was washed into an extractor with 60 L of EtOAc.
  • the organic phase was washed with 16 L of 5% aqueous Na2C ⁇ 3 solution, 2 X 10 L Di water and 2 X 6 L of saturated aqueous sodium chloride.
  • the combined aqueous washes were back extracted with 20 L of EtOAc and the organic phase was washed with 2 X 3 L water and 2 X 4 L of saturated aqueous sodium chloride.
  • the combined EtOAc extracts were concentrated under 10 mbar vacuum with an internal temperature of ⁇ 20°C in a 100 L batch- type concentrator to ca. 8 L.
  • the solvent switch to cyclohexane was achieved by slowly bleeding in ca. 20 L of cyclohexane, and reconcentrating to ca. 8 L.
  • To the slurry was added 5 L of cyclohexane and 280 mL of EtOAc and the mixture was heated to reflux, when everything went into solution.
  • the solution was cooled and seed (10 g) was added at 58°C.
  • the slurry was cooled to 22°C in 4 h and the product was isolated by filtration after a 1 h age at 22°C.

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Abstract

A process for synthesizing the epoxide of formula (I) consists of, at a minimum, formation of a halohydrin form the allyl acetonide reactant, followed by base-induced cyclization, the epoxide product (I) being useful as an intermediate for the synthesis of inhibitors of renin or HIV protease or other proteases.

Description

TITLE OF THE INVENTION PROCESS FOR MAKING AN EPOXIDE
BACKGROUND OF THE INVENTION
This case is related to Merck Cases 19045, 19046, 19046IA and U.S. Patent 5,169,952.
The present invention is concerned with a novel intermediate and process for synthesizing compounds which inhibit the protease encoded by human immunodeficiency virus (HIV), and in particular, the compound disclosed and referred to as "Compound J" in EPO 541,168, which published on May 12, 1993, or pharmaceutically acceptable salts thereof.
Figure imgf000003_0001
These compounds are of value in the prevention of infection by HIV, the treatment of infection by HIV and the treatment of the resulting acquired immune deficiency syndrome (AIDS).
More specifically, the instant process involves the preparation of the epoxide intermediate for the production of Compound J, the HIV protease inhibitor depicted above. The process relates to iodohydrin formation of the allyl acetonide via the intermediate iodoiminolactone. Base-induced cyclization of the iodohydrin then forms the epoxide intermediate. The iodohydrin formation proceeds with high diastereoselectivity, and there is a substantial absence of hydrolysis of the amide bond linkage in this process.
A retrovirus designated human immunodeficiency virus (HIV) is the etiological agent of the complex disease that includes progressive destruction of the immune system (acquired immune deficiency syndrome; AIDS) and degeneration of the central and peripheral nervous system. This virus was previously known as LAV, HTLV-III, or ARV. A common feature of retrovirus replication is the extensive post-translational processing of precursor polyproteins by a virally encoded protease to generate mature viral proteins required for virus assembly and function. Inhibition of this processing prevents the production of normally infectious virus. For example, Kohl, N.E. et al., Proc. Nat'l Acad. Sci., 85, 4686 (1988), demonstrated that genetic inactivation of the HIV encoded protease resulted in the production of immature, non-infectious virus particles. These results indicate that inhibition of the HIV protease represents a viable method for the treatment of AIDS and the prevention or treatment of infection by HIV.
The nucleotide sequence of HIV shows the presence of a pol gene in one open reading frame [Ratner, L. et ah, Nature, 313, 277 (1985)]. Amino acid sequence homology provides evidence that the pol sequence encodes reverse transcriptase, an endonuclease and an HIV protease [Toh, H. et al., EMBO J., 4, 1267 (1985); Power, M.D. et al, Science, 231, 1567 (1986); Pearl, L.H. et al, Nature, 329, 351 (1987)]. The end product compounds, including Compound J, that can be made from the novel intermediates and process of this invention are inhibitors of HIV protease, and are disclosed in EPO 541 ,168, which published on May 12, 1993.
Previously, the synthesis of Compound J and related compounds was accomplished via a 12-step procedure which employed a hydroxy protected dihydro-5(S)-hydroxymethyl-3(2H) furanone which was alkylated, and involved replacement of an alcohol leaving group on the alkylated furanone with a piperidine moiety. The coupled product was then hydrolyzed to open the furanone ring into a hydroxy acid moiety, and the acid was ultimately coupled to 2(R)-hydroxy-l(S)- aminoindane. This procedure is described in EPO 541,168. The extreme length of this route (12 steps), renders this process time consuming and labor intensive, and it requires the use of many expensive reagents and an expensive starting material. A route requiring fewer reaction steps and/or more efficient reagents would provide desirable economical and time- saving benefits.
The iodolactamization of olefinic tertiary amide A is known to occur with subsequent hydrolysis of the charged iodoiminolactam B intermediate giving the iodolactone C as the only isolated product (Scheme ALPHA). See Tamaru, Y. et al., J. Am. Chem. Soc, 106, 1079- 1085 (1984); Trost, B.M. et al., eds. Comprehensive Organic Synthesis; Selectivity, Strategy, & Efficiency in Modern Organic Chemistry, Volume 4, Pergamon Press, New York 1991, p. 398-421. In this process, it is known that very efficient chirality transfer occurs from the 2-position to the 4-position, to give the 2,4-syn products (represented by the corresponding hydroxy-acid D) in high diastereoselectivity.
SCHEME ALPHA
Figure imgf000005_0001
+
A B
Figure imgf000005_0002
In another existing process, the acetonide is reacted with (S)- glycidyl tosylate in the presence of strong base LHMDS to form the epoxide (see Scheme BETA). Since both the starting material (S)- glycidyl tosylate and product are epoxides, the acetonide anion reacts also with the product epoxide; therefore, about 20% double addition byproducts after formed, in addition to the product epoxide in 71% yield. After crystallization from MeOH, an additional MTBE recrystallization was required to provide the epoxide free of dimer; consequently the overall isolated yield from the acetonide can range from 56-61%. The formation of double nucleophilic addition products is a problem inherent to the electrophile glycidyl tosylate. The (S)-glycidyl tosylate is also presently the most costly raw material in the synthesis of Compound J.
SCHEME BETA
Figure imgf000006_0001
(S)-Glycidyl Tosylate
LHMDS
Figure imgf000006_0002
Acetonide
Acetonide
LHMDS
Figure imgf000006_0003
Epoxide
Figure imgf000006_0004
Double Addition Products The reaction of the lithium enolate of the acetonide intermediate with electrophiles is known to occur with very high selectivity and in high yield for the desired 2(R) products. See Askin, D. et al, J. Org. Chem., 57, 2771-2773 (1992); Askin, D. et al, Tetrahedron Lett.., 35, 673-676 (1994). It was also known that halohydrin derivatives are cleanly converted to the desired epoxide intermediate for Compound J. It was however unexpected that the conditions of the instant invention would result in the isolation of the iodohydrin in excellent yield, exceeding 70% overall from the acetonide intermediates.
SUMMARY OF THE INVENTION
A process is disclosed for synthesizing the epoxide of the formula
Figure imgf000007_0001
comprising the first step of formation of a halohydrin from the allyl acetonide reactant, followed by the step of base-induced cyclization. An additional first step involves allylation of an acetonide reactant to form the allyl acetonide. The products are useful as intermediates for the synthesis of inhibitors of renin or HIV protease or other proteases.
ABBREVIATIONS
Designation Protecting Group BOC (Boc) t-butyloxycarbonyl CBZ (Cbz) benzyloxycarbonyl (carbobenzoxy) TBS (TBDMS) t-butyl-dimethylsilyl Designation Activating Group
Ts or tosyl or tosylate p-toluenesulfonyl
Ns or nosyl or nosy late 3-nitrobenzenesulfonyl
Tf or triflyl or triflate trifluoromethanesulfonyl
Ms or mesyl or mesylate methanesulfonyl
Designation Coupling Reagent BOP reagent benzotriazol-l-yloxytris(dimethylamino)- phosphonium hexafluorophosphate
BOP-C1 bis(2-oxo-3-oxazolidinyl)phosphinic chloride EDC 1 -ethyl-3-(3-dimethylaminopropyl) carbodiimide hydrochloride
Other
BOC-ON 2-(tert-butylcarbonyloxyimino)-2- phenylacetonitrile
(BOC)2θ (BOC20 or Boc2θ) di-t-butyl dicarbonate n-Bu4N+F" tetrabutyl ammonium fluoride nBuLi (n-Buli) n-butyllithium
(S)-CSA (lS)-(+)-10-camphorsulfonic acid
DABCO diazabicyclooctane
DBN diazabicyclononane
DBU diazabicyloundecane
DI deionized
DIEA or DIPEA diisopropylethylamine
DMA dimethylacetamide
DMAP dimethylaminopyridine
DME dimethoxyethane
DMF dimethylformamide
DMPU dimethyltetrahydropyrimidinone
DMSO dimethylsulfoxide
Et3N triethylamine
EtOAc ethyl acetate h hour(s) IPA 2-propanol
KF Karl Fisher titration for water
LDA lithium diisopropylamide
LHMDS lithium hexamethyldisilazide
L-PGA (L)-pyroglutamic acid
MeCN acetonitrile
MTBE methyl t-butyl ether
NMP N-methylpyrrolidinone r.t. room temperature
TFA trifluoroacetic acid
TG thermal gravimetry: loss on heating
THF tetrahydrofuran
TLC thin layer chromatography
TMEDA tetramethylethylenediamine
TMU tetramethyl urea
DETAILED DESCRIPTION OF THE INVENTION
The process of the present invention is illustrated by the following Scheme:
SCHEME GAMMA
Figure imgf000010_0001
Figure imgf000010_0002
Allyl acetonide halogenating agent
Figure imgf000010_0003
Iodohydrin lodoiminolactone
Base X=halo
Epoxide .
Figure imgf000010_0004
The above scheme illustrates three steps, beginning with allylation of the acetonide, followed by halohydrin formation, and then base-induced cyclization forming product epoxide.
In the present invention, a process of synthesizing the epoxide of Formula I,
Figure imgf000011_0001
comprises the steps of:
(a) contacting one equivalent of the allyl acetonide of Formula π,
Figure imgf000011_0002
with about one to two equivalents of a halogenating agent in solvent mixed with aqueous weak base, at a temperature range of between about -40°C and about 100°C, to form the halohydrin of Formula III, and
Figure imgf000012_0001
(b) adding base in solvent or solvents to elicit the formation of the epoxide of Formula I.
From the acetonide reactant the present process of synthesizing the epoxide of Formula I,
Figure imgf000012_0002
comprises the steps of:
(a) reacting one equivalent of the acetonide
Figure imgf000012_0003
with about one equivalent of allylhalide in strong base, to give the allyl acetonide of Formula π,
Figure imgf000013_0001
(b) mixing thereto about one to two equivalents of a halogenating agent in solvent mixed with aqueous weak base, at a temperature range of between about -40°C and about 100°C, to foi the halohydrin of Formula HI, and
Figure imgf000013_0002
(c) adding base in solvent or solvents, to elicit formation of the epoxide of Formula I.
In the preparation of the allyl acetonide of Scheme GAMMA, the preferred allylation reagents include allyl halides such as allyl chloride, allyl bromide or allyl iodide, as well as other allyl electrophiles such as allyl methane sulfonate or allyl esters in the presence of a transition metal catalyst. Most preferred allylation reagents include allyl halides such as allyl chloride, allyl bromide, and allyl iodide.
For this allylation reaction, preferred bases are strong bases and include amide bases such as the lithium, sodium, potassium or magnesium salts of amines, such as diethylamine, disopropylamine, dicyclohexylamine, piperidine, pyrrolidine, or bistrimethylsilylamine; metal alkyls such as the Ci-6 alkyllithium such as n-, iso-, sec-, and tert- butyllithium, methyl, ethyl, or aryl lithiums such as phenyllithium; Grignard reagents such as methyl ethyl, propyl, or butyl magnesium halide; alkoxides such as the methoxide, ethoxide, isopropoxide, tert- butoxide, tert-amyloxide alkoxides of lithium, sodium, potassium or magnesium.
In the allylation reaction, the most preferred base is lithium hexamethyldisilazide (LHMDS).
Also in the allylation reaction, preferred solvents include ethereal solvents such as THF, DME, MTBE, diethylether, diglyme, or dibutylether; hydrocarbon solvents such as pentane, hexane, heptane, benzene, toluene or ethyl benzene; or other solvents compatible with bases and organometallic reagents such as DMSO, DMPU, NMP, TMU, TMEDA, and crown ethers; and including mixtures of these solvents.
Most preferred solvents for allylation are ethereal solvents for allylation such as THF, DME, and MTBE.
The preferred temperature range for the allylation is -78 °C to +30°C. The incubation period lasts at least 15 minutes and typically up to 3 hours.
For halohydrin formation, preferred halogenating reagents include halogens, interhalogen compounds, halonium salts, or hypohalite salts or esters, oxyhalogen salts or acids, halo-amides, halo-ureas, halo- carbamates, halo-sulfonamides, halo-amines, or other halogenated nitrogen compounds, or combinations thereof with either halide salts or phase transfer catalysts or both. Preferred halogenating reagents are hypohalite salts or esters, halo amides, ureas, carbamates, sulfonamides, amines, or other halogenated nitrogen compounds such as N- iodosuccinimide, N-bromosuccinimide with an iodide salt, or N- chlorosuccinimide with an iodide salt. Most preferred halogenating reagents are N-iodosuccinimide, N-bromosuccinimide in combination with an iodide salt, or N-chlorosuccinimide in combination with an iodide salt.
Reaction conditions for halohydrin formation are solutions, suspensions, or other biphasic systems containing weak bases such as sodium bicarbonate, calcium carbonate, magnesium hydroxide, basic alumina, neutral alumina, sodium acetate, dibasic sodium phosphate, dibasic potassium phosphate, potassium fluoride, other salts, or water in common organic solvents. Preferred reaction conditions are weak bases such as sodium bicarbonate, basic alumina, potassium fluoride, or water. Most preferred reaction conditions are basic alumina, or sodium bicarbonate. Solvents must be compatible with the reaction conditions and include ethers, aromatic chlorinated hydrocarbons, esters, alcohols, MeCN, DMF, DMPU, or ketones. Preferred are chlorinated hydrocarbons, ethers and esters. Most preferred are dichloromethane, IP AC, EtOAc, DME, and MTBE. Temperature range is between about -40°C and about 100°C, but preferably between about 0 and about 35°C. Incubation lasts at least about 10 minutes and is typically stopped before about 48 hours.
Base-induced cyclization to form the epoxide is accomplished by treating the halohydrin with a base. Preferred bases for such cyclization include hydroxides and oxides of lithium, sodium, potassium, magnesium, calcium, or tetraalkylammonium; alkoxides such as lithium, sodium, potassium, magnesium, and tetraalkylammonium methoxide, ethoxide, n- and iso-propoxide, n-, iso-, sec-, and tert- butoxide. Other suitable bases include tertiary and hindered amines such as triethylamine, DIEA, DBU, DBN, DABCO, methyl morpholine, diisiopropylamine, dicyclohexyl amine, bis trimethyl-silylamine or tetra- methylpiperidine as well as metal amide salts thereof. Most preferred bases are lithium, sodium, potassium, or tetraalkylammonium hydroxides; alkoxides such as lithium, sodium and potassium methoxide, ethoxide, iso-propoxide, or tert-butoxide; or tertiary amines such as DIEA. Alkali hydroxide means LiOH, KOH, or NaOH or mixtures thereof.
Also for the base-induced cyclization, preferred solvents are ethers, esters, hydrocarbons, aromatic solvents, chlorinated hydrocarbons, ketones, water, alcohols, DMSO, MECN, DMF, or DMPU, or other polar solvents, or mixtures thereof. Most preferred solvents are ethers, esters, alcohols, or polar aprotic solvents. Base-induced cyclization is carried out in a temperature range of between about -40°C and about 100°C. Incubation lasts at least about 10 minutes and is typically stopped before about 48 hours.
In the process of the present invention, a wide variety of solvents can be used, except where noted. Hydrocarbon solvents include pentane, hexane, heptane, cyclohexane, methyl-cyclohexane, benzene, toluene and xylene. Aromatics as solvents include benzene, toluene, xylene, and ethyl-benzene. Chlorinated hydrocarbons as solvents include methylene chloride, chloroform, carbontetrachloride, dichloroethane, trichloroethane, tetrachloroethane, trichloroethylene, tetrachloroethylene, chlorobenzene and dichlorobenzene. Ethers as solvents include diethyl ether, dibutylether, tetrahydrofαran, dimethoxyethane, diethoxyethane, and MTBE. Esters as solvents include ethyl acetate, IPAC, and ethoxyethyl acetate. Ketones as solvents include acetone, MEK, and MEBK. Alcohols as solvents include methanol, ethanol, propanol, isopropanol, butanol, and methoxyethanol. Polar aprotic solvents as solvents include DMF, DMA, DMSO, DMPU, TMU, NMP and acetonitrile. Tertiary amines as solvents include triethylamine, diisopropyl ethyl amine, pyridine, DABCO, DBU, DBN, penamethyl piperidine, and DMAP.
In one embodiment of the present invention, a process of synthesizing the epoxide of Formula I,
Figure imgf000016_0001
comprises the steps of:
(a) contacting one equivalent of the allyl acetonide of Formula π,
Figure imgf000017_0001
with about one to two equivalents of a halogenating agent, in solvent mixed with aqueous weak base, at a temperature range of between about -40°C and about 100°C, to form the halohydrin of Formula HI,
Figure imgf000017_0002
said halogenating agent selected from the group consisting of N-iodosuccinimide, N-bromosuccinimide or N- chlorosuccinimide, the last two of which may be combined with an iodide salt, said solvent selected from the group consisting of dichloromethane, IPAC, EtOAc, DME, and MTBE, said weak base selected from basic alumina or sodium bicarbonate, and
(b) adding base in water to elicit formation of the epoxide of Formula I, said base selected from the group consisting of lithium hydroxide, sodium hydroxide, potassium hydroxide, tetralkylammonium hydroxide; any Ci_4 alkoxide of lithium, sodium or potassium; and DIEA. In another embodiment of the present invention involving the acetonide reactant, the present process of synthesizing the epoxide of Formula I,
Figure imgf000018_0001
comprises the steps of:
(a) reacting one equivalent of the acetonide
Figure imgf000018_0002
with about one equivalent of allylhalide in strong base, said allyl halide selected from allyl chloride, allyl bromide and allyl iodide, to give the allyl acetonide of Formula π,
Figure imgf000018_0003
π (b) mixing thereto about one to two equivalents of a halogenating agent in solvent mixed with aqueous weak base, at a temperature range of between about -40°C and about 100°C, to form the halohydrin of Formula HI,
Figure imgf000019_0001
said halogenating agent selected from the group consisting of N-iodosuccinimide, N-bromosuccinimide or N- chlorosuccinimide, the last two of which may be combined with an iodide salt, said solvent selected from the group consisting of dichloromethane, IPAC, EtOAc, DME, and MTBE, said weak base selected from basic alumina or sodium bicarbonate, and
(c) adding base in water to elicit formation of the epoxide of Formula I, said base selected from the group consisting of lithium hydroxide, sodium hydroxide, potassium hydroxide, tetralkylammonium hydroxide; any Cl-4 alkoxide of lithium, sodium or potassium; and DIEA.
In another embodiment of the present invention, a process of synthesizing the epoxide of Formula I,
Figure imgf000020_0001
comprises the steps of:
(a) contacting one equivalent of the allyl acetonide of Formula π,
Figure imgf000020_0002
said allyl acetonide dissolved in isopropyl acetate, with about one to two equivalents of N-iodosuccinimide in about 0.5 M aqueous sodium bicarbonate, at room temperature, to form the iodohydrin of Formula HI, and
Figure imgf000020_0003
(b) adding alkali hydoxide in water to elicit formation of the epoxide of Formula I. In another embodiment of the present invention, the process of synthesizing the epoxide of Formula I,
Figure imgf000021_0001
comprises the steps of:
(a) reacting one equivalent of the acetonide
Figure imgf000021_0002
said acetonide dissolved in ethereal solvent, with about one equivalent of allylbromide and about one equivalent of about 1.0-2.0 M lithiumhexamethyldisilazide (in ethereal solvent), to give the allyl acetonide of Formula π,
Figure imgf000021_0003
(b) mixing thereto about one to two equivalents of N- iodosuccinimide in about 0.5 M aqueous sodium bicarbonate, at room temperature, to form the iodohydrin of Formula III, and
Figure imgf000022_0001
(c) adding alkali hydroxide in water to elicit formation of the epoxide of Formula I.
The processes and intermediates of this invention are useful for the preparation of end-product compounds that are useful in the inhibition of HIV protease, the prevention or treatment of infection by the human immunodeficiency virus (HIV) and the treatment of consequent pathological conditions such as AIDS. Treating AIDS or preventing or treating infection by HTV is defined as including, but not limited to, treating a wide range of states of HIV infection: AIDS, ARC (AIDS related complex), both symptomatic and asymptomatic, and actual or potential exposure to HIV. For example, the end-product compounds that can be made from the processes and intermediates of this invention are useful in treating infection by HIV after suspected past exposure to HIV by, e.g., blood transfusion, organ transplant, exchange of body fluids, bites, accidental needle stick, or exposure to patient blood during surgery.
The end-product HIV protease inhibitors are also useful in the preparation and execution of screening assays for antiviral compounds. For example, end-product compounds are useful for isolating enzyme mutants, which are excellent screening tools for more powerful antiviral compounds. Furthermore, such compounds are useful in establishing or determining the binding site of other antivirals to HIV protease, e.g., by competitive inhibition. Thus the end-product compounds that are made from the processes and intermediates of this invention are commercial products to be sold for these purposes. HIV protease inhibitor compounds that can be made from the intermediates and processes of the instant invention are disclosed in EPO 541,164. The HIV protease inhibitory compounds may be administered to patients in need of such treatment in pharmaceutical compositions comprising a pharmaceutical carrier and therapeutically- effective amounts of the compound or a pharmaceutically acceptable salt thereof. EPO 541,164 discloses suitable pharmaceutical formulations, administration routes, salt forms and dosages for the compounds.
The compounds of the present invention, may have asymmetric centers and occur as racemates, racemic mixtures and as individual diastereomers, or enantiomers with all isomeric forms being included in the present invention.
When any variable (e.g., aryl, heterocycle, R, R , R , n, X, etc.) occurs more than one time in any constituent, its definition on each occurrence is independent of its definition at every other occurrence. Also, combinations of substituents and/or variables are permissible only if such combinations result in stable compounds.
As used herein except where noted, "alkyl" is intended to include both branched- and straight-chain saturated aliphatic hydrocarbon groups having the specified number of carbon atoms (Me is methyl, Et is ethyl, Pr is propyl, Bu is butyl; t-Bu is tert-butyl); "Halo", as used herein, means fluoro, chloro, bromo and iodo. As used herein, "aryl" is intended to mean phenyl (Ph) or naphthyl.
Representative experimental procedures utilizing the novel process are detailed below. These procedures are exemplary only and should not be construed as being limitations on the novel process of this invention. EXAMPLE 1
Conversion of Acetonide to Allyl Acetonide
Figure imgf000024_0001
Acetonide Allyl acetonide
Acetonide 32.1 g
Allyl bromide 12.70 g
Lithiumhexamethyldisilazide (LHMDS) 1.0 M in THF 105 mL
Tetrahydrofuran (THF) 200 mL
The acetonide was dissolved in 200 mL THF in a 100 mL 3 neck flask equipped with an addition funnel and degassed by bubbling in nitrogen for 20 min. The mixture was cooled to -25 °C and the allyl bromide was added via a weighed syringe. The LHMDS was transferred to the addition funnel under nitrogen pressure via cannula. The LHMDS was allowed to slowly drop into the magnetically stirred reaction mixture over 20 min. The internal temperature reached -14°C while the cooling bath was at -30°C. The mixture was aged at -20 to -15°C for 30 min. Water (100 mL) and IP AC (100 mL) were added and the temperature rose to 5°C. The lower aqueous phase was discarded and the organic phase was washed with 100 mL of 0.2 M HCI in 3% aq. NaCI, 30 mL brine, and 30 mL 0.5 M sodium bicarbonate. The organic phase was evaporated (55°C, 100 Torr) to an oil, another 40 mL of IP AC were added, and the mixture was again evaporated to an oil. At this point the crude allyl acetonide may be taken directly on to the next step or purified by crystallization from 30:1 hexane-IPAC or 30:1 methylcyclohexane- IPAC to give the allyl acetonide as a white crystalline solid in 87% yield. Allyl acetonide 1 c NMR data for major rotamer (62.5 MHz)
171.0 140.4 140.2 134.8
129.6 128.6 128.2 127.1
126.6 125.6 124.0 117.9
96.8 78.9
65.6 47.5 38.6
38.0 36.1 26.6 24.1 ppm
EXAMPLE 2
Conversion of Allyl Acetonide to lodohyrin and Cyclization to Epoxide with NIS
Figure imgf000025_0001
Allyl acetonide Iodohydrin
Figure imgf000025_0002
Allyl acetonide (crude from above preparation) ca 0.1 mol N-iodosuccinimide (NIS) 29.24 g Aqueous sodium bicarbonate (0.5 M) 350 mL
Isopropyl acetate (IPAC) 300 mL
The crude allyl acetonide was dissolved in IPAC and stirred with the aqueous sodium bicarbonate and NIS for 17 h. Aqueous sodium bisulfite (38-40%) solution was added and the upper organic phase was separated. The organic phase was washed with 300 mL water and 2 x 100 mL brine. At this point the crude iodohydrin solution in IPAC can be directly taken on to the next step or the solution could be evaporated and crystallized from methylcyclohexane-IPAC to give the iodohydrin as a pale yellow crystalline solid, 13c NMR:, m.p. rotation.
Iodohydrin (IPAC solution crude from above preparation) ca 0.1 mol Lithium hydroxide monohydrate 50 g
Water 200 mL
Iodohydrin 13C NMR data for major rotamer (62.5 MHz)
172.2 140.6 140.4 139.3
129.5 128.8 128.2 127.2
126.8 125.7 124.0 96.9
79.1 68.7 65.8 43.7
40.6 39.0 36.2 26.5
24.3 16.3 ppm
EXAMPLE 3
Conversion of Allyl Acetonide to lodohyrin and Cyclization to
Epoxide with NCS/Nal
The iodohydrin in IPAC was stirred with the lithium hydroxide in water for 3 h at 25-30°C. The upper organic phase was washed with 200 mL water and 200 mL brine and was dried over ca 2 g of magnesium sulfate. The IPAC solution was filtered and evaporated (50-60°C, 100 Torr) down to ca 50 mL when the epoxide began to crystallize. The mixture was allowed to cool to 25°C over 30 min and 75 mL of methylcyclohexane were added in 10 mL portions with stirring over 30 min. The mixture was aged for 1 h and the crystals were filtered off and washed with 2 x 20 mL methylcyclohexane and dried to give 24.10 g (64%) of the epoxide as a white crystalline solid of 99.9 A% purity by HPLC. The mother liquor and washes were evaporated to an oil and dissolved in 40 mL IPAC. The solution was treated with 10 g of Darco G60 carbon for 2 h at 25°C and filtered through a pad of Solkafloc. The filtrate was evaporated down to ca 20 mL and 40 mL of methylcyclohexane were added. The crystalline epoxide was filtered off and washed with 2 x 10 mL methylcyclohexane to afford another 4.96 g (13%) of epoxide 96.2 A% by HPLC. The conversion of the iodohydrin to epoxide may also be accomplished by the addition of 1.7 M potassium- tert-butoxide in THF (0.70 mL, 1.2 mmol) or 5 M potassium hydroxide in methanol (0.24 mL, 1.2 mmol) or DIEA (155 mg, 1.2 mmol) to a solution of the iodohydrin (505 mg, 1.0 mmol) in IPAC (2-3 mL) followed by washing with 2 x 2 mL water and crystallization from methylcyclohexane-IPAC.
Allyl acetonide 26.15 g
N-chlorosuccinamide (NCS) 22.7 g
Sodium iodide 25.5 g
Aqueous sodium bicarbonate (0.5 M) 350 mL Isopropyl acetate (IPAC) 300 mL
The NCS and Nal were stirred together in 200 mL of water for 20 min. The mixture turned dark brown then immediately a black solid separated out. The solid dissolved and the color faded to clear yellow with further aging. The crude allyl acetonide was dissolved in IPAC and stirred with the aqueous sodium bicarbonate and the clear yellow solution prepared above for 17 h. Aqueous sodium bisulfite (38-40%) solution was added and the upper organic phase was separated. The organic phase was washed with 300 mL water and 2 x 100 mL brine. At this point the crude iodohydrin solution in IPAC can be directly taken on to the next step or the solution could be evaporated and crystallized from methylcyclohexane-IPAC to give the iodohydrin as a pale yellow crystalline solid.
EXAMPLE 4
Preparation of Amide 1
Figure imgf000028_0001
A solution of (-)-cis-l-aminoindan-2-ol (884 g, 5.93 mol) in 17.8 L of dry THF (KF = 55 mg/mL) (KF stands for Karl Fisher titration for water) and triethylamine (868 mL, 6.22 mol) in a 50 L round bottom flask equipped with a thermocouple probe, mechanical stirrer, and a nitrogen inlet adapter and bubbler, was cooled to 15°C. Then, 3- phenylpropionyl chloride (1000 g, 5.93 mol) was added over 75 minutes, while the internal temperature between 14-24°C with an ice-water cooling batch. After addition, the mixture was aged at 18 to 20°C for 30 minutes and checked by HPLC analysis for the disappearance of (-)-cis- 1 -aminoindan-2-ol.
Progress of the reaction is monitored by high performance liquid chromatography (HPLC) analysis: 25 cm Dupont C8-RX column, 60:40 acetonitrile/lOmM (KH2PO4/K2HPO4), 1.0 mL/min., injection volume = 20 mL, detection = 200 nm, sample preparation = 500 X dilution. Approximate retention times:
retention time (min. identity 6.3 cis-aminoindanol The reaction was treated with pyridiniump-toluene- sulfonate (241 g, 0.96 mol, 0.16 equiv.) and stirred for 10 minutes (the pH of the mixture after diluting 1 mL sample with an equal volume of water is between 4.3-4.6). Then, 2-methoxypropene (1.27 L, 13.24 mol, 2.2 equiv.) was added and reaction was heated to 38-40°C for 2 h. The reaction mixture was cooled to 20° C and partitioned with ethyl acetate (12 L) and 5% aqueous NaHC03 (10 L). The mixture was agitated and the layers were separated. The ethyl acetate extract was washed with 5% aqueous NaHCθ3 (10 L) and water (4 L). The ethyl acetate extract was dried by atmospheric distillation and solvent switched to cyclohexane (total volume of ~30L). At the end of the distillation and concentration (20 volume % of ethyl acetate extraction volume), the hot cyclohexane solution was allowed to slowly cool to 25°C to crystallize the product. The resulting slurry was further cooled to 10°C and aged for 1 h. The product was isolated by filtration and the wet cake was washed with cold (10°C) cyclohexane (2 X 800 mL). The washed cake was dried under vacuum (26" of Hg) at 40°C to afford 1.65 kg of acetonide 1 (86.4%, 98 area% by HPLC), iH NMR (300.13 MHz, CDC13, major rotamer) δ 7.36-7.14 (m, 9 H), 5.03 (d, J=4.4, 1 H), 4.66 (m, 1 H) 3.15 (m, 2 H), 3.06 (br s, 2 H), 2.97 (m, 2 H), 1.62 (s, 3 H), 1.37 (s, 3 H); 1 c NMR (75.5 MHz, CDCI3, major rotamer) δc 168.8, 140.9, 140.8, 140.6, 128.6, 128.5, 128.4, 127.1, 126.3, 125.8, 124.1, 96.5, 78.6, 65.9, 38.4, 36.2, 31.9, 26.5, 24.1. Anal. Calcd for C21H23NO2:
C, 78.47; H, 7.21; N, 4.36. Found: C, 78.65; H, 7.24; N, 4.40. EXAMPLE 5
Preparation of Epoxide 3 Tosylate Method
Figure imgf000030_0001
A solution of acetonide 1 (1000 g, 3.11 mol) and 2(S glycidyl tosylate 2 (853 g, 3.74 mol, 1.2 equiv.) in 15.6 L of THF (KF = 22 mg/mL) in a 50 L 4-neck round bottom flask, equipped with a thermocouple, mechanical stirrer, addition funnel and nitrogen inlet adapter was degassed 3 times via vacuum-nitrogen purge and cooled to -56°C. Then, lithium hexamethyldisilazide (LiN[(CH3)3Si]2)(2.6 L, 1.38 M, 1.15 equiv.) was added over 2 h, while keeping the internal temperature between -50 to -45°C. The reaction mixture was stirred at -45 to -40°C for 1 h and then allowed to warm to -25°C over 1 h. The mixture is stirred between -25 to -22°C for 4 h (or until the starting acetonide is 3.0 area %). Progress of the reaction is monitored by HPLC analysis: 25 cm X 4.6 nm Zorbax Silica column, 20% ethyl acetate in hexane, 2.0 mL/min, injection volume = 20 mL, detection = 254 nm, sample preparation = 100 X dilution. Approximate retention times:
retention time (min identity
5.5 amide 1
6.5 glycidyl tosylate 2
13.5 epoxide 3 The reaction mixture was quenched with DI water (6.7 L) at -15°C and partitioned with ethyl acetate (10 L). The mixture was agitated and the layers were separated. The ethyl acetate extract was washed with a mixture of 1% aqueous NaHC03 (5 L) and saturated NaCI (0.5 L). The ethyl acetate extract (28.3 L) was concentrated by vacuum distillation (28" of Hg) and additional ethyl acetate was added to complete the solvent switch to ethyl acetate (final volume = 11.7 L). The ethyl acetate concentrate was further solvent switched to MeOH to crystallize the product and concentrated to a final volume of 3.2 L. The residual ethyl acetate solvent was removed by charging 10 L of methanol and collecting 10 L of distillate. The resulting slurry was stirred at 22°C for 1 h, then cooled to 5°C and aged for 0.5 h. The product was isolated by filtration and the wet cake was washed with cold methanol (2 X 250 mL). The washed cake was dried under vacuum (26" of Hg) at 25°C to afford 727 g of epoxide 3 (61.2%, 98.7 area % of the major epoxide by HPLC): 1 C NMR (300 MHz, CDCI3) δ 171.1, 140.6, 140.5, 139.6, 129.6, 128.8, 128.2, 127.2, 126.8, 125.6, 124.1, 96.8, 79.2, 65.8, 50.0, 48.0, 44.8, 39.2, 37.4, 36.2, 26.6, 24.1.
EXAMPLE 6
Preparation of penultimate 6
Figure imgf000032_0001
A slurry of the 2(S)-t-butylcarboxamide-4-iV-Boc-piperazine 4 (1950 g, 6.83 mol, >99.5% ee) (ee = enantiomeric excess) and the epoxide 3 (2456 g, 97.5:2.5 mixture of 4S/R epoxides, 6.51 mol) in isopropanol (2-propanol, 18.6 L) in a 72 L round bottom flask with four inlets, equipped with a mechanical stirrer, reflux condenser, steam bath, Teflon coated thermocouple and nitrogen inlet, was heated to reflux (internal temperature was 84-85°C). After 40 min, a homogeneous solution was obtained. The mixture was heated at reflux for 28 h. The internal temperature during reflux was 84-85°C. Progress of the reaction was monitored by HPLC analysis: 25 cm Dupont C8-RX column, 60:40 acetonitrile/10 mM (KH2PO4/K2HPO4), 1.0 mL/min., detection = 220 nm, sample preparation = 2 μL, reaction mixture diluted to 1 mL in acetonitrile. Approximate retention times:
retention time (min) identity
4.8 piperazine 4
8.9 epoxide 3
15.2 coupled product 5
After 28 h, the remaining epoxide 3 and coupled product 5 (by HPLC analysis) were 1.5 area % and 91-93 area %, respectively. The mixture was cooled to 0 to 5°C and 20.9 L of 6 N HCI was added while keeping the temperature below 15°C. After the addition was complete, the mixture was warmed to 22°C. Evolution of gas is noted at this point (isobutylene). The mixture was aged at 20 to 22°C for 6 h.
Progress of the reaction was monitored by HPLC analysis: same conditions as above. Approximate retention times:
retention time (min) identitv
7.0 cis-aminoindanol
11.9 penultimate 6
15.1 coupled product 5
The mixture was cooled to 0°C and 7.5 L of 50% NaOH was slowly added to adjust the pH of the mixture to pH=l 1.6, while keeping the temperature less than 25°C during the addition. The mixture was partitioned with ethyl acetate (40 L) and water (3 L). The mixture was agitated and the layers were separated. The organic phase (60 L) was concentrated under reduced pressure (29" of Hg) and solvent switched to DMF and concentrated to a final volume of 10.5 L (KF = 1.8 mg/mL). The HPLC assay yield of 6 in ethyl acetate was 86.5%. The penultimate compound 6 in DMF was directly used in the next step without further purification. For isolated 6: 13c NMR (75.4 MHz, CDCI3) δ 175.2, 170.5, 140.8, 140.5, 139.9, 129.1, 128.5, 127.9, 126.8, 126.5, 125.2, 124.2, 73.0, 66.0, 64.8, 62.2, 57.5, 49.5, 47.9, 46.4, 45.3, 39.6, 39.3, 38.2, 28.9.
EXAMPLE 7
Preparation of monohydrate of Compound J
Figure imgf000034_0001
The solution of 6 in DMF (10.5 L, KF = 10 mg/mL) from the previous step was charged with 8 L of sieve dried DMF (KF. < 30 mg/L) and the mixture was heated with a steam bath under vacuum of 30" of Hg to distill off mainly water and/or any residual isopropanol or ethyl acetate solvent. The final concentrate volume was 13.5 L (KF = 1.8 mg/mL) and then triethylamine (2.86 L, 20.51 mol) was added to the 25°C solution followed by 3-picolyl chloride hydrochloride (96%, 1287 g, 7.84 mol). The resulting slurry was heated to 68°C. The progress of the reaction was followed by HPLC analysis using the same conditions as the previous step. Approximate retention times:
Retention time (min ) Identitv
2.7 DMF
4.2 3-picolyl chloride
4.8 Compound J
9.1 penultimate 6
The mixture was aged at 68°C until the residual penultimate compound 6 was < 0.3 area % by HPLC analysis.
The mixture was stirred at 68°C for 4 h, then cooled to 25°C and partitioned with ethyl acetate (80 L) and a mixture of 24 L of saturated aqueous NaHC03 and distilled water (14 L). The mixture was agitated at 55°C and the layers were separated. The ethyl acetate layer was washed three times with water (20 L) at 55°C. The washed ethyl acetate layer is concentrated at atmospheric pressure to a final pot volume of 30 L. At the end of the atmospheric concentration, water (560 mL) was added to the hot solution and the mixture was cooled to 55°C and seeded with Compound J monohydrate. The mixture was cooled to 4°C and filtered to collect the product. The product was washed with cold ethyl acetate (2 X 3 L), and dried at house vacuum at 25 °C to afford 2905 g (70.7%) of Compound J monohydrate as a white solid.
EXAMPLE 8
Pyrazine-2-tert-butyl carboxamide 9
Figure imgf000035_0001
8 2-Pyrazinecarboxylic acid (8) 3.35 kg (27 mol)
Oxalyl chloride 3.46 kg (27.2 mol) tert-Butylamine (KF = 460 μg/ml) 9.36 L (89 mol)
EtOAc (KF = 56 μg/ml) 27 L
DMF 120 mL
1-Propanol 30 L
The carboxylic acid 8 was suspended in 27 L of EtOAc and 120 mL of DMF in a 72 L 3 -neck flask with mechanical stirring under N2 and the suspension was cooled to 2°C. The oxalyl chloride was added, maintaining the temperature between 5 and 8°C.
The addition was completed in 5h. During the exothermic addition CO and C02 were evolved. The HCI that was formed remained largely in solution. A precipitate was present which is probably the HCI salt of the pyrazine acid chloride. Assay of the acid chloride formation was carried out by quenching an anhydrous sample of the reaction with t- butylamine. At completion <0.7% of acid 8 remained.
The assay for completion of the acid chloride formation is important because incomplete reaction leads to formation of a bis-tert- butyl oxamide impurity.
The reaction can be monitored by HPLC: 25 cm Dupont Zorbax RXC8 column with 1 mL/min flow and detection at 250 nm; linear gradient from 98% of 0.1% aqueous H3PO4 and 2% CH3CN to 50% aqueous H3PO4 and 50% CH3CN at 30 min. Retention times: acid 8 = 10.7 min, amide 9 = 28.1 min.
The reaction mixture was aged at 5°C for 1 h. The resulting slurry was cooled to 0°C and the tert-butylamine was added at such a rate as to keep the internal temperature below 20°C.
The addition required 6 h, as the reaction was very exothermic. A small portion of the generated tert-butylammonium hydrochloride was swept out of the reaction as a fluffy white solid.
The mixture was aged at 18°C for an additional 30 min. The precipitated ammonium salts were removed by filtration. The filter cake was washed with 12 L of EtOAc. The combined organic phases were washed with 6 L of a 3% NaHCθ3 and 2 X 2 L of saturated aq. NaCI. The organic phase was treated with 200 g of Darco G60 carbon and filtered through Solka Flok and the cake was washed with 4 L of EtOAc.
Carbon treatment efficiently removed some purple color in the product.
The EtOAc solution of 9 was concentrated at 10 mbar to 25% of the original volume. 30 L of 1-propanol were added, and the distillation was continued until a final volume of 20 L was reached.
At this point, the EtOAc was below the limit of detection in the H NMR (<1%). The intemal temperature in this solvent change was < 30°C. A 1-propanol/EtOAC solution of 3 was stable to reflux atatmospheric pressure for several days.
Evaporation of an aliquot gave a tan solid m.p 87-88°C. 13c NMR (75 MHz, CDC13, ppm) 161.8, 146.8, 145.0, 143.8, 142.1, 51.0, 28.5.
EXAMPLE 9
rac-2-tert-Butyl-carboxamide-piperazine 10
Figure imgf000037_0001
Materials
Pyrazine-2-tert-butylcarboxamide 9 2.4 kg (13.4 mol) in 1- Propanol solution 12 L 20% Pd(OH)2/C 16 wt.% water 144 g
The pyrazine-2-tert-butylcarboxamide 9/1 -propanol solution was placed into the 5 gal autoclave. The catalyst was added and the mixture was hydrogenated at 65°C at 40 psi (3 atm) of H2.
After 24 h the reaction had taken up the theoretical amount of hydrogen and GC indicated <1 % of 9. The mixture was cooled, purged with N2 and the catalyst was removed by filtration through Solka Floe. The catalyst was washed with 2 L of warm 1 -propanol.
It was found that the use of warm 1 -propanol during washing of the filter cake improved filtration and lowered the losses of product on the filter cake.
The reaction was monitored by GC: 30 m Megabore column, from 100°C to 160°C at 10°C/min, hold 5 min, then at 10°C/min to 250°C, retention times: 9 = 7.0 min, 10 = 9.4 min. The reaction could also be monitored by TLC with EtOAc/MeOH (50:50) as solvent and Ninhydrin as developing agent.
Evaporation of an aliquot indicated that the yield over amidation and hydrogenation is 88% and that the concentration of 10 is 133 g/L.
Evaporation of an aliquot gave 10 as a white solid m.p. 150- 151°C; 13C NMR (75 MHz, D2θ, ppm) 173.5, 59.8, 52.0, 48.7, 45.0, 44.8, 28.7.
EXAMPLE 10
(S)-2-tert-Butyl-carboxamide-piperazine bis (S)-Camphorsulfonic acid salt (S)-ll
H H
,N. 2 (+)-CSA ^ NIM * 2 (+)-CSA
N" "CONHt-Bu N CONHt-Bu
H H
10 11
Materials rac-2-tert-Butyl-carboxamide-piperazine 10 4.10 kg (22.12 mol) in 1 -Propanol Solution in 25.5 Kg solvent
(S)-(+)-10-Camphorsulfonic acid 10.0 Kg (43.2 mol)
1 -Propanol 12 L
Acetonitrile 39 L Water 2.4 L The solution of amine 10 in 1 -propanol was charged to a 100 L flask with an attached batch concentrator. The solution was concentrated at 10 mbar and a temperature < 25°C to a volume of ca 12 L.
At this point the product had precipitated from the solution, but went back into a solution when the mixture was heated to 50°C.
Analysis of a homogeneous aliquot indicated that the concentration of 10 was 341 g/L The concentration was determined by HPLC: 25 cm Dupont Zorbax RXC8 column with 1.5 mL/min flow and detection at 210 nm, isocratic (98/2) CH3CN/0.1 % aqueous H3PO4. Retention time of 10:2.5 min.
Acetonitrile (39 L) and water (2.4 L) were added to give a clear, slightly brown solution.
Determination of the water content by KF titration and CH3CN/I -propanol ratio by 1H NMR integration showed that the CH3CN/1 -propanol/H2θ ratio was 26/8/1.6. The concentration in the solution was 72.2 g/L.
The (S)-lO-camphorsulfonic acid was charged over 30 min in 4 portions at 20°C. The temperature rose to 40°C after the CSA was added. After a few minutes a thick white precipitate formed. The white slurry was heated to 76°C to dissolve all the solids, the slightly brown solution was then allowed to cool to 21 °C over 8 h.
The product precipitated at 62°C. The product was filtered without aging at 21 °C, and the filter cake was washed with 5 L of the CH3CN/l-propanol/H2θ 26/8/1.6 solvent mixture. It was dried at 35°C in the vacuum oven with N2 bleed to give 5.6 Kg (39%) of 11 as a white crystalline solid m.p. 288-290°C (with decomp.) [α]D25 = 18.9° (c = 0.37, H2θ). 3C NMR (75 MHz, D2O, ppm) 222.0, 164.0, 59.3, 54.9, 53.3, 49.0, 48.1, 43.6, 43.5, 43.1 , 40.6, 40.4, 28.5, 27.2, 25.4, 19.9, 19.8.
The ee of the material was 95% according to the following chiral HPLC assay: an aliquot of 11 (33 mg) was suspended in 4 mL of EtOH and 1 mL of Et3N. Boc2θ (11 mg) was added and the reaction mixture was allowed to age for 1 h. The solvent was completely removed in vacuo, and the residue was dissolved in ca. 1 mL of EtOAc and filtered through a Pasteur pipet with Siθ2, using EtOAc as eluent. The evaporated product fractions were redissolved in hexanes at ca. 1 mg/mL. The enantiomers were separated on a Daicel Chiracell AS column with a hexane/IPA (97:3) solvent system at a flow rate of 1 mL/min and detection at 228 nm. Retention times: S antipode = 7.4 min, R = 9.7 min.
EXAMPLE 11
(S)-2-tert-Butylcarboxamide-4-tert-butoxycarbonyl-piperazine 4 from salt 11
Figure imgf000040_0001
11 4
Materials
(S)-2-tert-Butyl-carboxamide-piperazine
Bis (S) - (+) - CSA salt 11, 95% ee 5.54 Kg (8.53 mol)
Di-tert-butyl dicarbonate 1.86 Kg (8.53 mol)
Et3N 5.95L (42.6 mol)
EtOH Punctilious 200 proof 55 L
EtOAc 2 L
To the (S)-CSA salt 11 in a 100 L 3-neck flask with an addition funnel under N2 was added EtOH, followed by triethylamine at 25°C. The solid dissolved readily on the addition of the Et3N. The Boc2θ was dissolved in EtOAc and charged to the addition funnel. The solution of Boc2θ in EtOAc was added at such a rate as to keep the temperature below 25 °C. The addition took 3 h. The reaction mixture was aged for 1 h after completion of the addition of the Boc2θ solution. The reaction can be monitored by HPLC: 25 cm Dupont Zorbax RXC8 column with 1 mL/min flow and detection at 228 nm, isocratic (50/50) CH3CN/O.I M KH2PO4 adjusted to pH=6.8 with NaOH. Retention time of 4 = 7.2 min. The chiral assay was carried out using the same system as in the previous step. The reaction could also be monitored by TLC with a 100% EtOAc as the solvent. (Rf=0.7)
The solution was then concentrated to ca. 10 L at an intemal temperature of <20°C in a batch-type concentrator under 10 mbar vacuum. The solvent switch was completed by slowly bleeding in 20 L of EtOAc and reconcentrating to ca 10 L. The reaction mixture was washed into an extractor with 60 L of EtOAc. The organic phase was washed with 16 L of 5% aqueous Na2Cθ3 solution, 2 X 10 L Di water and 2 X 6 L of saturated aqueous sodium chloride. The combined aqueous washes were back extracted with 20 L of EtOAc and the organic phase was washed with 2 X 3 L water and 2 X 4 L of saturated aqueous sodium chloride. The combined EtOAc extracts were concentrated under 10 mbar vacuum with an internal temperature of <20°C in a 100 L batch- type concentrator to ca. 8 L. The solvent switch to cyclohexane was achieved by slowly bleeding in ca. 20 L of cyclohexane, and reconcentrating to ca. 8 L. To the slurry was added 5 L of cyclohexane and 280 mL of EtOAc and the mixture was heated to reflux, when everything went into solution. The solution was cooled and seed (10 g) was added at 58°C. The slurry was cooled to 22°C in 4 h and the product was isolated by filtration after a 1 h age at 22°C. The filter cake was washed with 1.8 L of cyclohexane and dried in the vacuum oven at 35°C under N2 bleed to give 1.87 Kg (77%, >99.9 area % by HPLC, R-isomer below level of detection) of 4 as a slightly tan powder. [α]D^ = 22.0° (c = 0.20, MeOH), m.p. 107°C; 3C NMR (75 MHz, CDCI3, ppm) 170.1, 154.5, 79.8, 58.7, 50.6, 46.6, 43.6, 43.4, 28.6, 28.3. While the foregoing specification teaches the principles of the present invention, with examples provided for the purpose of illustration, it will be understood that the practice of the invention encompasses all of the usual variations, adaptations, modifications, deletions or additions of procedures and protocols described herein, as come within the scope of the following claims and it equivalents.

Claims

WHAT IS CLAIMED IS:
1. A process of synthesizing the epoxide of Formula I,
Figure imgf000043_0001
comprising the steps of:
(a) contacting one equivalent of the allyl acetonide of Formula π,
Figure imgf000043_0002
with about one to two equivalents of a halogenating agent in solvent mixed with aqueous weak base, at a temperature range of between about -40°C and about 100°C, to form the halohydrin of Formula HI, and
Figure imgf000043_0003
m (b) adding base in solvent or solvents to elicit formation of the epoxide of Formula I.
2. A process of synthesizing the epoxide of Formula I,
Figure imgf000044_0001
comprising the steps of:
(a) reacting one equivalent of the acetonide
Figure imgf000044_0002
with about one equivalent of allylhalide in strong base, to give the allyl acetonide of Formula π,
Figure imgf000044_0003
(b) mixing thereto about one to two equivalents of a halogenating agent in solvent mixed with aqueous weak base, at a temperature range of between about -40°C and about 100°C, to form the halohydrin of Formula HI, and
Figure imgf000045_0001
(c) adding base in solvent or solvents to elicit formation of the epoxide of Formula I.
The process of Claim 1 , for synthesizing the epoxide of Formula I,
Figure imgf000045_0002
comprising the steps of:
(a) contacting one equivalent of the allyl acetonide of Formula π,
Figure imgf000045_0003
with about one to two equivalents of a halogenating agent, in solvent mixed with aqueous weak base, at a temperamre range of between about -40°C and about 100°C, to form the halohydrin of Formula III,
Figure imgf000046_0001
said halogenating agent selected from the group consisting of N-iodosuccinimide, N-bromosuccinimide or N- chlorosuccinimide, the last two of which may be combined with an iodide salt, said solvent selected from the group consisting of dichloromethane, EPAC, EtOAc, DME, and MTBE, said weak base selected from basic alumina or sodium bicarbonate, and
(b) adding base in water to elicit formation of the epoxide of Formula I, said base selected from the group consisting of lithium hydroxide, sodium hydroxide, potassium hydroxide, tetralkylammonium hydroxide; any Cl-4 alkoxide of lithium, sodium or potassium; and DIEA.
4. The process of Claim 2, for synthesizing the epoxide of Formula I,
Figure imgf000046_0002
, I comprising the steps of:
(a) reacting one equivalent of the acetonide
Figure imgf000047_0001
with about one equivalent of allylhalide in strong base, said allyl halide selected from allyl chloride, allyl bromide and allyl iodide, to give the allyl acetonide of Formula π,
Figure imgf000047_0002
(b) mixing thereto about one to two equivalents of a halogenating agent in solvent mixed with aqueous weak base, at a temperature range of between about -40°C and about 100°C, to form the halohydrin of Formula III,
Figure imgf000047_0003
m said halogenating agent selected from the group consisting of N-iodosuccinimide, N-bromosuccinimide or N- chlorosuccinimide, the last two of which may be combined with an iodide salt, said solvent selected from the group consisting of dichloromethane, IPAC, EtOAc, DME, and MTBE, said weak base selected from basic alumina or sodium bicarbonate, and
(c) adding base in water to elicit formation of the epoxide of Formula I, said base selected from the group consisting of lithium hydroxide, sodium hydroxide, potassium hydroxide, tetralkylammonium hydroxide; any Cl-4 alkoxide of lithium, sodium or potassium; and DIEA.
5. A process of synthesizing the epoxide of Formula I,
Figure imgf000048_0001
comprising the steps of :
(a) contacting one equivalent of the allyl acetonide of Formula π,
Figure imgf000048_0002
said allyl acetonide dissolved in isopropyl acetate, with about one to two equivalents of N-iodosuccinimide in about 0.5 M aqueous sodium bicarbonate, at room temperamre, to form the iodohydrin of Formula HI, and
Figure imgf000049_0001
(b) adding alkali hydoxide in water to elicit formation of the epoxide of Formula I.
6. A process of synthesizing the epoxide of Formula I,
Figure imgf000049_0002
comprising the steps of:
(a) reacting one equivalent of the acetonide
Figure imgf000049_0003
said acetonide dissolved in ethereal solvent, with about one equivalent of allylbromide and about one equivalent of about 1.0-2.0 M lithiumhexamethyldisilazide (in ethereal solvent), to give the allyl acetonide of Formula H,
Figure imgf000050_0001
(b) mixing thereto about one to two equivalents of N- iodosuccinimide in about 0.5 M aqueous sodium bicarbonate, at room temperamre, to form the iodohydrin of Formula IH, and
Figure imgf000050_0002
(c) adding alkali hydroxide in water to elicit formation of the epoxide of Formula I.
The compound
Figure imgf000051_0001
10
8. The compound
Figure imgf000051_0002
The compound
20
Figure imgf000051_0003
10. The compound
X = halo
Figure imgf000051_0004
11. The compound
Figure imgf000052_0001
10
15
20
25
30
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US5981759A (en) * 1997-06-20 1999-11-09 Merck & Co., Inc. Process for indinavir intermediate
US9205125B2 (en) 2005-11-09 2015-12-08 Onyx Therapeutics, Inc. Compounds for enzyme inhibition
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US9657058B2 (en) 2006-06-19 2017-05-23 Onyx Therapeutics, Inc. Compounds for enzyme inhibition
US8921324B2 (en) 2007-10-04 2014-12-30 Onyx Therapeutics, Inc. Crystalline peptide epoxy ketone protease inhibitors and the synthesis of amino acid keto-epoxides
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US9878047B2 (en) 2012-07-09 2018-01-30 Onyx Therapeutics, Inc. Prodrugs of peptide epoxy ketone protease inhibitors
US9315542B2 (en) 2012-07-09 2016-04-19 Onyx Therapeutics, Inc. Prodrugs of peptide epoxy ketone protease inhibitors
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US10682419B2 (en) 2012-07-09 2020-06-16 Onyx Therapeutics, Inc. Prodrugs of peptide epoxy ketone protease inhibitors

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ATE210662T1 (en) 2001-12-15
PT748319E (en) 2002-05-31
RU2137769C1 (en) 1999-09-20
AU1882895A (en) 1995-09-18
UA45968C2 (en) 2002-05-15
EP0748319A1 (en) 1996-12-18
HUT75611A (en) 1997-05-28
CA2183976A1 (en) 1995-09-08
MX9603871A (en) 1997-07-31
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FI963452A (en) 1996-09-03
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JP3871705B2 (en) 2007-01-24
NZ281866A (en) 1998-05-27
CZ291816B6 (en) 2003-06-18
AU690231B2 (en) 1998-04-23
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