GB2333775A - Process for preparing 4-alkylcarbonyl-(s)-piperazine-2-alkylcarboxamide - Google Patents

Abstract

A chiral hydrogenation process for the synthesis of a chiral piperazine, of the structure wherein R<SP>1</SP> is OX, and X is C 1-4 alkyl unsubstituted or substituted with aryl or trihalo, comprising hydrogenating a compound (1) Formula (2) in the presence of Rh or Ir chiral Bisphosphine catalysts. The compound of formula I is an intermediate for an HIV protease inhibitor. Certain intermediates used in the preparation of the compound of formula I are also claimed.

Description

TITLE OF THE INVENTION PROCESS FOR PREPARING 4-TERT-BU?"YLOXYCARBONYL-(S)- PIPERAZINE-2-TERT-BUTYLCARBOXAMIDE BACKGROUND OF THE INVENTION The present invention is concerned with a process for synthesizing intermediate compounds useful for preparing 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 synthesis of 4-tert butyloxycarbonyl-(S).piperazine-2-tert-butyl-carboxamide 1 of the structure,

which is an intermediate for the synthesis of the clinically efficacious compound J, of the structure

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 HW.

The nucleotide sequence of HIV shows the presence of a pol gene in one open reading frame (Ratner, L. et al., 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 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 described in EP 541,168. In the process, 4-tert-butyloxy-carbonyl-(S)-piperazine-2-tert- butylcarboxamide is prepared in a classical resolution of the racemic piperazine-2-tert-butylcarboxamide. The undesired (R) enantiomer is racemized in a separate step and recycled. The process is summarized in Scheme I: SCHEME I

Oxalyl Chloride > 0 o 0 &verbar; H2, Pd (OH) 2 COOH NH2t-Bu no CONHt-Bu 95 Pd(OH), 95 % H H Boc N L PGA L-P N ; L-PGA Boc20 N KOH N CONHt-Bu N CONHt-Bu 80 % N CONHt-Bu H H H 48 % (88 % ee, mother liq.) + 95 % H aq. NaOH N ; 2 L-PGA NslICON Ht-Bu H 52% yield (82% ee, crystalline salt) Although the process is high yielding and efficient, it requires a multitude of operations to resolve the racemic amine and then recycle the undesired enantiomer. The process is therefore expensive both in terms of capital investment and manpower. Additionally, the load on the waste stream from the washes and salt breaks is extensive, especially from the resolving agent L-pyroglutamic acid.

A key step in the assembly of Compound J is the coupling of the enantiomerically pure piperazine (a) with the enantiomerically pure epoxide (b) to afford the backbone of this important drug for the treatment of HIV infection ((a) Vacca, J.P.; Dorsey, B.D.; Schleif, W.A.; Levin, R. B. ; McDaniel, S. L. ; Darke, P.L.; Zugay, J.; Quintero, J.C.; Blahy, O.M.; Sardana, V.V.; Schlabach, A.J.; Graham, P.I.; Condra, J.H.; Gotlib, L.; Holloway, M. K. ; Lin, J.; Chen, I.-W.; Vastag, K.; Ostovic, D.; Anderson, P.S.; Emini, E.A.; Huff, J.R. Proc. Natl. Acad.

Sci. USA 1994, 91, 4096. (b)Idem., J. Med. Chem. 1994, 37, 3443. (c) Askin, D.; Eng, K.K; Rossen, K; Purick, R.M.; Wells, KM.; Volante, R.P.; Reider, P.J. Tetrahedron Lett. 1994,35, 673. (d) Maligres, P.E.; Upadhyay, V.; Rossen, K.; Cianciosi, S.J.; Purick, R.M.; Eng, K.K.; Reamer; R.A. Askin, D.; Volante, R.P.; Reider, P.J. Tetrahedron Lett.

1995, 36, 2195. (e) Maligres, P.E.; Weissman, S.A.; Upadhyay, V.; Cianciosi, S.J.; Purick, R.M.; Eng, K.K; Reamer, R.A.; Sager, J.; Rossen, K.; Askin, D.; Volante, R.P.; Reider, P.J. Tetrahedron 1996, 52, 3327. (f) Rossen, K; Reamer, R.A.; Volante, R.P.; Reider, P.J.

Tetrahedron Lett., 1996, 37, 6843. (g) Rossen, K.; Volante, R.P.; Reider, P.J. Tetrahedron Lett. 1997, 38, 777).

Compound J The preparation of piperazine (a) was previously reported using a chiral hydrogenation of the tetrahydropyrazine (c) (Rossen, K.; Weissman, S.A.; Sager, J.; Reamer, R.A.; Askin, D.A.; Volante, R.P.; Reider, P.J. Tetrahedron Lett. 1995, 36, 6419). While the chiral hydrogenation occurs in high yield and high ee using the Rh-BINAP catalyst, the synthesis of the tetrahydropyrazine hydrogenation substrate (c) requires 5 steps and thus makes this approach noncompetitive with the classical resolution approach (Askin, D.; Eng, K.K.; Rossen, K; Purick, R.M.; Wells, K.M.; Volante, R.P.; Reider, P.J.

Tetrahedron Lett. 1994,35, 673).

The synthesis of the heterocycle tetrahydropyrazine is achieved from readily available starting materials using an approach analogous to a previously reported piperazine-2-carboxamide synthesis, where a number of differently substituted piperazine-2-carboxamides were prepared (The Ugi-4-component condensation between chloroacetaldehyde, a carboxylic acid, an isocyanide and a mono-alkyl ethylenediamine gives (d) in a simple one pot reaction in acceptable yields.

Rossen, K; Sager, J.; DiMichele, L. M. Tetrahedron Lett. 1997, 38, 3183.

(b) Ugi, I.; Lohberger, S.; Karl, R. in Comprehensive Organic Chemistry: Selectivity for Synthetic Efficiency, Vol. 20. (Eds. B.M. Trost, C.H. Heathcock), Pergamon, Oxford 1991, P. 1083).

Chiral hydrogenation of simple acyclic alpha (acylamino)acrylic acids and their methyl esters is a known reaction that can occur with high chemical ( > 95%) and optical yield ( > 95%) with Rh-chiral bisphosphine catalysts [R. Noyori, Asymmetric Catalysis in Organic Chemistry, John Wiley and Sons, New York, 1994; M. Burk, et al., J. Am. Chem. Soc. 1993, 115, 101251. Unfortunately, chiral hydrogenation of more complex systems is less successful, and both conversion and optical yield drop off dramatically [H. Brunner, et al., Chem. Ber. 1992, 125, 2085; J. Armstrong, et al., Tetrahedron Lett. 1994, 35, 3239]. Substrates with an olefin as part of a vinylogous urea such as in 1 have not been successfully chirally hydrogenated. It is novel and unexpected to find that the chiral hydrogenation of 9 to 10 described in this invention works in high chemical and optical yield.

The present invention is set forth in Scheme II, concerning a novel process for the preparation of the piperazine intermediate 10 for the production of HIV protease inhibitor compound J. The essential step is accomplished by chirally hydrogenating the partially unsaturated tetrahydropyrazine derivative 9 with a chiral bisphosphine catalyst such as rhodium 2,2'-bis(diphenylphosphino)-1,1'-binaphthyl, to the fully saturated piperazine 10. Simple deprotection of the formyl group leads to the intermediate 1. Both the substitution pattern of 9 and choice of catalyst are essential to obtain the high chemical and optical yield.

SCHEME II

Boc Boc N, [(COD) (R)-BINAP Rh] OTf N OHON CQNHtBu H2 CONH tBu OHC 9 Boc 35% aq. hydrazine 0 lN H CONHtBu The chiral hydrogenation of the present invention builds up the desired chiral center from a readily accessible starting material in one step in high chemical and optical yield.

BRIEF DESCRIPTION OF THE INVENTION The present invention provides a new method to effect synthesis in high yields of compound 10 by chiral hydrogenation. The end product compound is useful as an inhibitor of HIV protease, renin and other proteases.

TABLE OF ABBREVIATIONS

BINAP 2,2'-bis(diphenylphosphino)-1,1'-binaphthyl Boc t-Bu 10 carbon 1 Boc-BPPM (2S,4S)-tert-Butyl 4-(diphenylphosphino)-2-(diphenyl- phosphinomethyl)-2-pyrrolidine-carboxylate Cbz Benzyl oxycarbonyl COD 1,5-c clooctadiene DIOP (R,R)-2 ,3-O-isopropylidene-2 ,3-dihydroxy-l 1 ,4-bis- (diphenylphosphino)-butane DUPHOS 1 ,2-Bi s((2S,5S)-2, 5-diethylphospholano)benzene PROPHOS 1,2-bis(di (diphenylphosphino) propane SKEWPHOS 2,4-bis(di (diphenylphosphino) pentane JOSIPHOS (R)-(-)-1-[(S)-2-(diphenylphosphino) )ferrocenyl]- ethyldicyclahexylphosphine PHANESHOS 9,12-bis(diphenylphosphino)[2.2]paracyclophane 3,5 DiMethyl- 9, 12-bis(di(3 ,5-dimethylphenyl )phosphino)- [2.2]PHANEPHOS [2.2]paracyclophane 3,5-DiMethyl-4- 9, 12-bis(di(3,5-dimethyl-4-methoxyphenyl)phosphino)- Methoxy [2.2]- [2.2]paracyclophane PHANEPHOS DIPAMP 1,2-Bis[(o-methoxy-phenyl)(phenyl)phosphino]ethane CHIRAPHOS (2S,3S)-(-)-Bis(diphenylphosphino)butane TolBINAP(R)-(+)-2,2'-bis(di-p-tolylphosphino)-1,1'-binaphthyl TfO triflate DETAILED DESCRIPTION OF THE INVENTION The present invention provides new methods for making compound J of the structure

by improvements in the synthesis of an intermediate of the structure

wherein R1 is OX, and X is C1-4 alkyl unsubstituted or substituted with aryl or trihalo.

One chiral hydrogenation process in this invention is for the synthesis of a chiral piperazine, of the structure

wherein R1 is OX, and X is ClA alkyl unsubstituted or substituted with aryl or trihalo, and comprises the steps of: (a) providing a quantity of the compound

(b) mixing thereto between about 1 mole Sc and about 13 mole % of the catalyst of the structure: (diene) Rhodium (chiral bisphosphine) (anionic counterion); or (diene) Iridium (chiral bisphosphine) (anionic counterion); (c) hydrogenating the mixture in solvent in the presence of a hydrogen source, at a temperature between about -100C and about 90"C; (d) to give the desired chiral piperazine.

Another chiral hydrogenation process of this invention is for the synthesis of a chiral piperazine, of the structure

wherein R1 is OX , and X is C 1-4 alkyl unsubstituted or substituted with aryl or trihalo, and comprises the steps of: (a) providing a quantity of the compound

(b) mixing thereto between about 1 mole % and about 13 mole % of the catalyst of the structure: (diene) Rhodium (chiral bisphosphine) (anionic counterion); or (diene) Iridium (chiral bisphosphine) (anionic counterion); (c) hydrogenating the mixture in solvent in the presence of a hydrogen source, at a temperature between about -100C and about 900C; (d) to give the desired chiral piperazine.

Another process of the invention is a process for making a compound of the formula

wherein R1 is OX, and X is C14 alkyl unsubstituted or substituted with aryl or trihalo, comprising the steps of: (a) combining mono-carbamate-protected ethylene diamine with CH(Z2)C(O)H, tertbutylisocyanide and formic acid to form

where Z is Cl or Br; (b) eliminating HZ by adding Et3N to the product of (a) to form

(c) cyclizing the product of (b) with an alkoxide base to form

In one preferred process, the alkoxide base is selected from the group consisting of LiOtBu, NaOtBu and KOtBu.

One preferred limitation is any of the above processes, wherein R1 is OtBu.

The diene of the catalyst in the processes of this invention may be selected from the group consisting of 1,5-cyclooctadiene, bicyclo[2.2. 1]hepta-2,5-diene, 1,5-hexadiene and two ethylene molecules.

The counterion of the catalyst in the processes of this invention may be selected from the group consisting of perchlorate, tetrafluoroborate, triflate, hexafluorophosphate, and hexafluoroantimonate anion.

The chiral bisphosphine in the processes of this invention may be selected from the group consisting of

wherein Ar is Ph or tolyl.

The solvent in the processes of the present invention may contain alcohol, said alcohol selected from the group comprising trifluoro ethanol, methanol, ethanol, n-propyl alcohol, isopropyl alcohol, amyl alcohol, butanol, and pentanol.

The source of hydrogen of Step c) may be selected from the group consisting of hydrogen gas, ammonium formate, hydrazine or triethylammonium formate.

In one preferred embodiment, the source of hydrogen is hydrogen gas, and Step c) of the processes given above is carried out under a pressure of between about 0.3 and about 200 atmospheres.

In another preferred embodiment the pressure of hydrogen gas is between about 2 and about 200 atmospheres.

One preferred temperature range for chiral hydrogenation is between about 20"C and about 90"C.

Another preferred embodiment of the chiral hydrogenation process of this invention is for the synthesis of the chiral piperazine, of the structure

and comprises the steps of: (a) providing a quantity of the compound

(b) mixing thereto between about 1 mole% and about 13 mole8 of the catalyst of the structure: (R)-BINAP-Rh-(1, 1,5-cyclooctadiene) triflate; (c) hydrogenating the mixture in alcoholic solvent under hydrogen at a pressure between about 2 and about 200 atmospheres, at a temperature of between about -100C and about 90"C; (d) to give the desired chiral piperazine.

In the scheme of the present invention, Scheme III, SCHEME III

Q R1 Chiral Hydrogenation Catalyst Ol, R Source of Hydrogen N N N CONH tBu N CONHt o'H O H I H O R'Ilective Deprotection H CONH-tBu H m wherein R1 is OX, and X is C1 4 alkyl unsubstituted or substituted with aryl or trihalo.

A chiral hydrogenation catalyst of the structure (diene) Rhodium (chiral bisphosphine) (anionic counterion), or (diene) Iridium (chiral bisphosphine) (anionic counterion) is contacted in solvent with substrate I, then hydrogenated in the presence of a source of hydrogen to give Compound n. Subsequent conventional steps of selective deprotection gives Compound III.

The most preferred substrate is 1, where R1 is preferably OtBu.

Suitable catalysts for the hydrogenations are Rh-chiral bisphosphine combinations or Ir-chiral bisphosphine combinations, in quantitities ranging from about 1 mole % to about 13 mole%. The preferred catalysts are prepared in situ or are isolated, and have the general structure: (diene) Rhodium (chiral bisphosphine) (anionic counterion), wherein the diene includes but is not limited to 1,5-cyclooctadiene, bicyclo[2.2. 1]hepta.2,5-diene, 1 ,5-hexadiene or 2 ethylene molecules.

Preferred chiral bisphosphines include but are not limited to BINAP and its atropisomeric analogues, such as TolBINAP, A or B.

Ar=Ph BINAP Ar=pCH3-C6H4 TolDlNAP The negatively charged counterion neutralizes the positive charge of the catalytic complex. Preferred anionic counterions include but are not limited to perchlorate, tetrafluoroborate, triflate, hexafluorophosphate (PF6-), or hexafluoroantimonate (SbF6-) anion.

Alternative, less preferable catalysts include complexes such as Rh (chiral bisphosphine) (ROH)2 (anionic counterion), obtained by substituting the diene with a second molecule of an ROH or alcoholic solvent. Another less preferred catalytic complex is generated in situ by reaction of [Rh Cl (diene)2)2 with the chiral bisphosphine.

Suitable reaction solvents are an alcohol, an ester, an ether, a halo carbon or an aromatic solvent, or mixtures thereof. Typical alcoholic solvents include but are not limited to methanol, ethanol, trifluoroethanol, n-propyl alcohol, isopropyl alcohol, butanol, or pentanol. Typical ester solvents include but are not limited to ethylacetate and isopropyl acetate. Typical ether solvents include but are not limited to diethylether, tetrahydrofliran. Typical aromatic solvents include but are not limited to benzene and toluene. Typical halogenated solvents include but are not limited to CH2C12, CHCl3.

Preferred solvents for the chiral hydrogenation reaction of the present invention are solvents containing one or more alcohols.

Most preferred solvents are alcohols, such as trifluoroethanol, methanol, ethanol, isopropylalcohol, amylalcohol, or mixtures thereof.

A source of hydrogen is needed in the chiral hydrogenation reaction of the present invention. In one embodiment, chiral hydrogenation is performed in the absence of air under a hydrogen atmosphere. Alternatively, standard transfer hydrogenation reagents, such as ammonium formate, hydrazine or triethylammonium formate may be used as a source of hydrogen. The preferred source is hydrogen gas under pressure of between about 0.3 and about 200 atm, most preferably between about 2 and about 200 atm.

The chiral hydrogenation reaction can be performed between about -100C and about 90"C, but the preferred temperature range is between 200C and about 90"C.

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 (HrV), 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 HW. 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 as says for antiviral compounds. For example, end-product compounds are useful for isolating enzyme mutants, which are excellent screening tools for more powerfill 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- 1 (S)-indanyl)-2(R)-phenylmethyl-4(S)-hydr 5-(1-(4-(3-pyridylmethyl)-2(S)-N'-(t=butylcarboxamido)-piperazinyl)) pentaneamide; [1S-[1a[aS*,gR*, d(R*)), 2a]]-N-(2,3-dihydro-2-hydroxy-1H-inden-1-yl)- 2[[( 1, 1-dimethylethyl)amino]carbonyl] -g-hydroxy-a-(phenyl-methyl)-4-(3- pyridinylmethyl)-1-piperazinepentaneamide; or N-(1(S)-2,3-dihydro-2(R)-hydroxy-1H-indenyl)-4(S)-hydroxy-2(R) phenylmethyl-5-[4- (3-pyri dylmethyl)-2(S)-(t-butylcarbamoyl)- piperazinyl] pentaneamid e.

When any variable (e.g., aryl, R1, X, etc.) occurs more than one time in any constituent or in formula I, 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). As used herein, with exceptions as noted, "aryl" is intended to mean phenyl (Ph) or naphthyl.

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 therapeuticallyeffective 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. Also, combinations of solvents, 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 In order to prepare a tetrahydropyrazine, the readily available N-Boc-ethylenediamine was combined with dichloroacetaldehyde to form the imine and then added tertbutylisocyanide and formic acid. The initially formed Ugi adduct 7 readily eliminates HCl with Et3N to give the vinylchloride 8.

(Preparation of 8: A solution ofN-Boc-ethylenendiamine (7.07 g, 44.1 mmol) and dichloroacetaldehyde hydrate (6.30 g, 48 mmol) in 100 mL of toluene is heated to 500C for 4 h and evaporated to dryness. The residual product is dissolved in 100 mL of MeOH and tert-butylisocyanide (8.0 mL, 71 mmol) and formic acid (96%, 2.0 mL, 51 mmol) are added at OOC. The reaction mixture is stirred at 230C for 2 days, when Et3N (12.5 mL, 90 mmol) is added. After stirring for 3 h at 230C, the reaction mixture is diluted with 500 mL of EtOAc and 500 mL of hexane and washed twice with 5% aqueous citric acid, 5% aqueous NaHCO3, water and brine. The organic phase is dried over Na2S04, treated with Darco G60 and filtered through a plug of SiO2 to give after evaporation 8 as a semisolid red material. Dichloroacetaldehyde hydrate is commercially available from TCI, N-Boc-ethylenediamine is commercially available from Aldrich, but is readily prepared in high yield from ethylenediamine).

In the subsequent cyeilization of 8 to 9, alkoxide bases were used with increasing conversions observed by going from LiOtBu to NaOtBu and KOtBu. While complete consumption of the starting material could be attained with KOtBu, the resulting yield was still low, presumably because of competitive polymersiation of the vinylchloride.

An acceptable yield in the cyclisation was obtained by careful control of the amount of base (1.6 equiv. of KOtBu), concentration (0.05M) and solvent (addition of KOtBu in tert-butanol to ThF solution of vinylchloride) (Preparation of 9: To a solution of 8 (1.00 g, 2. 88 mmol) in 50 mL of dry ThF under N2 is added KOtBu (1 M solution in tert-butanol, 4.5 mL) at 230C. After 3 h, the reaction mixture is diluted with 400 mL of EtOAc, washed with 5% aqueous citric acid, H20 and brine. The organic phase is dried (MgSOq), treated with Darco G60, and filtered through a plug of SiO2. The residue after evaporation is chromatographed on SiO2 (60% EtOAc in hexanes increasing to 70%) to give 9 as a tan solid.).

Chiral hydrogenation of 9 was achieved with various Rh and Ru based catalysts under a standard set of conditions (50 psi H2, 18 h, MeOH, 2 mol% catalyst). The results are summarized in Scheme 1 (Preparation of 10: To a solution of 100 mg of 9 in 4 mL of degassed MeOH is added 2 mol% of the catalyst. The mixture is then hydrogenated at 50 psi H2 for 24 h. Conversion and ee are determined using a Hewlett Packard SFC instrument with a YMC column (PN:A-903-5NP) followed by 2 Chiracel AS columns with 8% isocratic MeOH as eluent (1 mL / min). RT 9: 14.1 min, RT (R)-1O: 15.5 min, (S)-10: 17.0 min. Complete conversion of9 to 10 is obtained with 6 mol% of [(R)-BINAP (COD) Rh] OTf at 1500 psi H2 and 40"C for 24 h to give (S)-10. The absolute stereochemistry is determined by preparing authetic (S)-10 from (S)-2 of known absolute stereochemistry (EDC, HCOOH).

A list of suitable catalysts is shown below: Catalvst [(R)-BINAP Rh (COD)] OTf [(R)-pTolBINAP Rh (COD)]OTf [(4R,5R)-DIOP Rh (COD)] OTf [CHIRAPHOS Rh (COD)] OTf [(R,R) DIPAMP Rh (COD)] BF4 (R)-(S) JOSIPHOS Rh (COD)] OTf [3,5-DiMethyl[2.2]PHANEPHOS Rh (COD))OTf [3 ,5-DiMethylA-Methoxy[2 .2]PHANEPHOS Rh (COD)]OTf [TolBINAP Ru Cl2] Et3N adduct [[2.2]PHANEPHOS Ru (CF3C02)] with nBu4NI In the hydrogenation of 9, the best activity and enantioselectivity was obtained using the Rh-BINAP catalyst. Lower conversions were obtained with [2.2]PHANEPHOS based catalysts while the ferrocenyl based catalysts did not work with this substrate (Pye, P.J.; Rossen, K.; Reamer, R.A.; Tsou, N.N.; Volante, R.P.; Reider, P.J. J.

Am. Chem. Soc. 1997, 119, 6207).

Conversion of 9 to 10 was achieved at 100 atm H2 pressure a aqueous hydrazine led to a clean deprotection to give 1 and the enantiomeric purity of 1 was essentially unchanged (Preparation of 1: A solution of 330 mg (1.06 mmol) of 10 (99%ee) is heated in 5 mL of 35% aqueous hydrazine to 1000C for 9 hours. The reaction mixture is diluted with 100 mL of H20 and the product is extracted into 100 mL of EtOAc.

The organic phase is washed three times with H2O, dried over MgSO4 and evaporated to dryness to give 1 as a white crystalline material. An aliquot of the product was formylated (EDC, HCOOH) and its ee was determined as 98% using the SFC).

EXAMPLE 2 Conversion of Indene Oxide to Cls-1-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 119.

Conc. H2S04 9B 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 0-50 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 20-250.

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 coverted 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 15 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 1N 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 1N NH3/MeOH (20 ml) was added and the resin reslurried. 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 cis-1-amino-2-indanol ready for the tartaric acid resolving agent, B. 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 (116 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 250C and the internal pH at 10.5 with 1 M 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 (117 g) were concentrated to a volume of 600 mL.

C. Preparation of (1S,2R)-indene oxide The substrate, (1S, 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.

D. Preparation of c is-1-amino-2-indanol Indene oxide (117 g) diluted to a total volume of 600 mL in methylene chloride was diluted with acetonitrile (600 mL) and cooled to 20 C. Methanesulfonic acid (114 ml') was then added. The mixture was warmed to 250C and aged for 2 h. Water (600 mL) was added and the mixture heated at 450C 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 50C and filtered, dried in vacuo, to provide cis 1-amino-2-indanol.

E. Preparation of 1S-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 -100C. The reaction mixture was warmed to 220C 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 (855Z 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 400C to yield 1Samino, 2R-indanol.

F. Preparation of lS-amino-2R-indanol (1S, 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 -100C. The reaction mixture was warmed to 220C 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 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 1S-amino, 2R-indanol.

Alternatively, the remaining aqueous phase containing 1Samino-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. Tartaric acid was added and water was removed by distillation to crystallize the tartaric acid salt of the amino indanol.

G. 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 mixture was diluted with 5 M aqueous sodium hydroxide solution (50 mL) and extracted with methylene chloride. The organic extracts were concentrated in vacuo to give oxazoline.

H. Resolution of cis- 1-Amino-2-indanol Cis-1-Amino-2-indanol (100 g) was dissolved in methanol (1500 mL) and a solution of Tartaric acid (110 g) in methanol (1500 mL) was added. The mixture was heated to 600C and cooled to 200C, filtered and dried in vacuo to give amino, 2R-indanol L-tartaric acid salt as a methanol solvate.

I. Preparation of 1S-Amino-- 2R-indanol 1S-Amino, 2R-indanol Tartaric acid salt methanol solvate (88 g) was dissolved in water (180 mL) and heated to 55-600C. The solution was clarified by filtration and the pH adjusted to 12.5 with 50% aqueous sodium hydroxide. The mixture was cooled to 0-50C over 2 h, then aged at that temperature for 1 h, filtered, washed with cold water and dried in vacuo at 400C to yield 1S-amino, 2R-indanol.

J. Conversion of 1.2 indanol to cis-1-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 0-100C a volume of 0.22 ml of concentrated H2S04. 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.

K. Preparation of Indanol Reactants Compounds (+)-trans-2-bromo-1-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).

L. Preparation of cis-1-amino-2-indanol from trans-2-bromo 1-indanol Trans-2-bromo-1-indanol (10 g, 46.9 mmole diluted in 100 mL of acetonitrile containing 0.8 mL water) was cooled to -50C 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 80-1000C, removing acetonitrile by distillation to provide an aqueous solution of cis-1-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 cis-1-amino-2-indanol.

M. Preparation of cis-1S-amino-2R-indanol from cis-(1S,2R)- indandiol Cis-(1S,2R)-indandiol (1 g) was dissolved in acetonitrile (10 mL), cooled to OOC and concentrated sulfuric acid (1.0 mL) was added.

The mixture was aged for 40 minutes with warming to 200C. 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 11 and the resulting solid (potassium sulfate) removed by filtration to provide an aqueous solution of the cis- 1S-amino-2R-indanol.

N. Preparation of cis-1-amino-2-indanol from trans-1,2- indan di ol Trans-1,2-indandiol (1.5 g) was dissolved in acetonitrile (25 mL) cooled to OOC, and concentrated sulfuric acid (1.1 mL) was added.

The mixture was gradually warmed to 200C 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-1-amino-2-indanol.

O. Preparation of cis-1-amino-2-indanol from cis-1. 2-indandiol Cis- 1,2indandiol (1.0 g) was dissolved in acetonitrile (20 mL), cooled to -400C, 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 800C for 1 hour to provide an aqueous solution of cis-1-amino-2-indanol.

Prenaration of Acetonide 2-4

COCI 0 NH2 I NH OH 2-1 2-3 !149.l9) 0 [149. 19] 54 [281. 35] MsOH ; \N O 2-Methoxypropene W 2-4 [321.42] (-)-cis-1-aminoindan-2-ol (2-1) 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 (2-2) 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 NaHCO3 10. 8 L water 26. 2 L A slurry mixture consisting of (-)-cis-1-aminoindan-2-ol (21, 900 g, 6.02 mol) in 40 L of DEM and aqueous sodium carbonate solution (760 g, 6. 13 mol, of Na2CO3 H2O 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 46-470C and aged for 15 minutes. The reaction mixture was heated to 46470C and aged for 15 minutes to insure dissolution of the solids. The aqueous phase had a pH of 11.5. Neat 3-phenylpropionyl chloride 2.2 (1.05 kg, 6.23 mol) was added over 2 h between 470C to 590C. The internal temperature increased from 47"C to 590C during the addition of 2-2; the hydroxyamide 2-3 crystallized out of solution during the acid chloride addition. After the addition was complete, the reaction mixture was aged at 590C for 0.5 h and then warmed to 720C to insure dissolution of the solids. The temperature was increased to 720C 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 KH2P04 and K2HP04.

Approximate retention times: retention time (min.) 4.1 hydroxy amide 2-3 6.3 cis-aminoindanol 2-1 12.5 ester amide by product After complete acid chloride addition and 0.5 h age at 720C, the HPLC assay of the reaction mixture showed - 0.6 area % of 2-1, - 0.2 area % of ester amide by product and 98.7 area % of hydroxyamide. The hydroxy amide 2-3 was not efficiently rejected in the isolation of acetonide 2-4. 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 880C to 89"C to 40 L.

The dried DEM slurry of hydroxyamide 2-3 was treated with 1.28 L of 2-methoxypropene followed by 18.6 g of MSA at 300C. The addition of MSA in absence of 2-methoxypropene resulted in the formation of an amine ester. This impurity reconverts to hydroxy-amide 2-3 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 390C to 40 C for 3 h. The acetonide formation was monitored by HPLC analysis using the same conditions as described above in this example. Approximate retention times: retention time (min.) identitv 4.1 hydroxy amide 2-3 6.9 methylene ketal impurity 9.0 acetonide 2-4 12.5 ester amide by product The mixture was aged at 38-400C until 2-3 is 0.4 A%. A typical HPLC area So profile is as follows: 0.4 area % of hydroxyamide 23, 96.9 area % of acetonide 2-4, 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 2-3. The washed organic phase (34.2 L) was concentrated via atmospheric distillation at 780C to 800C to final volume of 3.5 L. The acetonide concentration was made -525 g/L to minimize isolation losses. The hot DEM solution of 2-4 was allowed to cool to 570C, seeded with 0.5 g of 2-4 and further cooled to OOC and aged for 0.5 h. The batch started to crystallize out of solution between 53"C to 550C. 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 300C to afford acetonide 2-4.

Preparation of Acetonide 24 from (2-1 # tartaric acid) salt (-)-cis-1-aminoindan-2-ol tartrate salt 100 g 297 mmol methanol solvate (44.3 wt. So of free base 2-1) sodium carbonate monohydrate 63.76 g 514 mmol diethoxymethane (DEM) 2. 83 L 3-phenylpropionyl chloride (2-2) 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 NaHCO3 520 mL water 1. 32 L A slurry mixture consisting of (-) 2-1 .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 Na2CO3-H2O 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 500C. Heating the reaction mixture to 60 C did not dissolve all the solids. Neat 3-phenyipropionyl chloride 2-2 (52.7 g, 312 mmol) was added over 30 min at 500C and the mixture was aged at 50 C for 15 min. Progress of the reaction is monitored by HPLC analysis: 60:40 Acetonitrile/5.0 mM of each KH2PO4 and K2HP04, 1.0 mL/min.

Approximate retention times: retention time (min.) identitv 4.1 hydroxy amide 2-3 6.3 cis-aminoindanol 2-1 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 So of 2-3.

After this point, the reaction mixture was heated to 750C.

The temperature was increased to 750C to dissolve the hydroxyamide 2-3 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 300C and treated with 63 mL of 2methoxypropene 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 2-3 is 0.7 ASo. A typical HPLC area % profile is as follows: 0.4 area So of hydroxy amide, 96.9 area So of acetonide 2-4, 0.2 area So of ester amide by product, 1.1 area % of methylene ketal impurity. The reaction mixture was cooled to 200C, 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 780C to 800C 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 2-4 was allowed to cool to 50-520C, seeded with 100 mg of product and further cooled to 50C 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 300C to afford acetonide 2-4.

Preparation of Acetonide 2-4 (Isoprpyl Acetate Solvent) (-)-bis-1-aminoindan-2-ol (2-1) (98.5 wgt. %) 80 g 535 mmol isopropyl acetate (IPAC) 1.2 L water 560 mL 5N sodium hydroxide 116 mL 580 mmol 3-phenylpropionyl chloride (2-2) 90.8 g 539 mmol methanesulfonic acid (MSA) 1.1 mL 17.0 mmol 2-methoxypropene (95% by GC) 119 mL 1.24 mol 5% aqueous NaHCO3 950 mL water 400 mL methyl cyclohexane 2. 25 L A mixture of (-)-cis-1-aminoindan-2-ol 2-1 (80 g, 535 mmol) in 1.2 L of IPAC and 560 mL of water was treated with 2-2(90.8 g, 539 mmol) while the pH was maintained between 8.0-10.5 at 70-720C with 5 N sodium hydroxide (116 mL, 580 mmol).

Progress of the reaction was monitored by HPLC analysis: 60:40 Acetonitrilel5.0 mM of each KH2P04 and K2HPO4. Approximate retention times: retention time (min.) identitv 4.1 hydroxy amide 2-3 6.3 cis-aminoindanol 2-1 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 726C-730C.

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 2-3 was treated with 2-methoxypropene (119 mL, 1.24 mol) followed by MSA (1.1 mL, 3.2 mole %) at 350C-380C for 4.5 h. The acetonide formation was monitored by HPLC analysis using the same conditions as described above. The mixture was aged at 38-400C until 2-3 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 00C-50C. 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 methylcyclo-hexane 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 650C-700C to insure dissolution of the solids, then cooled to 550C, seeded with the product and cooled to OOC. The moisture was aged at 00C 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 300C to afford acetonide 2-4.

Qy LDS $ N9 B X LDS + THF 2-4 & ) [120.98] -15 to 20"C [321.42] N O jn 2-5 [361.49] Acetonide (2-4) [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 [192.1] 35.73 g 0.186 mol THF sieve dried 1.43 L Water 1.05 L 0.3 M H2SO4 1. 18 L 6 % NaHCO3 1. 18 L IPAc The crystalline acetonide 2-4 (200 g, 0.622 mol, 99.1 wt. %) was dissolved in 1.25 L sieve dried TITh' (KF = 11 mg/L) under nitrogen atmosphere at 250C 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 -200C.

A THF solution of lithium hexamethyldisilazide (LDS, 1.32 M) was added to the allyl bromide/2-4 solution at such a rate as to maintain the reaction temperature at -200C. The LDS addition took 30 min. The mixture was aged at -15 to -200C 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 2-4 = 6.6 min; allyl acetonide 2-5 = 11.8 min; epi-2-5 = 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 11-15 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 1H 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 93-94io assay yield for 2-5. The ratio of the desired 2-5:epi-2-5 was 96:4 by HPLC (same conditions as above). GC analysis at this point indicated that the hexamethyldisila

[361.49] [505.40] NCS [133.5] 141.2 g 1.06 mol NaHCO3 [84.01] 36.6 g 0. 434 mol NaI (149.9] 158.6 g 1.06 mol Na2SO3 [126.0] 80 g Water 1. 56 L To the allyl amide 2-5 solution in IPAc from the previous step at 250C 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 50C. Solid Nchlorosuccinimide (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 6-110C. The addition took 30 min, and the mixture became dark. The mixture was warmed to 250C and aged with vigorous stirring. Progress of the reaction was monitored by HPLC: same system as above, approximate retention times: iodohydrins 2-6, epi-2-6, bis-epi-2-6 = 8.1 min; allyl amide 2-5= 11.8 min. Analysis of the mixture by HPLC after 2.25 h indicated > 99.58 conversion. The approximate diastereomer ratio of 2-6:epi-2.6:bis-epi-2-6 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 250C. 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 yield of the iodohydrin 2-6 at this point (corrected for coeluting diastereomers).

[505.40] [377.49] NaOMe [54.02] d= 0.945 25 wt % in MeOH 172 g 0.796 mol 3% aqueous Na2SO4 1. S L n-PrOH The solution of the iodohydrin 2-6 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 240C 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 250C. Analysis of the reaction was carried out by HPLC (same conditions as above), approximate retention times: epoxide epi-2-7 = 6.5 min, epoxide 2-7, bis-epi-2-7= 7.1 min, iodohydrin 2-6 = 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 250C 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 150C. After > 99% conversion was achieved (1 h after NaOMe addition), the mixture was diluted with IPAc (4056 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 2-7 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 2-7/iodohydrin 2-6 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 -2-7 at this point (corrected for 4% co-eluting bis-epi-2-7). The IPAc solution of epoxide 2-7 was concentrated at reduced pressure (28" Hg) to a volume of about 600 mL while maintaining the batch at 15-220C.

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 < 300C. Temperatures > 350C during the concentration/solvent switch can give an n-propyl ether as a degradation by-product derived from epoxide 2-7. Analysis of the solvent composition by 1H NMR showed < 1 mol % IPAc remaining. The thick slurry was cooled to -100C 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 epoxide 2-7. Normal phase HPLC (see analytical research memo for procedure) indicated no bis-epi-2-7 present in the isolated solids.

Preparation of Penultimate 2-9

BocN1 I NH N t-BuNH0 0 N 9 t-BuNHO O-Zo [285. 4] 0 9 MeOH, reflux 2-7 N [377.5] BocN OH N HCl (g) -P HCI 0 t-BuNH oO X 2-8 N [662.9] HNCThN OH NH 9H I N, t-BuNrr\0 2-9 S [522.7] 2(S)-t-butylcarboxamide-4-N-Boc-piperazine 1 159 g 557mmol (98.9 wt.%, 99.6% ee) epoxide 2-7(97.6 wt. %, 1.0% epi-2-7) 200 g 530 mmol methanol 1.06L HCl(g) 194 g 5.32 mol 23%NaOH 740 mL isopropyl acetate 4.0 L water 700 mL *corrected for wt. % purity Solid 2(S)-t-butylcarboxamide-4-t-butoxycarbonyl-piperazine 1 (159 g, 557 mmol) and the epoxide 2-7 (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 64-650C.

Progress of the reaction was monitored by HPLC analysis: 60:40 acetonitrile/l0 mM (KH2PO4/K2HPO4). Approximate retention times: retention time (min) 4.8 piperazine 1 6.6 methyl ether 2-10 8.2 epoxide epi-2-7 8.9 epoxide 2-7 15.2 coupled product 2-8 The mixture was maintained at reflux until epoxide 2-7 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 2-10 was present at 1.0-1.5 A% at completion. Typical time to achieve this conversion was 24-26 h at reflux.

The mixture was cooled to -50C 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) identitv 6.0 Boc intermediate 2-11 7.0 cis-aminoindanol 2-12 11.9 penultimate 2-9 15.1 coupled product 2-8 16.5 lactone 2-13 25.0 acetonide intermediate 2-14

The mixture was aged at 50 to 80C until Boc intermediate 2-11 is < 0.5 area % by HPLC analysis. At this point, penultimate 2-9 was about 92-93 A %, 2-12 was < 1.0 A% and 2-13 was 0.6 A So by HPLC analysis. The deblocking was complete after 4 h at 50C. Cooling and quenching the reaction promptly upon completion limits decomposition of 2-9 to 2-12 and 2-13 under the hydrolysis conditions.

The mixture was cooled to -10 to -150C. 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).

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 400C with no penalty in yield or degradation. This solution of crude 2-9 was then used directly in the next step to afford compound J.

Preparation of monohydrate

penultimate 2-9 261 g 499 mmol potassium bicarbonate 152 g 1.52 mol water 6.1L picolyl chloride 93.3 g 569 mmol isopropyl acetate 3.17 L An isopropyl acetate solution of penultimate (4.96 L; 52.5 gIL 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 440C 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 gin 630 mL of water, 1.59 mol, -3.0 equiv.) and heated to 60"C. Then, an aqueous solution of picolyl choride (93.8 g in 94 mL of water; 572 mmol, 1.14 equiv.) was added over 4 hours. The batch was seeded with compound 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 600C to 650C. 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 780C. The layers were separated and the organic phase was washed with hot water (3 X 1.34 L) at 780C. The hot water wash removed the bis-alkylated compound J and the level was reduced to < 0.1 area So by HPLC analysis.

The organic phase was slowly cooled to 750C and seeded with compound J monohydrate (8.0 g) and then further cooled to 40C 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, 220C) to afford compound J monohydrate.

Pvrazine-2-tert-butvl carboxamide 2-16

2-Pyrazinecarboxylic acid (2-15) 3.35 kg (27 mol) Oxalyl chloride 3.46 kg (27.2 mol) tert-Butylamine (KF = 460 mg/ml) 9.36 L (89 mol) EtOAc (KF = 56 mg/ml) 27 L DMF 120 mL 1-Propanol 30 L The carboxylic acid 2-15 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 20C. The oxalyl chloride was added, maintaining the temperature between 5 and 8"C.

The addition was completed in 5 h. During the exothermic addition CO and CO2 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 2-15 remained.

The assay for completion of the acid chloride formation is important because incomplete reaction leads to formation of a bis-tertbutyl 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 2-15 = 10.7 min, amide 2-16= 28.1 min.

The reaction mixture was aged at 50C for 1 h. The resulting slurry was cooled to OOC and the tert-butylamine was added at such a rate as to keep the internal temperature below 200C.

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 180C for an additional 30 min. The precipitated ammoniwn 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% NaHCO3 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 2-16 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 1H 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 87-880C. 13C NMR (75 MHz, CDCl3, ppm) 161.8, 146.8,145.0, 143.8, 142.1, 51.0, 28.5.

Materials Pyrazine-2-tert-butylcarbossmide 2-162.4 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 2- 16/1-propanol solution was placed into the 5 gal autoclave. The catalyst was added and the mixture was hydrogenated at 650C 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 2-16. The mixture was cooled, purged with N2 and the catalyst was removed by filtration through Solka Floc. 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 1600C at 100C/min, hold 5 min, then at 100C/min to 2500C, retention times: 2-16 = 7.0 min, 2-17 = 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 a yield over amidation and hydrogenation and a concentration of 2-17.

Evaporation of an aliquot gave 2-17 as a white solid m.p. 150 151"C; 13C NMR (75 MHz, D2O, ppm) 173.5, 59.8, 52.0, 48.7, 45.0, 44.8, 28.7.

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 (17)

WHAT IS CLAIMED IS:

1. A chiral hydrogenation process for the synthesis of a chiral piperazine, of the structure

wherein R1 is OX, and X is Cl-4 alkyl unsubstituted or substituted with aryl or trihalo, comprising the steps of (a) providing a quantity of the compound

(b) mixing thereto between about 1 mole % and about 13 mole % of the catalyst of the structure: (diene) Rhodium (chiral bisphosphine) (anionic counterion); or (diene) Iridium (chiral bisphosphine) (anionic counterion); (c) hydrogenating the mixture in solvent in the presence of a hydrogen source, at a temperature between about -100C and about 90"C.

2. A chiral hydrogenation process for the synthesis of a chiral piperazine, of the structure

wherein R1 is OX, and X is C1-4 alkyl unsubstituted or substituted with aryl or trihalo, comprising the steps of: (a) providing a quantity of the compound

(b) mixing thereto between about 1 mole So and about 13 mole % of the catalyst of the structure: (diene) Rhodium (chiral bisphosphine) (anionic counterion); or (diene) Iridium (chiral bisphosphine) (anionic counterion); (c) hydrogenating the mixture in solvent in the presence of a hydrogen source, at a temperature between about -100C and about 90"C.

3. The process of Claim 1 or 2, wherein R1 is OtBu.

4. The process of Claim 1 or 2, wherein the diene of the catalyst is selected from the group consisting of 1,5-cyclooctadiene, bicyclo[2.2 . 1]hepta-2,5-diene, 1,5-hexadiene and two ethylene molecules.

5. The process of Claim 1 or 2, wherein the counterion of the catalyst is selected from the group consisting of perchlorate, tetrafluoroborate, triflate, hexafluorophosphate, and hexafluoroantimonate am on.

6. The process of Claim 1 or 2, wherein the chiral bisphosphine is selected from the group consisting of

wherein Ar is Ph or tolyl.

7. The process of Claim 1 or 2 wherein the solvent contains alcohol, said alcohol selected from the group comprising trifluoro ethanol, methanol, ethanol, n-propyl alcohol, isopropyl alcohol, amyl alcohol, butanol, and pentanol.

8. The process of Claim 1 or 2 wherein the source of hydrogen of Step c) is selected from the group consisting of hydrogen gas, ammonium formate, hydrazine or triethylammonium formate.

9. The process of Claim 8, wherein the source of hydrogen is hydrogen gas, and Step c) is carried out under a pressure of between about 0.3 and about 200 atmospheres.

10. The process of Claim 9, wherein the pressure is between about 2 and about 200 atmospheres.

11. The process of Claim 1 or 2, wherein the temperature range of Step c) is between about 20"C and about 90"C.

12. A chiral hydrogenation process for the synthesis of the chiral piperazine, of the structure

comprising the steps of: (a) providing a quantity of the compound

(b) mixing thereto between about 1 mole% and about 13 mole% of the catalyst of the structure: (R)-BINAP-Rh- (1, 5-cyclooctadiene) triflate; (c) hydrogenating the mixture in alcoholic solvent under hydrogen at a pressure between about 2 and about 300 atmospheres, at a temperature of between about -100C and about 90"C.

13. A process for the synthesis of a compound of the structure

wherein R1 is OX, and Xis C1-4 alkyl unsubstituted or substituted with aryl or trihalo, comprising the steps of: (a) combining mono-carbamate-protected ethylene diamine with CH(Z2)C(O)H, tertbutylisocyanide and formic acid to form

where Z is Cl or Br; (b) eliminating HZ by adding Et3N to the product of (a) to form

(c) cyclizing the product of (b) with an alkoxide base to form

14. A process of claim 13, wherein the alkoxide base is selected from the group consisting of LiOtBu, NaOtBu and KOtBu.

15. A process for preparing a compound of the formula

wherein R1 is OX, and X is C1 4 alkyl unsubstituted or substituted with aryl or trihalo which comprises cyclizing

where Z is Cl or Br, with an alkoxide base.

16. A process for preparing a compound of the formula

wherein R1 is OX, X is C1 4 alkyl unsubstituted or substituted with aryl or trihalo, and Z is Cl or Br, which comprises eliminating HZ by adding Et3N to

17. A process for preparing a compound of the formula

wherein R1 is OX, X is C1-4 alkyl unsubstituted or substituted with aryl or trihalo, and Z is Cl or Br, which comprises combining monocarbamate-protected ethylene diamine with CH(Z2)C(O)H, tertbutylisocyanide and formic acid.