PROCESS TO MAKE HIV PROTEASE INHIBITOR FROM 2(S)-4-PICOLYL-2-PIPERAZINE-t-BUTYLCARBOXAMIDE

Abstract: A process for making a clinically efficacious HIV protease inhibitor eliminates one step in its synthesis, by an alternative convergent synthesis using 2(S)-4-picolyl-2-piperazine-t-butylcarboxamide as an intermediate; as indicated above.

Description: TITLE OF THE INVENTION PROCESS TO MAKE HIV PROTEASE INHIBITOR FROM (2S)-4- PICOLYL-2-PIPERAZINE-t-BUTYLCARBOXAMIDE BACKGROUND OF THE INVENTION The present application is related to Merck 18996, U.S.S.N. 08/059,038, filed May 7, 1993, and Merck cases 19045, 19046IA, MRL 94/005, 19182, MRL 94/143, 191 14 and 191 15. 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 certain oligopeptide analogs, such as Compound J in the Examples below. 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). These compounds are also useful for inhibiting renin and other proteases. The invention described herein concerns a process to prepare the HIV protease inhibitor J from the 4-picolyl piperazine carboxamide 1 via a two-step procedure. The piperazine 1 is condensed with epoxide 2 to afford the coupled product 3. Removal of the acetonide protecting group of 3 directly affords the HIV-1 protease inhibitor J. Deblock 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 ΓJOI gene in one open reading frame [Ratner, L. et al., Nature, 313, 277 (1985)]. Amino acid sequence homology provides evidence that the p_ρj 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 certain oligopeptide analogs that can be made from the novel intermediates and processes of this invention, are inhibitors of HIV protease, and are disclosed in EPO 541,168, which published on May 12, 1993. See, for example, Compound J therein. Previously, the synthesis of Compound J and related compounds was accomplished via a 12-step procedure. This procedure is illustrated in EPO 541 ,168. In prior methods, the HIV protease inhibitor J was prepared by coupling of the epoxide intermediate 2 with the Boc-protected piperazine carboxamide 4 to afford the Boc -protected coupled intermediate 5. Deblocking of 5 then afforded a penultimate Compound 6 which was subjected to picolylation to afford J. The disadvantage with this route is that three chemical steps are necessary to convert the epoxide 2 to J. Thus, after deblocking, a separate picolylation step is necessary to effect conversion to J. Since the more reactive 4-position of the piperazine carboxamide must be protected prior to coupling, the most efficient blocking method for the chiral 2- piperazine-t-butylcarboxamide would be the incorporation of the 3- picolyl moiety at this point. However, it was unexpected that the reaction of piperazine 1 with epoxide 2 would be efficient, since piperazine 1 contains three basic amine functions capable of attacking the epoxide 2. The Boc-protected piperazine 4, however, contains only one basic amine function, and thus it was expected that the coupling of 2 and 4 would be straightforward. The process of the present invention eliminates one step, an advantage for simplifying the already complex synthesis of Compound J. The present process is shorter and highly efficient. BRIEF DESCRIPTION OF THE INVENTION The present invention provides an alternative convergent synthesis that eliminates an extra synthetic step and produces higher yields. The product compound J is useful as an inhibitor of HIV protease, renin and other proteases. DETAILED DESCRIPTION OF THE INVENTION The present invention provides a process for synthesis of a compound of the structure comprising the steps of: (a) heating for at least one hour a mixture of one equivalent of with about one equivalent of at a temperature range between about 25°C and about 150°C, said mixture optionally containing suitable solvent; (b) deblocking by treatment with acid, and (c) neutralizing the acid, to give the desired compound. In one embodiment, the present invention provides a process for synthesis of a compound of the structure comprising the steps of: (a) heating for at least one hour a mixture of one equivalent of t-BuNH^^O with about one equivalent of at a temperature range between about 65°C and about 85°C, said mixture optionally containing as solvent methanol or isopropanol or mixture thereof; (b) cooling the mixture to about 0°C; (c) deblocking with gaseous HCl; and (d) neutralizing with NaOH, to give the desired compound. This invention also covers the compound t-BuNH^O The coupling can be carried out by heating the piperazine 1 and the epoxide 2 neat or in a variety of solvents. The coupling reaction can be carried out at temperatures ranging from 25 °C to 150°C, preferred is the range of 50°C to 120°C with the most preferred temperatures being 65°C to 85°C. Desired solvents for this step include esters such as ethyl acetate, isopropyl acetate, n-butyl acetate; acetonitrile; alcohols such as methanol, ethanol, n-propanol, n-butanol, t-butanol, t-amyl alcohol and isopropanol; hydrocarbons such as cyclohexane and toluene; ethers such as THF and DME; and formamides such as DMF. Preferred solvents are alcohols with the most preferred being methanol and isopropanol. The deblocking of intermediates 3 to J is accomplished by standard methods, i.e., treatment with strong acids such as gaseous HCl in alcoholic solvents or aqueous HCl, with gaseous HCl being the most preferred method. The products of this invention 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 HIV 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. The end product HIV protease inhibitor compound J has the structure or pharmaceutically acceptable salts or hydrates thereof. Compound J is named N-(2(R)-hydroxy-l (S)-indanyl)-2(R)-phenylmethyl-4(S)-hydroxy-5-( l (4-(3-pyridylmethyi)-2(S)-N'-(t-butylcarboxamido)-piperazinyl))- pentaneamide; [ 1 S-[ 1 α[αS*,γR*,δ(R*)l,2α]]-N-(2.3-dihydro-2-hydrox y- 1 H-inden- 1 - yl)-2-[[( l , l -dimethylethyl)amino]carbonyl]-γ-hydroxy- -(phenyI- methyl)-4-(3-pyridinylmethyl)-2-piperazinepentaneadmide; or N-(l(S)-2,3-dihydro-2(R)-hydroxy-l H-indenyl)-4(S)-hydroxy-2(R)- phenylmethyl-5-[4-(3-pyridylmethyl)-2(S)-t-butylcarbamoyl)- piperazinyljpentaneamide. HIV protease inhibitor compounds that can be made from the 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 therapeutical ly-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) 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. Representative experimental procedures utilizing the novel process are detailed below. These procedures are exemplary only and are not limitations on the novel process of this invention. EXAMPLE 1 Pyrazine-2-tert-butyl carboxamide 8 8 2-Pyrazinecarboxylic acid (7) 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 7 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 HCl that was formed remained largely in solution. A precipitate was present which is probably the HCL 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 7 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 7 = 10.7 min, amide 8 = 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% NaHC03 and 2 X 2 L of saturated aq. NaCl. 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 8 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 1 H NMR (<1 %). The internal 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. J 3c NMR (75 MHz, CDCI3, ppm) 161.8, 146.8,145.0, 143.8, 142.1 , 51.0, 28.5. EXAMPLE 2 rac-2-tert-Butyl-carboxamide-piperazine 9 Materials Pyrazine-2-tert-butylcarboxamide 8 2.4 kg ( 13.4 mol ) in I - Propanol solution 12 L 20% Pd(OH)2/C 16 wt.% water 144 g The pyrazine-2-tert-butylcarboxamide 8/1 -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 8. 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: 8 = 7.0 min, 9 = 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 9 is 133g/L. Evaporation of an aliquot gave 9 as a white solid m.p. 150- 15 TC; !3c NMR (75 MHz, D2θ, ppm) 173.5, 59.8, 52.0, 48.7, 45.0, 44.8, 28.7. EXAMPLE 3 (S)-2-tert -Butyl-carboxamide-piperazine bis (S)-Camphorsulfonic acid salt (S)-1100 10 Materials rac-2-tert-Butyl-carboxamide-piperazine 9 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 9 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 9 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 9:2.5 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 ^ H NMR integration showed that the CH3CN/l -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 dπed at 35°C in the vacuum oven with N2 bleed to give 5.6 Kg (399. ) of 10 as a white crystalline solid m.p 288-290°C (with decomp.) |cc]D 25 = 1 . ^ (c = 0.37, H20). 1 C 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 10 (33 mg) was suspended in 4 mL of EtOH and 1 mL of Et3N. Boc2θ (1 1 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 4 Synthesis of (S)-4-(3-Picolyl .-2-tert-butylcarboxamide piperazine (1 ) 2(S)-tert-Butylcarboxamide piperazine Bis 7.15 g (1 1 mmol) (+)CSA salt (10) 3-Pyridinecarboxaldehyde 1.04 mL ( 1 1 mmol) Titanium (IV) isopropoxide 4 mL ( 13.7 mmol) Sodium cyanoborohydride 0.47 g (7.5 mmol) A slurry of the 2(S)-tert-butylcarboxamide piperazine Bis (+)-CSA salt in 30 mL of 1 -propanol was washed twice with 25% NaOH solution and twice with saturated aqueous sodium sulfate. The homogeneous 1 -propanol phase is concentrated at reduced pressure to give 1.30 g (94%) of 2(S)-tert-butylcarboxamide piperazine as a white solid. The crude 2(S)-tert-butylcarboxamide piperazine is suspended in 20 mL of toluene and the aldehyde is added followed by the titanium (IV) isopropoxide. The reaction turns dark and after stirring at 20°C for 2 h, the sodium cyanoborohydride is added. After 18 h of stirring, 50 mL of EtOH is added and the precipitate is removed by filtration and washed with EtOAc. The combined organic phases are evaporated to give a yellow oil (2.3 g), which is chromatographed on Siθ2 (EtOAc/MeOH 50/50). Evaporation of product containing fractions gives 1.20 g of 2(S)-tert-butylcarboxamide-4-(3-pyridylmethyl)- piperazine (40%). EXAMPLE 5 N-[2(R)-hydroxy-l(S)-indanyl]-5-[(2(S)-tertiary-butylaminocarbonyl)- 4-(3-pyridylmethyl)piperazino]-4(S)-hydroxy-2(R)-phenylmethyI- pentanamide monohydrate J*H2θ) Deblock (2S)-4-(3-Picolyl)-2-tert-butylcarboxamide- 7.9 g (28.5 mmol) piperazine (1) [3aS-[3[2S*,3(R*)],3aα,8aα]]-3,3a,8,8a- 10.0 g (26.5 mmol) tetrahydro-2,2-dimethyl3-[3-(2-oxiranyl)- - 1 -oxo-2-(phenylmethyl)propyl]-2H-indeno- [ l ,2-d]-oxazole (2) tert-amyl alcohol 88 mL (2-methyl-2-butanol) A mixture of 1 (7.9 g, 28.5 mmol) and the epoxide 2 ( 10 g, 26.5 mmol) in isopropyl alcohol (88 mL) was heated to the reflux point 82°C and held for 72 h to complete the formation of 3. The solution of 3 is cooled to 0°C and treated with anhydrous HCl gas and the mixture is aged between 0-5 °C for 3 h. The hydrolysis was quenched by the slow addition of 50% NaOH to adjust the pH of the mixture to 12 while keeping the temperature less than 25°C. The mixture is then partitioned with isopropyl acetate (200 mL) and water (50 mL). The mixture was agitated and the layers were separated and the aqueous phase was reextracted with isopropyl acetate (50 mL). The isopropyl acetate solution of J is concentrated to about 100 g/L and water is added to saturate the hot isopropyl acetate solution. The mixture was seeded and cooled to afford J ( 15.1 g, 90%) from epoxide 2. EXAMPLE 6 Conversion of Indene Oxide to Cis-l-Amino-2-Indanol Materials Mol. Wt. Grams or ml Millimoles Indene oxide 132 1 ml 8.33 Acetonitrile 41 10 ml 244 Water 18 2.15 ml 1 19.4 Cone. H2SO4 98 0.92 ml 16.6 5N KOH 57 3.0 ml 15 Dowex 50 x 4 (H+ ) 1.9 meq/ml 15 ml wet resin 28.5 meq Methanol 17 50 ml 50 To one ml of indene oxide (8.33 mmoles) dissolved in 10 ml acetonitrile was added 0.15 ml water (8.33 mmoles). The mixture was cooled to 0-5° in an ice bath. Concentrated sulfuric acid was added dropwise while maintaining the batch temperature below 10°. When all the acid was added and the temperature was allowed to rise to 20-25°. The clear solution was aged for 30 minutes. To this mixture was added 2 ml of water and the solution heated for 30 minutes. When the methyl oxazoline was completely converted to cis amino indanol the reaction mixture was cooled to room temperature. A solution of 5N KOH (3 ml, 15 mmoles) was added. This is 90% of theory for the sulfuric acid. The solution remained acid to litmus. If the pH rises above, 2 re-acylation occurs and the yield of amino indanol is reduced. The white solid (K2SO4) was removed by filtration. Dowex resin 15 ml (wet with acetonitrile) was added with stirring. The stirred resin was aged for 1 minutes and sampled for LC (dilx 50). When the LC peak for amino indanol disappeared, the resin was collected by filtration, washed with acetonitrile and then with methanol. The wet resin was treated with a solution of 50 ml IN NH3 in methanol and the slurry stirred at room temperature for 30 minutes. The resin was again collected by filtration and the methanol/NH3 saved. Another charge of IN NH3/MeOH (20 ml) was added and the resin re- slurried. After removal of the resin the methanol/NH3 solutions of the amino indanol were combined and concentrated to remove the NH3. Analysis of the final MeOH solution shows 1.0 g (81 % yield) cis-1 - amino-2-indanol ready for the tartaric acid resolving agent. EXAMPLE 7 Preparation of racemic indene oxide Indene (95%, 122 mL) was dissolved in methanol (812 mL) and acetonitrile (348 mL), then filtered. The filtrate was diluted with 0.05 M sodium dibasic phosphate (1 16 mL), then adjusted to pH 10.5 with 1 M aqueous sodium hydroxide. Aqueous hydrogen peroxide (35%, 105 mL) was diluted with water (53 mL) and added over 3 h, while maintaining the temperature at 25 °C and the internal pH at 10.5 with 1M aqueous sodium hydroxide (120 mL total). After 6 h, 1 M aqueous sodium metabisulfite was added (26 mL), while maintaining the pH above 8.3 by addition of 1 M aqueous NaOH (39 mL). Water (700 mL) was added and the mixture extracted with methylene chloride (580 mL and 300 mL). The combined organic extracts containing indene oxide ( 1 17 g) were concentrated to a volume of 600 mL. EXAMPLE 8 Preparation of (I S. 2R . -indene oxide The substrate, (I S, 2R)-indene oxide is prepared according to the method described by D.J. O'Donnell, et al., J. Organic Chemistry, 43, 4540 (1978), herein incorporated by reference for these purposes. EXAMPLE 9 Preparation of cis-l -amino-2-indanol Indene oxide (1 17 g) diluted to a total volume of 600 mL in methylene chloride was diluted with acetonitrile (600 mL) and cooled to -20°C. Methanesulf onic acid (1 14 mL) was then added. The mixture was warmed to 25°C and aged for 2 h. Water (600 mL) was added and the mixture heated at 45°C for 5 h. The organic phase was separated and the aqueous phase further heated at reflux for 4 h with concentration to approximately 200 g/L. The solution was adjusted to pH 12.5 with 50% aqueous sodium hydroxide, and then cooled to 5°C and filtered, dried in vacuo, to provide cis l -amino-2-indanol. EXAMPLE 10 Preparation of lS-amino-2R -indanol (1,S, 2R)-indene oxide (85% ee,) (250 g, 0.185 mole) was dissolved in chlorobenzene (300 mL) and heptanes (1200 mL) and slowly added to a solution of methanesulfonic acid (250 mL, 0.375 mole) in acetonitrile (1250 mL) at a temperature of less than about -10°C. The reaction mixture was warmed to 22°C and aged for 1.0 h. Water was added to the mixture and concentrated by distillation until an internal temperature of 100°C was achieved. The reaction mixture was heated at 100°C for 2-3 h then cooled to room temperature. Chloro- benzene (1000 mL) was added, the mixture stirred, the organic phase separated. The remaining aqueous phase containing lS-amino, 2R- indanol (85% ee, 165 g, 60%) was adjusted to pH 12 with 50% aqueous sodium hydroxide and the product collected by filtration and dried in vacuo at 40°C to yield lS-amino, 2R-indanol (85% ee, 160 g). EXAMPLE 1 1 Preparation of lS-amino-2R-indanol (IS, 2R)-indene oxide (85% ee,) (250 g, 0.185 mole) was dissolved in chlorobenzene (300 mL) and heptanes (1200 mL) and slowly added to a solution of fuming sulfuric acid (21 % SO3, 184 mL) in acetonitrile (1250 mL) at a temperature of less than about -10°C. The reaction mixture was warmed to 22°C and aged for 1.0 h. Water was added to the rnixture and concentrated by distillation until an internal temperature of 100°C was achieved. The reaction mixture was heated at 100°C for 2-3 h, then cooled to room temperature. Chloro¬ benzene (1000 mL) was added, the mixture stirred, the organic phase separated. The remaining aqueous phase containing l S-amino, 2R- indanol (85% ee, 205 g, 74%) was diluted with an equal volume of acetonitrile. The pH was adjusted to 12.5 with 50% aqueous sodium hydroxide and the organic phase separated. The remaining aqueous phase was extracted with additional acetonitrile. The combined acetonitrile extracts were concentrated in vacuo to provide l S-amino, 2R -indanol (85% ee, 205 g). Alternatively, the remaining aqueous phase containing 1 S- amino-2R-indanol (85% ee, 205 g, 74%) was diluted with an equal volume of butanol and the pH was adjusted to 12.5 with 50% aqueous sodium hydroxide and the organic phase separated. The organic phase was washed with chlorobenzene. L-tartaric acid was added and water was removed by distillation to crystallize the tartaric acid salt of the amino-indanol. EXAMPLE 12 Use of benzonitrile Indene oxide (5 g) was dissolved in benzonitrile (50 mL) at 25°C and sulfuric acid (98%, 2.25 mL) was added. The mixmre was diluted with 5M aqueous sodium hydroxide solution (50 mL) and extracted with methylene chloride. The organic extracts were concentrated in vacuo to give 5.03 g of oxazoline. EX AMPLE 13 Resolution of cis-l -Amino-2-indanol Cis-l-Amino-2-indanol (100 g) was dissolved in methanol (1500 mL) and a solution of L-tartaric acid (110 g) in methanol (1500 mL) was added. The mixture was heated to 60°C and cooled to 20°C, filtered and dried in vacuo to give l S-amino, 2R -indanol L-tartaric acid salt as a methanol solvate (88 g). EXAMPLE 14 Preparation of lS-Amino--2R -indanol lS-Amino, 2R-indanol L-tartaric acid salt methanol solvate (88 g) was dissolved in water (1 0 mL) and heated to 55-60°C. The solution was clarified by filtration and the pH adjusted to 12.5 with 50% aqueous sodium hydroxide. The mixture was cooled to 0-5°C over 2 h, then aged at that temperature for 1 h, filtered, washed with cold water and dried in vacuo at 40°C to yield l S-amino. 2R-indanol ( 100% ee, 99% pure, 37 g). EXAMPLE 15 Conversion of 1.2 indanol to cis-l -amino-2-indanol Materials Mol Wt Grams or ml Millimoles 1 ,2 indane diol 150 300 mg. 2 acetonitrile 41 2.5 ml 47.3 water 18 0.04 ml 2 sulfuric acid 98 0.22 ml 4 5 N KOH 57 1.6 ml 8.0 Dowex 10 ml 50 x 4 (H+) methanol (1 m NH3) 30 ml To 300 mg indane diol dissolved in 3 ml of acetonitrile containing 0.04 ml water was added dropwise at 0-10°C a volume of 0.22 ml of concentrated H2SO4. After the addition was complete the ice bath was removed and the batch warmed to room temperature. After a 30 minute age the clear solution was sampled for Ic assay (dilx 500). When all the glycol was consumed, the solution was treated further with water and heated to reflux on a steam bath to hydrolyze the oxazoline. When Ic analysis showed hydrolysis complete, 1.6 ml 5 N KOH was added to neutralize the sulfuric acid. Potassium sulfate was filtered from the solution. The filtrate was assayed for cis amino indanol and contained 196 mg (66% of theory, which is also 75% corrected for unreacted starting material). The solution was passed over 10 ml of Dowex 50 x 4 (H+ ). The column spents were checked for product. All the amino indanol was adsorbed. After washing the resin with methanol, the product was eluted with a solution 1 M in NH3 (dry). The ammoniacal methanol was concentrated to remove the NH3 and the final solution of amino-indanol ready for resolution was assayed. (175 mg, or 59% of theory when uncorrected for unreacted glycol). EX AMPLE 16 Preparation of Indanol Reactants Compounds (±)-trans-2-bromo-l -indanol were prepared by methods of S. M.Sutter et al., J. Am. Chem. Soc, 62, 3473 ( 1940); and D. R. Dalton et al., J. C. S. Chem. Commun., 591 (1966). Compounds (+)-trans-2-bromo- 1 -indanol and cis- and trans- 1 ,2-indandiols were prepared by the methods of M. Imuta et al., J. Org. Chem., 43, 4540 (1978). EXAMPLE 17 Preparation of cis- 1 -amino-2-indanol from trans -2-bromo- 1 -indanol 7 α/ι_ * -2-bromo-l -indanol (10 g, 46.9 mmole diluted in 100 mL of acetonitrile containing 0.8 mL water) was cooled to -5°C and concentrated sulfuric acid (5.2 mL) was added. The mixture was aged for 1 h, then 5 M aqueous potassium hydroxide was added to adjust the pH to 11. The reaction mixture was filtered, removing the potassium sulfate salts. The aqueous acetonitrile filtrate was adjusted to pH less than 2 with sulfuric acid and heated to 80-100°C, removing acetonitrile by distillation to provide an aqueous solution of c _- l -amino-indanol. The solution was concentrated to a volume of 20 mL, then adjusted to pH 12.5 with potassium hydroxide. The product crystallizes, was filtered and dried in vacuo to provide cΛ_- l-amino-2-indanol (4.25 g). EXAMPLE 18 Preparation of c/_?-l S-amino-2R-indanol from <_ ._>-(! S.2R)-indandiol C_.s-(lS,2R)-indandiol (1 g) was dissolved in acetonitrile (10 mL), cooled to 0°C and concentrated sulfuric acid (1.0 mL) was added. The mixture was aged for 40 minutes with warming to 20°C. Water (0.8 mL) was added and the mixture was heated to reflux. Aqueous 5 M potassium hydroxide (1.6 mL) was added to adjust the pH to more than 1 1 and the resulting solid (potassium sulfate) removed by filtration to provide an aqueous solution of the c _-lS-amino-2R-indanol (0.79 g, 66% yield). EXAMPLE 19 Preparation of cis - 1 -amino-2-indanol from trans - 1.2-indandiol Trans- 1 ,2-indandiol (1.5 g) was dissolved in acetonitrile (25 mL) cooled to 0°C, and concentrated sulfuric acid (1.1 mL) was added. The mixture was gradually warmed to 20°C and aged to 3 hours. Water (2 mL) was added and the mixture heated to reflux. Concentrated aqueous sodium hydroxide was added to adjust the pH to 12. The resulting solid was removed by filtration to provide an aqueous acetonitrile solution of cis- l-amino-2-indanol (1.02 g, 63% yield). EXAMPLE 20 Preparation of cis- 1 -amino-2-indanol from c/.τ- 1 .2-indandiol Cis- 1 ,2-indandiol (1.0 g) was dissolved in acetonitrile (20 mL), cooled to -40°C, and fuming sulfuric acid (21 % SO3, 0.8 mL) was added. The mixture was aged for 1 hour with gradual warming to 0°C. Water was added and the mixture heated to 80°C for 1 hour to provide an aqueous solution of c s-l -amino-2-indanol. EX AMPLE 21 Preparation of Amide 14 [149.19] [281.35] [321.42] (-)-c _-l -aminoindan-2-ol (11) 900 g 6.02 mol (99.7 wgt. %, 99.9 area %, >99.5 % ee) sodium carbonate monohydrate 760 g 6.13 mol diethoxymethane (DEM) 56.3 L 3-phenylpropionyl chloride (13) 1.05 kg 6.23 mol methanesulfonic acid (MSA) 18.6 g 0.19 mol 2-methoxypropene (95% by GC) 1.28 L 13.3 mol 5% aqueous NaHC03 10.8 L water 26.2 L A slurry mixture consisting of (-)-c/s- l -aminoindan-2-ol (11 , 900 g, 6.02 mol) in 40 L of DEM and aqueous sodium carbonate solution (760 g, 6.13 mol, of Na2Cθ3»H2θ in 6.4 L of water) in a 100 L reactor with four inlets, equipped with a thermocouple probe, mechanical stirrer, and a nitrogen inlet adapter and bubbler, was heated to 46-47°C and aged for 15 minutes. The reaction mixture was heated to 46-47°C and aged for 15 minutes to insure dissolution of the solids. The aqueous phase had a pH of 1 1.5. Neat 3-phenylpropionyl chloride 13 (1.05 kg, 6.23 mol) was added over 2 h between 47°C to 59°C. The internal temperature increased from 47 °C to 59°C during the addition of 13; the hydroxyamide 12 crystallized out of solution during the acid chloride addition. After the addition was complete, the reaction mixture was aged at 59°C for 0.5 h and then warmed to 72°C to insure dissolution of the solids. The temperature was increased to 72°C to dissolve the hydroxyamide so that a homogeneous sample can be obtained for HPLC assay and to simplify the phase cuts. Progress of the reaction was monitored by HPLC analysis: 60:40 Acetonitrile/5.0 mM of each KH2PO4 and K2HPO4. Approximate retention times: retention time (min.) identity 4.1 hydroxy amide 12 6.3 cis-aminoindanol 11 12.5 ester amide by product After complete acid chloride addition and 0.5 h age at 72°C, the HPLC assay of the reaction mixture showed ~ 0.6 area % of 11, - 0.2 area % of ester amide by product and 98.7 area % of hydroxyamide. The hydroxy amide 12 was not efficiently rejected in the isolation of acetonide 14. The aqueous phase was separated and the organic phase was washed twice with 4.5 L of water. The washed organic phase was concentrated and dried via atmospheric azeotropic distillation. The initial volume of ~ 40 L was concentrated to 27 L. A total of 16 L of fresh DEM was charged to the still and the batch was concentrated at 88°C to 89°C to 40 L. The dried DEM slurry of hydroxyamide 12 was treated with 1.28 L of 2-methoxypropene followed by 18.6 g of MSA at 30°C. The addition of MSA in absence of 2-methoxypropene resulted in the formation of an amine ester. This impurity reconverts to hydroxyamide 12 during the basic work up at the end of the acetonide formation. The pH of 1.0 mL sample diluted with 1.0 mL water was found to be 2.8-3.0. The resulting mixture was aged at 39°C to 40°C for 3 h. The acetonide foimation was monitored by HPLC analysis using the same conditions as described above in this example. Approximate retention times: retention time (min.) identity 4.1 hydroxy amide 12 6.9 methylene ketal impurity 9.0 acetonide 14 12.5 ester amide by product The mixture was aged at 38-40°C until 12 is < 0.4 A%. A typical HPLC area % profile is as follows: 0.4 area % of hydroxyamide 12, 96.9 area % of acetonide 14, 0.2 area % of ester amide by product, 1.1 area % of methylene ketal impurity. The reaction mixture was cooled to 24°C and quenched with 10.8 L of 5% aqueous sodium bicarbonate solution. The aqueous phase was separated and the organic phase was washed twice with 10.8 L of water. The pH of the water wash was 7.6. If the pH was too low, the acetonide group could be hydrolyzed back to give the hydroxyamide 12. The washed organic phase (34.2 L) was concentrated via atmospheric distillation at 78°C to 80°C to final volume of 3.5 L. The acetonide concentration was made ~ 525 g/L to minimize isolation losses. The hot DEM solution of 14 was allowed to cool to 57°C, seeded with 0.5 g of 14 and further cooled to 0°C and aged for 0.5 h. The batch started to crystallize out of solution between 53°C to 55°C. The product was isolated by filtration and the wet cake was washed with cold (0°C) DEM (300 mL). The washed cake was dried under vacuum (26" of Hg) at 30°C to afford 1 .74 kg of acetonide 14 (90%, >99.5 area % by HPLC). EXAMPLE 22 Preparation of Acetonide 14 from (l l »tartaric acid ) salt (-)-_/_- l -aminoindan-2-ol tartrate salt 100 g 297 mmol methanol solvate (44.3 wt. % of free base 11 ) sodium carbonate monohydrate 63.76g 514 mmol diethoxymethane (DEM) 2.83 L 3-phenylpropionyl chloride (13) 52.7 g 312 mol methanesulfonic acid (MSA) 0.95 g 9.86 mmol 2-methoxypropene (95% by GC) 63 mL 658 mmol 5% aqueous NaHCθ3 520 mL water 1.32 L A slurry mixture consisting of (-) 11 •tartrate salt methanol solvate (100 g, 44.3 g of free base, 297 mmol) in 2.0 L of (DEM) and aqueous sodium carbonate solution (63.8 g, 514 mmol, of Na2Cθ »H2θ in 316 mL of water) in a 5.0 L reactor with four inlets, equipped with a thermocouple probe, mechanical stirrer, and a nitrogen inlet adapter and bubbler, was heated to 50°C. Heating the reaction mixture to 60°C did not dissolve all the solids. Neat 3-phenylpropionyl chloride 13 (52.7 g, 312 mmol) was added over 30 min at 50°C and the mixture was aged at 50°C for 15 min. Progress of the reaction was monitored by HPLC analysis: 60:40 Acetonitrile/5.0 mM of each KH2PO4 and K2HPO4, 1.0 mL/min. Approximate retention times: retention time (min.) identity 4.1 hydroxy amide 12 6.3 cis-aminoindanol 11 12.5 ester amide by product After complete acid chloride addition and 15 min. age at 50°C, the HPLC assay of the slurry mixture showed ~ 0.1 area % of 11. After this point, the reaction mixture was heated to 75 °C. The temperature was increased to 75 °C to dissolve the hydroxyamide 12 in DEM and simplify the phase separations. The aqueous phase was separated and the organic phase was washed twice with water (250 mL). The sodium tartrate was removed in the aqueous phase. The first aqueous cut had a pH of 8.98. The pH of the two water washes were 9.1 and 8.1 , respectively. The washed organic phase was concentrated and dried via atmospheric distillation. Approximately 1.0 L of distillate was collected and 750 mL of fresh DEM was charged back to the distillation pot. The atmospheric distillation was continued until another 350 mL of distillate was collected. The solution KF was 93 mg/L. The dried DEM solution was cooled to 30°C and treated with 63 mL of 2-methoxypropene followed by 0.95 g of MSA. The pH of 1.0 mL sample diluted with 1.0 mL water is 3.2. The reaction mixture was aged at 35-42°C for 2 h. The acetonide formation was monitored by HPLC analysis using the same conditions as described above in this Example. Approximate retention times: same as above. The mixture is aged at 38-40°C until 12 is < 0.7 A%. A typical HPLC area % profile is as follows: 0.4 area % of hydroxy amide, 96.9 area % of acetonide 14, 0.2 area % of ester amide by product, 1.1 area % of methylene ketal impurity. The reaction mixture was cooled to 20°C, filtered to remove the cloudy appearance and quenched with 520 mL of 5% aqueous sodium bicarbonate solution. The aqueous phase was separated and the organic phase was washed with 500 mL of water. The pH of the water wash is 7.4. The washed organic phase (-2.0 L) was concentrated via atmospheric distillation at 78°C to 80°C to final volume of 1.0 L. The acetonide concentration in the isolation was maintained at - 525 g/L to minimize isolation losses. The hot DEM solution of 14 was allowed to cool to 50-52°C, seeded with 100 mg of product and further cooled to 5°C and aged for 20 min. The batch started to crystallize out of solution at 50°C. The product was isolated by filtration and the wet cake was washed with cold (0°C) DEM (2 X 40 mL). The washed cake was dried under vacuum (26" of Hg) at 30°C to afford 83.8 g of acetonide 14 (87.9%, >99.5 area % by HPLC). EXAMPLE 23 Preparation of Acetonide 14 (Isopropyl Acetate Solvent) (-)-c _»-l -aminoindan-2-ol (11 ) 80 g 535 mmol (98.5 wgt. %) isopropyl acetate (IPAC) 1.2 L water 560 mL 5N sodium hydroxide 1 16 mL 580 mmol 3-phenylpropionyl chloride (13) 90.8 g 539 mmol methanesulfonic acid (MSA) 1.1 mL 17.0 mmol 2-methoxypropene (95% by GC) 1 19 mL 1.24 mol 5% aqueous NaHCθ3 950 mL water 400 mL methyl cyclohexane 2.25 L A mixture of of (-)-ct l -aminoindan-2-ol 11 (80 g, 535 mmol) in 1.2 L of IPAC and 560 mL of water was treated with 5 (90.8 g, 539 mmol) while the pH maintained between 8.0-10.5 at 70-72°C with 5 N sodium hydroxide (1 16 mL, 580 mmol). Progress of the reaction was monitored by HPLC analysis: 60:40 Acetonitrile/5.0 mM of each KH2PO4 and K2HPO4. Approximate retention times: retention time (min.) identity 4.1 hydroxy amide 12 6.3 cis-aminoindanol 11 12.5 ester amide by product At the end of the reaction, the aqueous phase was separated and the organic phase was washed with water (400 mL) at 72°C-73°C. The pH of the aqueous phase and the aqueous wash was 8.1 and 7.9, respectively. The wet IPAC phase was dried via atmospheric distillation. A total of 3.0 L of IPAc was charged to lower the batch KF to < 100 mg/L. The final volume is -1.60 L. The resulting IPAC slurry of hydroxyamide 12 was treated with 2-methoxypropene ( 1 19 mL, 1.24 mol) followed by MSA (1.1 mL, 3.2 mole %) at 35°C-38°C for 4.5 h. The acetonide formation was monitored by HPLC analysis using the same conditions as described above. The mixture was aged at 38-40°C until 12 is < 0.4 area %. The reaction was filtered to remove the hazy precipitate and the filtrate was quenched into cold sodium bicarbonate solution (950 mL) over 15 min. The aqueous phase was separated and the organic phase was washed with water (400 mL). The sodium bicarbonate solution was cooled to 0°C-5°C. The pH of the aqueous phase and the aqueous wash was found to be 7.5 and 7.9, respectively. Atmospheric distillation was carried out while the solvent was switched to methylcyclohexane from IPAC. The initial volume before atmospheric concentration was 1.65 L. A total of 1.5 L of methylcyclohexane was added to complete the solvent switch to methylcyclohexane from IPAC. The batch temperature at the end of the solvent switch was 101 °C and the final batch volume was -900 mL. The batch was heated to 65°C-70°C to insure dissolution of the solids, then cooled to 55°C, seeded with the product and cooled to 0°C. The mixture was aged at 0°C for 15 min and the product was isolated by filtration and washed with cold methylcyclohexane (200 ml). The washed cake was dried under vacuum (26" of Hg) at 30°C to afford 151 g of acetonide 14 (87.5%, >99.5 area % by HPLC). EXAMPLE 24 [321.42] [120.98] [361 .49] Acetonide (14) [321.42] 200 g 0.617 mol (99.1 wt. %) Allyl Bromide [120.98] 77.6 g 53.6 mL 0.642 mol LDS (FMC 9404) 1.32 M in THF 518 mL 0.684 mol Citric acid 1192.1] 35.73 g 0.186 mol THF sieve dried 1.43 L Water 1.05 L 0.3 M H2SO4 1.18 L 6 % NaHC03 1.18 L IPAc The crystalline acetonide 14 (200 g, 0.622 mol, 99.1 wt. %) was dissolved in 1.25 L sieve dried THF (KF = 1 1 mg/L) under nitrogen atmosphere at 25°C with mechanical stirring. The resulting KF of the solution at this point was 40 mg/L. The solution was subjected to three alternating vacuum/nitrogen purge cycles to thoroughly degas the solution of dissolved oxygen. Allyl bromide was added to the THF solution. The resulting KF was 75 mg/L. Typical complete conversion (> 99.5%) has been obtained with pre-LDS solution KF levels of 200 mg/L with the 10% base excess present in this procedure. The solution was then cooled to -20°C. A THF solution of lithium hexamethyldisilazide (LDS. 1.32 M) was added to the allyl bromide/14 solution at such a rate as to maintain the reaction temperature at -20°C. The LDS addition took 30 min. The mixture was aged at -15 to -20°C and quenched when the conversion was > 99%. Analysis of the reaction was carried out by HPLC. Approximate retention times: hydroxyacetonide by product = 5.3 min, ethyl benzene = 5.6 min, acetonide 14 = 6.6 min; allyl acetonide 15 = 1 1.8 min; epi-15 = 13.3 min. After 1 h, the reaction had gone to > 99.5% conversion. The reaction was quenched by the addition of a solution of citric acid (35.7 g, 0.186 mol) in 186 mL of THF. The mixture was aged at 15°C for 30 min following the citric acid addition. The mixture was concentrated at reduced pressure (about 28" Hg) to about 30% of the initial volume while maintaining a pot temperature of 1 1-15°C and collecting 900 mL of distillate in a dry ice- cooled trap. The solvent was then switched using a total of 2.7 L of isopropyl acetate (IPAc) while continuing the reduced pressure distillation. The solvent switch was stopped when < 1 mole % THF remained by *H NMR (see analytical report for GC method). The maximum temperature during the distillation should not exceed 35°C. The crude mixture in IPAc was washed with 1.05 L of distilled water, 1.18 L of 0.3 M sulfuric acid, and 1.18 L of 6% aqueous sodium bicarbonate. The volume of the organic phase after the washes was 1.86 L. The pH of the mixture after the three aqueous washes was 6.5, 1.3 and 8.5, respectively. HPLC analysis of the mixture at this point indicated 93-94% assay yield for 15. The ratio of the desired 15:epi-15 was 96:4 by HPLC (same conditions as above). GC analysis at this point indicated that the hexamethyldisilazane by-product had been completely removed in the workup. EXAMPLE 25 [361.49] [505.40] NCS [133.5] 141.2 g 1.06 mol NaHC03 [84.01] 36.6 g 0.434 mol Nal [149.9] 158.6 g 1.06 mol Na2S03 [ 126.0] 80 g Water 1.55 L To the allyl amide 15 solution in IPAc from the previous step at 25°C was added a solution of 36.6 g of sodium bicarbonate in 1.03 L of distilled water and the biphasic mixture was cooled to 5°C. Solid N-chlorosuccinimide (141.2 g, 1.06 mol) was added. There was no exotherm after the addition of NCS. To this mixture was added an aqueous solution of sodium iodide ( 158.6 g, 1.06 mol) while maintaining the reaction mixture at 6-1 1 °C. The addition took 30 min, and the mixture became dark. The mixture was warmed to 25°C and aged with vigorous stirring. Progress of the reaction was monitored by HPLC: same system as above, approximate retention times: iodohydrins 16, epi-16, bis-epi-16 = 8.1 min; allyl amide 15 = 1 1.8 min. Analysis of the mixture by HPLC after 2.25 h indicated > 99.5% conversion. The approximate diastereomer ratio of 16:epi-16:bis-epi-16 in the crude mixture is roughly 94:2:4 at this point when resolution of the components can be obtained on this system. The agitation was discontinued and the layers were separated. To the organic phase was added aqueous sodium sulfite (80 g, 0.635 mol in 400 mL) over 10-15 min. The temperature of the mixture rose from 26-29°C after the sodium sulfite addition. The mixture was agitated for 40 min at 25°C. The solution was substantially decolorized after the sulfite wash. The layers were separated; the KF of the organic phase at this point was 25 g/L. The volume of the organic phase was 1.97 L. Quantitative analysis of the mixture by HPLC (same system as above) indicated a 86% overall assay yield of the iodohydrin 11 at this point (corrected for coeluting diastereomers). EXAMPLE 26 NaOMe [505.40] [377.49] NaOMe [54.02] d= 0.945 25 wt % in MeOH 172 g 0.796 mol 3% aqueous Na2Sθ4 1.5 L n-PrOH The solution of the iodohydrin 16 was concentrated in vacuo (28" Hg) to azeotropically dry the batch. A total of 700 mL of distillate was collected while maintaining a batch temperature of 22- 28°C. The distillate was replaced with 500 mL of IPAc (KF = 275 mg/L). The solution was cooled to 26°C and 25% NaOMe/MeOH solution (168.1 g) was added over a 10 min period. The temperature dropped to 24°C after the addition of sodium methoxide. The mixture became darker and a gummy solid briefly formed which redissolved. The mixture was aged for 1 h at 25°C. Analysis of the reaction was carried out by HPLC (same conditions as above), approximate retention times: epoxide epi-2 = 6.5 min, epoxide 2, bis-epi-2 = 7.1 min, iodohydrin 16 = 8.1 min. HPLC analysis indicated 99% conversion of the iodohydrin to the epoxide. After an additional 40 min, 4.1 g of the sodium methoxide/methanol solution was added. After 20 min, HPLC analysis indicated 99.5% conversion. The reaction was quenched by the addition of 366 mL of water at 25°C which was then agitated briefly ( 10 min) and the layers were separated. It was subsequently found that extended aging of the reaction and water wash agitation settling gave substantial back reaction to iodohydrin under these conditions in the pilot plant. This problem is especially acute in the water washes. To eliminate this problem, the reaction was run at 15°C. After > 99% conversion was achieved (1 h after NaOMe addition), the mixture was diluted with IPAc (40 % of batch volume) and initially washed with an increased volume of water (732 mL) at 20°C. Colder temperatures and more concentrated mixtures can result in the premature precipitation of 2 during the washes. The agitation/settling times were kept to a minimum (10 min/30 min, respectively). In this way, the back reaction could be limited to < 1 %. Crude mixtures containing (97:3) epoxide 2/iodohydrin 16 have been carried forward in the isolation to afford epoxide product containing 0.6 % iodohydrin. Epoxide product containing this level of iodohydrin has been carried forward without complication. The organic phase was washed with 3% aqueous sodium sulfate (2 x 750 mL). The volume of the organic phase was 1.98 L after the washes. The pH of the three water washes was 10.7, 9.4 and 8.6, respectively. HPLC analysis indicated a 86% overall assay yield of epoxide 2 at this point (corrected for 4% co-eluting bis-epi-2). The IPAc solution of epoxide 2 was concentrated at reduced pressure (28" Hg) to a volume of about 600 mL while maintaining the batch at 15- 22°C. The solvent was switched to n-PrOH by adding 750 mL n-PrOH while vacuum concentrating to a pot volume of about 500 mL, maintaining the batch at < 30°C. Temperatures > 35 °C during the concentration solvent switch can give an n-propyl ether by-product derived from epoxide 2. Analysis of the solvent composition by H NMR showed < 1 mol % IPAc remaining. The thick slurry was cooled to -10°C over an hour and aged for 45 min. The solids were filtered and washed with 125 mL of cold nPrOH. The product was dried in a vacuum oven at 25°C to afford 188.5 g of epoxide 2 (98.9 A %, 97.6 wt. %, 0.8 wt. %. epi-2, 79.3% yield overall from 14.) Normal phase HPLC (see analytical research memo for procedure) indicated no bis- epi-2 present in the isolated solids. EXAMPLE 27 Preparation of penultimate 6 2(S)-t-butylcarboxamide-4-N-Boc-piperazine 4 159 g 557 mmol (98.9 wt.%, 99.6 % ee) epoxide 2 (97.6 wt. %, 1.0 % epi-2) 200 g 530 mmol methanol 1.06 L HCl(g) 194 g 5.32 mmol 23% NaOH 740 mL isopropyl acetate 4.0 L water 700 mL ♦ corrected for wt. % purity Solid 2(S)-t-butylcarboxa_nide-4-t-butoxycarbonyl-piperazine 4 ( 1 9 c. 557 mmol) and the epoxide 2 (200 g, 530 mol ) were added to a 2 L three neck flask, equipped with a mechanical stirrer. reflux condenser, heating mantle, teflon coated thermocouple and nitrogen inlet. Methanol (756 mL) was added and the resulting slurry was heated to reflux temperature. After 40 min., a homogeneous solution was obtained. The internal temperature during reflux was 64-65°C. Progress of the reaction was monitored by HPLC analysis: 60:40 acetonitrile/10 mM (KH2PO4/K2HPO4), retention times: retention time (min) identity 4.8 piperazine 4 6.6 methyl ether 16 8.2 epoxide epi-2 8.9 epoxide 2 15.2 coupled product 5 The mixture was maintained at reflux until epoxide 2 was between 1.2 to 1.5 area % by HPLC analysis. The coupled product at this point was about 94-95 area %. The methyl ether 16 was present at 1.0-1.5 A% at completion. Typical time to achieve this conversion was 24-26 h at reflux. epi-2 The mixture was cooled to 5°C and anhydrous HCl gas (194 g, 5.32 moles, - 10 equiv.) was bubbled directly into the methanol solution under nitrogen atmosphere while keeping the temperature between 5-8°C over 2-3 h. After the addition was complete, the mixture was aged between 5°-8°C for 1 -3 h. Evolution of gas was observed at this point (carbon dioxide and isobutylene). Progress of the reaction was monitored by HPLC analysis: same conditions as above, Approximate retention times: retention time (min) identity 6.0 Boc intermediate 17 7.0 cis-aminoindanol 11 1 1.9 penultimate 6 15.1 coupled product 5 16.5 lactone 18 25.0 acetonide intermediate 19 The mixture was aged at 5° to 8°C until Boc intermediate 17 is < 0.5 area % by HPLC analysis. At this point, penultimate 6 was about 92-93 A%, 11 was < 1.0 A% and 18 was 0.6 A% by HPLC analysis. The deblocking was complete after 4 h at 5°C. Cooling and quenching the reaction promptly upon completion limits decomposition of 6 to 11 and 18 under the hydrolysis conditions. 11 18 The mixture was cooled to -10 to 15°C. This mixture was then slowly added to a 5 liter flask equipped with a mechanical stirrer containing a cold, stirred solution of DI water (700 mL) and methanol (300 mL) at 0-2°C; the pH of the quenched mixture was maintained between 8.5-9.0 by addition of 23 wgt. % aqueous NaOH solution (giving a highly exothermic reaction) while keeping the temperature between 10-20°C. The final batch pH was 9.0-9.5. The mixture was extracted with isopropyl acetate (3.0 L). The mixture was agitated and the layers were separated. The spent aqueous phase was re-extracted with isopropyl acetate (1.0 L). HPLC assay yield of 6 in isopropyl acetate at this point is 94%. The combined organic phase (~ 5.0 L) was concentrated under reduced pressure (24- 25" of Hg) to a volume of about 1.12 L at a batch temperature of 30- 40°C. The pot temperature during the solvent switch can rise to 40°C with no penalty in yield or degradation. This solution of crude 6 was then used directly in the next step to afford compound J. EXAMPLE 28 Preparation of monohydrate penultimate 6 261 g 499 mmol potassium bicarbonate 152 g 1.52 mol water 6.1 L picolyl chloride 93.3 g 569 mmol isopropyl acetate 3.17 L An isopropyl acetate solution of penultimate (4.96 L; 52.5 g/L of penultimate) was concentrated under reduced pressure to a volume of 1.18 L (260 g, 499 mmol). The batch temperature was maintained between 35°C to 44°C while keeping vacuum pressure at 25" of Hg. The methanol content was less than <1.0 vol %. The resulting slurry was treated with an aqueous solution of potassium bicarbonate (152 g in 630 mL of water, 1.59 mol, - 3.0 equiv.) and heated to 60°C. Then, an aqueous solution of picolyl chloride (93.8 g in 94 mL of water; 572 mmol, 1.14 equiv.( was added over 4 hours. The batch was seeded with J monohydrate after charging 75% of the picolyl chloride charge. The batch temperature was between 60°C to 65°C. At the end of the addition, the slurry mixture was aged for 20 h between 60°C to 65°C. The reaction was complete when the penultimate is <1.0 area % by HPLC analysis. The picolyl chloride level was between 0.5 to 0.8 area %. The batch was then diluted with 2.5 L of isopropyl acetate and 1.34 L of water and heated to 78°C. The layers were separated and the organic phase was washed with hot water (3 X 1.34 L) at 78°C. The hot water wash removed the bis-alkylated J and the level was reduced to <0.1 area % by HPLC analysis. The organic phase was slowly cooled to 75°C and seeded with J monohydrate (8.0 g) and then further cooled to 4°C over 2 h. The mixture was filtered to collect the product and the wet cake was washed with cold isopropyl acetate (2 X 335 mL). The wet cake was dried in vacuo (28" Hg, 22°C) to afford 273 g of J monohydrate in 79% isolated yield from the epoxide. 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, and modifications, as come within the scope of the following claims and its equivalents.

Claims: WHAT IS CLAIMED IS: A process for synthesis of a compound of the structure comprising the steps of: (a) heating for at least one hour a mixture of one equivalent of t-BuNH^O with about one equivalent of at a temperature range between about 25°C and about 150°C, said mixture optionally containing suitable solvent; (b) deblocking by treatment with acid, and (c) neutralizing the acid, to give the desired compound. 2. The process of Claim 1 , wherein the temperature range is between about 50°C and about 120°C. 3. The process of Claim 1 , wherein the temperature range is between about 65°C and about 85 °C. 4. The process of Claim 1 , wherein the suitable solvent is either an ester, an alcohol, a hydrocarbon, an ether or a formamide. or mixture thereof. 5. The process of Claim 1 , wherein the suitable solvent is an alcohol. 6. The process of Claim 1 , wherein the suitable solvent is methanol or isopropanol. 7. The process of Claim 1 , wherein the deblocking of step (b) is carried out with gaseous HCl. A process for synthesis of a compound of the structure comprising the steps of: (a) heating for at least one hour a mixture of one equivalent of t-BuNH^O with about one equivalent of at a temperature range between about 65°C and about 85°C, said mixture optionally containing as solvent methanol or isopropanol or mixture thereof; (b) cooling the mixture to about 0°C; (c) deblocking with gaseous HCl; and (d) neutralizing with NaOH, to give the desired compound. 9. The compound t-BuNH^O

Inventors: ASKIN DAVID, ENG KAN K, REIDER PAUL, VOLANTE RALPH P, ASKIN, DAVID, ENG, KAN, K., REIDER, PAUL, VOLANTE, RALPH, P.
Applicants: MERCK & CO INC, MERCK & CO., INC.
Application year: 1996
Main classification: C07D401
IPC codes: C07D401