EP1206470A2 - Processes and intermediates for the preparation of isoxazolecarboxamides and analogues - Google Patents
Processes and intermediates for the preparation of isoxazolecarboxamides and analoguesInfo
- Publication number
- EP1206470A2 EP1206470A2 EP00955830A EP00955830A EP1206470A2 EP 1206470 A2 EP1206470 A2 EP 1206470A2 EP 00955830 A EP00955830 A EP 00955830A EP 00955830 A EP00955830 A EP 00955830A EP 1206470 A2 EP1206470 A2 EP 1206470A2
- Authority
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- European Patent Office
- Prior art keywords
- formula
- compound
- group
- process according
- alkyl group
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D413/00—Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms
- C07D413/02—Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms containing two hetero rings
- C07D413/12—Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms containing two hetero rings linked by a chain containing hetero atoms as chain links
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P31/00—Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
- A61P31/12—Antivirals
- A61P31/14—Antivirals for RNA viruses
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
- B01J19/2435—Loop-type reactors
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2475—Membrane reactors
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C229/00—Compounds containing amino and carboxyl groups bound to the same carbon skeleton
- C07C229/02—Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton
- C07C229/34—Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton containing six-membered aromatic rings
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C271/00—Derivatives of carbamic acids, i.e. compounds containing any of the groups, the nitrogen atom not being part of nitro or nitroso groups
- C07C271/06—Esters of carbamic acids
- C07C271/08—Esters of carbamic acids having oxygen atoms of carbamate groups bound to acyclic carbon atoms
- C07C271/10—Esters of carbamic acids having oxygen atoms of carbamate groups bound to acyclic carbon atoms with the nitrogen atoms of the carbamate groups bound to hydrogen atoms or to acyclic carbon atoms
- C07C271/22—Esters of carbamic acids having oxygen atoms of carbamate groups bound to acyclic carbon atoms with the nitrogen atoms of the carbamate groups bound to hydrogen atoms or to acyclic carbon atoms to carbon atoms of hydrocarbon radicals substituted by carboxyl groups
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C303/00—Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides
- C07C303/26—Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides of esters of sulfonic acids
- C07C303/28—Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides of esters of sulfonic acids by reaction of hydroxy compounds with sulfonic acids or derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/66—Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety
- C07C69/73—Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety of unsaturated acids
- C07C69/732—Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety of unsaturated acids of unsaturated hydroxy carboxylic acids
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D261/00—Heterocyclic compounds containing 1,2-oxazole or hydrogenated 1,2-oxazole rings
- C07D261/02—Heterocyclic compounds containing 1,2-oxazole or hydrogenated 1,2-oxazole rings not condensed with other rings
- C07D261/06—Heterocyclic compounds containing 1,2-oxazole or hydrogenated 1,2-oxazole rings not condensed with other rings having two or more double bonds between ring members or between ring members and non-ring members
- C07D261/10—Heterocyclic compounds containing 1,2-oxazole or hydrogenated 1,2-oxazole rings not condensed with other rings having two or more double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D261/18—Carbon atoms having three bonds to hetero atoms, with at the most one bond to halogen
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00027—Process aspects
- B01J2219/00033—Continuous processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00099—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor the reactor being immersed in the heat exchange medium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00162—Controlling or regulating processes controlling the pressure
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00177—Controlling or regulating processes controlling the pH
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B2200/00—Indexing scheme relating to specific properties of organic compounds
- C07B2200/07—Optical isomers
Definitions
- This application also relates to a U.S. Provisional Patent Application No. 60/150,358 (Attorney Docket No.: 0125.0028) entitled "Efficient Synthetic Routes For The Preparation Of Rhinovirus Protease Inhibitors And Key Intermediates" having named as inventors: Q. Tian, N. Nayyar, S. Babu, J. Tao, T. Moran, R. Dagnino, Jr., T. Remarchuk, M. Melnick, L. Mitchell, Jr., and S. Bender.
- This aforementioned application also relates to synthetic routes for the preparation of rhinovirus protease inhibitors and key intermediates for use therein.
- the present invention relates to an improved process for the preparation of
- the present invention also includes a novel group of intermediate compounds
- the present invention includes a
- Picornaviruses are a family of tiny non-enveloped positive-stranded RNA-
- viruses that infect humans and other animals. These viruses include the human rhinoviruses, human polioviruses, human coxsackieviruses, human
- echoviruses human and bovine enteroviruses, encephalomyocarditis viruses,
- the human rhinoviruses are a major cause of the common cold.
- proteolytic 3C enzymes are required for the natural maturation of the picornaviruses. Thus, inhibiting the activity of these proteolytic 3C enzymes should represent an important and useful approach for the treatment and cure of viral infections of this nature, including the common cold.
- Rhinoviral serotypes and is currently in human clinical trials.
- the '354 application also discloses methods and intermediates useful for synthesizing these compounds.
- the '354 application discloses methods for synthesizing the intermediates of
- the process of the present invention involves an enzymatic reduction step. Due to the expense of certain catalysts, including enzymatic catalysts, there has been a
- hollow fiber filter reactors in which a majority of the volume of the reagent(s) and
- the present invention relates to the discovery of a cost effective and efficient process for the preparation of the antipicornaviral agents of formula I, such as compound AG7088, as well as intermediates which are useful in that synthesis.
- the antipicornaviral agents of formula I comprise:
- Ri is H, F, an alkyl group, OH, SH, or an O-alkyl group; R and R are each independently H;
- n is an integer from 0 to 5
- Ai is CH or N
- a 2 and each A 3 are independently
- each R 4 ⁇ is independently H or lower alkyl, provided that no more than two
- heteroatoms occur consecutively in the above-depicted ring formed by Ai, A 2 , (A 3 ) n ,
- a and C O, and at least one of R 2 and R 3 is
- R 5 and R 6 are each independently H, F, an alkyl group, a cycloalkyl group, a
- heterocycloalkyl group an aryl group, or a heteroaryl group
- R 7 and R 8 are each independently H, an alkyl group, a cycloalkyl group, a
- heterocycloalkyl group an aryl group, a heteroaryl group, -OR 1 , -SR 17 , -NR ]7 R 18 , -
- R ⁇ , R 18 , and R 1 are each independently H, an alkyl group, a cycloalkyl group, a heterocycloalkyl group, an aryl group, a heteroaryl
- R and R 8 are independently alkyl groups, or an acyl group, provided that at least one of R and R 8 is an alkyl group, an
- R 9 is a five-membered heterocycle having from one to three heteroatoms selected from
- Z and Z] are each independently H, F, an alkyl group, a cycloalkyl group, a
- heterocycloalkyl group an aryl group, a heteroaryl group, -C(O)R 21 , -CO 2 R 21 , CN, -C(O)NR 21 R 22 , -C(O)NR 21 OR 22 , -C(S)R 21 , -C(S)NR 21 R 22 , -NO 2 , -SOR 21 , -SO 2 R 21 ,
- R 21 , R 22 , R23, and R 24 are each independently H, an alkyl group, a cycloalkyl group, a heterocycloalkyl group, an aryl group, a heteroaryl group, an acyl group, or a thioacyl group, or where any of two of R 2 ⁇ , R 2 , R 23 , and R 4 , together with the atom(s) to which they are bonded, form a heterocycloalkyl group, provided that Z and X are not both H;
- R ls together with the atoms to which they are bonded, form a cycloalkyl or heterocycloalkyl group, where Z ⁇ and R t are as defined above except for moieties that cannot form the cycloalkyl or heterocycloalkyl group;
- antipicornaviral agents of formula I may be any antipicornaviral agents of formula I.
- the present invention provides novel intermediates for use in the processes of the present invention, and novel processes for the preparation of those
- the present invention also relates to a continuous membrane reactor that may be used in the processes of the present invention.
- alkyl group is intended to mean a straight- or branched chain monovalent
- Suitable sustituents as defined below (e.g., one or more halogens, such as F, CI, Br, or I, with F and CI being preferred).
- suitable sustituents e.g., one or more halogens, such as F, CI, Br, or I, with F and CI being preferred.
- a "cycloalkyl group” is intended to mean a non-aromatic monovalent monocyclic, bicyclic, or tricyclic radical containing 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, or 14 carbon ring atoms, each of which may be saturated or unsaturated, and which may be unsubstituted or substituted by one or more suitable substituents as defined below, and to which may be fused one or more heterocycloalkyl groups, aryl groups, or heteroaryl groups, which themselves may be unsubstituted or substituted by one or
- cycloalkyl groups include following moieties:
- heterocycloalky group is intended to mean a non-aromatic monovalent
- heterocycloalkyl groups which themselves may be unsubstituted or substituted by one or more suitable substituents.
- illustrative examples of heterocycloalkyl groups include the following
- aryl group is intended to mean an aromatic monovalent monocyclic
- aryl group includes a benzyl group (Bzl).
- aryl groups include the following moieties:
- heteroaryl group is intended to mean an aromatic monovalent monocyclic, bicyclic, or tricyclic radical containing 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or 18 ring atoms, including 1, 2, 3, 4, or 5 heteroatoms selected from nitrogen, oxygen, and sulfur, which may be unsubstituted or substituted by one or more suitable substituents as defined below, and to which may be fused one or more cycloalkyl groups, heterocycloalkyl groups, or aryl groups, which themselves may be
- heteroaryl groups include the following moieties:
- heterocycle is intended to mean a heteroaryl or heterocycloalkyl group
- acyl group is intended to mean a -C(O)-R radical, where R is a
- a "thioacyl group” is intended to mean a -C(S)-R radical, where R is a
- a "sulfonyl group” is intended to mean a -SO 2 R radical, where R is a
- a "hydroxy group” is intended to mean the radical -OH.
- amino group is intended to mean the radical -NH 2 .
- alkylamino group is intended to mean the radical -NHR a , where R a is an
- dialkylamino group is intended to mean the radical -NR a R b , where R a and
- R b are each independently an alkyl group.
- alkoxy group is intended to mean the radical -OR a , where R a is an alkyl
- alkoxy groups include methoxy, ethoxy, propoxy, and the like.
- alkoxycarbonyl group is intended to mean the radical -C(O)OR a , where R a is an alkyl group.
- alkylsulfonyl group is intended to mean the radical -SO R a , where R a is an alkyl group.
- alkylaminocarbonyl group is intended to mean the radical -C(O)NHR a ,
- R a is an alkyl group
- dialkylaminocarbonyl group is intended to mean the radical -C(O)NR a R b , where R a and R b are each independently an alkyl group.
- a “mercapto group” is intended to mean the radical -SH.
- alkylthio group is intended to mean the radical -SR a , where R a is an alkyl
- a “carboxy group” is intended to mean the radical -C(O)OH.
- a “carbamoyl group” is intended to mean the radical -C(O)NH 2 .
- An "aryloxy group” is intended to mean the radical -OR c , where R c is an aryl
- heteroaryloxy group is intended to mean the radical -OR ⁇ ⁇ , where R ⁇ j is a heteroaryl group.
- arylthio group is intended to mean the radical -SR C , where R c is an aryl
- heteroarylthio group is intended to mean the radical -SRa, where R is a heteroaryl group.
- a “leaving group” (Lv) is intended to mean any suitable group that will be
- any conjugate base of a strong acid can act as a leaving group
- suitable leaving groups include, but are not limited to, -F, -CI, -Br, alkyl chlorides, alkyl bromides, alkyl iodides, alkyl sulfonates, alkyl benzenesulfonates, alkyl p-toluenesulfonates, alkyl methanesulfonates, triflate, and any groups having a bisulfate, methyl sulfate, or sulfonate ion.
- Typical protecting groups, reagents and solvents such as, but not limited to,
- suitable organic moiety is intended to mean any organic moiety recognizable, such as by routine testing, to those skilled in the art as not adversely affecting the inhibitory activity of the inventive compounds.
- suitable organic moieties include, but are not limited to, hydroxyl groups, alkyl groups, oxo groups, cycloalkyl groups, heterocycloalkyl groups, aryl groups, heteroaryl groups, acyl groups, sulfonyl groups, mercapto groups, alkylthio groups, alkoxy groups,
- carboxy groups amino groups, alkylamino groups, dialkylamino groups, carbamoyl groups, arylthio groups, heteroarylthio groups, and the like.
- a “prodrug” is intended to mean a compound that is converted under physiological conditions or by solvolysis or metabolically to a specified compound that is pharmaceutically active.
- a "pharmaceutically active metabolite” is intended to mean a pharmacologically active product produced through metabolism in the body of a specified compound.
- solvate is intended to mean a pharmaceutically acceptable solvate form of a specified compound that retains the biological effectiveness of such compound.
- solvates include compounds of the invention in combination with water,
- a "pharmaceutically acceptable salt” is intended to mean a salt that retains the
- Examples of pharmaceutically acceptable salts include sulfates, pyrosulfates, bisulfates, sulfites, bisulfites, phosphates,
- chlorides bromides, iodides, acetates, propionates, decanoates, caprylates, acrylates,
- succinates suberates, sebacates, fumarates, maleates, butyne-1, 4-dioates, hexyne-1,6- dioates, benzoates, chlorobenzoates, methylbenzoates, dinitrobenzoates,
- naphthalene-2-sulfonates and mandelates.
- the present invention further provides synthetic methods that are comprised of
- a synthetic method is comprised of a synthetic step when the synthetic step is at least part of the final synthetic method. In such a fashion, the synthetic method can be only the synthetic
- Such a synthetic method can have a few additional synthetic steps or can have numerous additional
- a desired salt may be prepared by any suitable method known to
- hydrochloric acid hydrobromic acid
- sulfuric acid sulfuric acid
- nitric acid sulfuric acid
- phosphoric acid and the
- an organic acid such as acetic acid; maleic acid; succinic acid; mandelic
- amino acid such as apsartic acid or glutamic acid
- aromatic acid such as benzoic acid or cinnamic acid
- sulfonic acid such as
- a desired salt may be prepared by any suitable method known to the art, including treatment of the free acid with an inorganic or organic base, such as
- an amine primary, secondary, or tertiary
- an alkali metal or alkaline earth metal hydroxide or the like.
- suitable salts include organic salts derived from amino acids such as glycine and arginine; ammonia; primary, secondary, and tertiary amines; and cyclic amines, such as piperidine, morpholine, and piperazine; as well as inorganic salts derived from sodium, calcium, potassium, magnesium, manganese, iron, copper, zinc, aluminum, and lithium.
- process of the present invention may exist as single stereoisomers, racemates, and/or
- optically pure is intended to mean a compound that comprises at least 90% of a single isomer (80% enantiomeric excess), more preferably at least 95% (90% e.e.), even more preferably at least 97.5% (95% e.e.), and most preferably at least 99%
- the antipicornaviral agents of formula I formed from the process of the present invention are optically pure.
- the present invention relates to a process of preparing antipicornaviral agents of formula I:
- Ri is H, F, an alkyl group, OH, SH, or an O-alkyl group
- R and R 3 are each independently H;
- n is an integer from 0 to 5
- Ai is CH or N
- a 2 and each A 3 are independently
- each R 1 is independently H or lower alkyl, provided that no more than two
- heteroatoms occur consecutively in the above-depicted ring formed by Ai, A 2 , (A 3 ) n ,
- R 5 and R 6 are each independently H, F, an alkyl group, a cycloalkyl group, a
- heterocycloalkyl group an aryl group, or a heteroaryl group
- R 7 and R 8 are each independently H, an alkyl group, a cycloalkyl group, a
- heterocycloalkyl group an aryl group, a heteroaryl group, -OR ⁇ 7 , -SR ⁇ 7 , -NR 17 R ⁇ 8 ,
- R and R 8 is an alkyl group, an aryl group, a heteroaryl group, or an acyl group, provided that at least one of R and R 8 is an alkyl group, an aryl group, a heteroaryl group, or an acyl group, provided that at least one of R and R 8 is an alkyl group, an aryl group, a heteroaryl group, or an acyl group, provided that at least one of R and R 8 is an alkyl group, an
- aryl group a heteroaryl group, -OR ⁇ , -SR i7 , -NR ⁇ 7 R] 8 , -NR ⁇ 9 NR ⁇ 7 R ⁇ 8 , or -NRj 7 OR ⁇ 8 ;
- R 9 is a five-membered heterocycle having from one to three heteroatoms selected from
- Z and Zi are each independently H, F, an alkyl group, a cycloalkyl group, a
- heterocycloalkyl group an aryl group, a heteroaryl group, -C(O)R 2 ⁇ , -CO 2 R 21 , CN,
- R 21 , R 2 , R 3 , and R 4 are each independently H, an alkyl group, a cycloalkyl group, a heterocycloalkyl group, an aryl group, a heteroaryl group,
- heterocycloalkyl group where and R t are as defined above except for moieties that cannot form the cycloalkyl or heterocycloalkyl group; or Z and Z ⁇ , together with the atoms to which they are bonded, form a cycloalkyl or
- the amide-forming reaction may be achieved by any suitable method, reagents
- a compound of formula H may be reacted with a compound of formula HI in the presence of HATU, DIPEA, CH CN and H 2 O to yield the desired compound of formula I.
- Any suitable purification method may be used to
- the compound of formula I is prepared by an amide-forming reaction comprising the steps of:
- preferable amide-forming reaction utilizes some or all of the reagents and reaction conditions disclosed below.
- the compound of formula H and the compound of formula HIA in DMF are combined in any suitable container.
- suitable container is preferably a single neck flask which is then covered with any
- the N-methylmorpholine is added via a syringe in one single portion and the reaction mixture cooled to about between -5° C and 5° C. More preferably, the
- reaction mixture is cooled to about O C
- a solution of the compound of formula Lv-X is then added to the reaction mixture.
- the solution of the compound of formula Lv-X is a solution of the compound of formula Lv-X in DMF.
- the compound of formula Lv-X is CDMT.
- the solution of the compound of formula Lv-X is added to the reaction mixture by any suitable method so as to maintain the reaction mixture at a constant temperature.
- the solution of the compound of formula Lv-X may be added to the reaction mixture dropwise utilizing a syringe.
- the reaction mixture is allowed to warm to about room temperature.
- the progress of the reaction may be followed by monitoring the disappearance of the compound of formula H by thin layer chromatography (hereinafter "TLC").
- the compound of formula I may then be removed from the slurry by any means
- the compound of formula I is purified by
- the present invention also discloses a novel method for preparing the compound of formula HIA comprising the step of reacting a
- the method for preparing the compound of formula HIA from the compound of formula NIK utilizes some or all of the reagents and reaction conditions disclosed below.
- the compound of formula HEB and DCM are placed
- TFA is added via
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the solvent and excess TFA may be any suitable means.
- the compound of formula HIA is used
- the present invention also relates to a process for the preparation of the
- formula HA are also useful intermediates for preparing the antipicornaviral agents of formula I.
- the present invention discloses a process for preparing the compounds of formula HA, comprising the steps of:
- formula XIV utilizes some or all of the reagents and reaction conditions disclosed below.
- the compound of formula XTH is stirred with CDI in THF under a nitrogen stream for at least about 1 hour at room temperature to yield an acyl imidazole intermediate.
- lithium bistrimethylsilylamide solution LHMDS
- t-Butyl acetate is added slowly to the LHMDS solution keeping the temperature below about -60° C to form a reaction mixture.
- the acyl imidazole intermediate prepared as disclosed above, is slowly added to the reaction mixture, comprising the lithium enolate of t-butyl acetate, under nitrogen keeping the internal temperature at or below
- reaction mixture is stirred at -60° C for at least an additional 1 hour.
- reaction mixture is then charged with 1M HC1 to
- the chiral purity should be about 98% at this stage.
- the organic layer is
- the product may be analyzed for purity. Should the product be significantly less than about 90% pure, the product can be chromatographed over silica using 20% ethyl acetate/hexanes. Under these preferable conditions, yields of between 60 and 88% of compound XIV are attainable.
- the conversion of the compound of formula X1N to that of compound of formula XV by reacting it with the compound of formula XVI may be carried using any suitable method, reagents and reaction conditions.
- the compound of formula XIV is first reacted with an alkali metal hydride before reacting it with the compound of formula XVI. More preferably
- the alkali metal hydride is sodium hydride.
- Any suitable hydrogenolysis method may be used to convert compound XV to compound XVH.
- palladium hydrogenolysis under pressure is used.
- any suitable reaction conditions may be used in the acylation of compound XVH.
- the method and some or all of the reagents and reaction conditions disclosed hereinafter are utilized.
- the crude compound of formula XV is dissolved in methylene chloride and cooled to about 0° C (internal temperature) by any suitable means, for example, using an ice/salt bath under a blanket of argon.
- the solution is charged with the compound of formula R 20 -X as a liquid. More preferably, R 0 -X is R 20 -C1.
- Diisopropylethyl amine is then added slowly. The reaction is allowed to slowly warm to room temperature.
- the reaction may be
- enzymatic hydrolysis is important as opposed to hydrolysis under standard conditions, because it produces compound HA with less than 5% epimer at the carbon linking the
- R 7 and R 8 groups Any suitable apparatus may be used in the enzymatic hydrolysis
- a continuous membrane reactor is used. More preferably, the
- continuous membrane reactor of the present invention is used as disclosed hereinafter.
- porcine pancrease lipase is used as the enzyme to hydrolyze compound XVIH. More preferably, the enzymatic hydrolysis is conducted at a pH of about 7.2 at a temperature of between about 37-40° C.
- Another aspect of the present invention is the preparation of the compounds of formula HA by a process comprising the steps of:
- the reaction mixture preferably maintained under about -68° C.
- Any suitable means for cooling the reaction mixture may be used.
- the cooling means may be a dry ice bath. After stirring for at least about 55 minutes the reaction mixture may be removed from the cooling means.
- An acid is then added to the reaction mixture to quench the reaction. More preferably, the acid is 1M HC1, the acid is added slowly, and the temperature of the reaction mixture is maintained at under about 25° C during the addition of the acid.
- the organic layer of the quenched reaction mixture is then separated and washed. More preferably, the organic layer is washed with saturated sodium bicarbonate and
- the organic layer is then dried and concentrated to yield the compound of formula XX. More preferably, magnesium sulfate is used as the drying agent. To prevent decomposition of the compound of formula XX, the compound is more preferably stored in a refrigerator.
- the solution of NaH in THF More preferably, the solution of NaH in THF is maintained at about -10° C whilst the compound of formula XX is added to it.
- reaction may be monitored by observing the disappearance of the starting materials
- HPLC may be used to monitor the progress of the reaction.
- the reaction mixture is then stirred for about 48 hours before MTBE is
- the acid is 1M HC1.
- the organic layers are then combined, dried, filtered and concentrate to yield the compound of formula XXI. More preferably, the combined organic layer is dried in magnesium sulfate and filtered through a short pad of silica gel.
- the method for converting the compound of formula XXI to the compound of formula XXIH utilizes some or all of the reagents and reaction conditions disclosed below.
- the compound of formula XXI is dissolved in a degassed mixture of THF and concentrated acid. More preferably, the concentrated
- compound of formula HA utilizes some or all of the reagents and reaction conditions
- the compound of formula XXIH is dissolved in dioxane, followed by the addition of diisopropylethylamine to form a suspension at 0°
- R 0 -X is R 20 -C1.
- the reaction mixture is then stirred for at least about 1
- the compound of formula HA may then be purified by any means known to
- the compound may be purified by recrystallization and/or chromatography.
- the present invention also relates to an improved process for the preparation of
- the compound of formula XXH is an important starting material for use in the process for preparing the compound of
- the method for converting the compound of formula XXIV to the compound of formula XXV utilizes some or all of the reagents and reaction conditions
- reaction mixture about 30° C to form a reaction mixture.
- Benzyl bromide is then added to the reaction mixture which is then stirred for at least about 65 hours.
- MTBE is then added to the reaction mixture and stirred for about 5 minutes.
- the reaction mixture is then filtered through a short pad of silica gel to remove most of a triethylamine salt which precipitates out of the reaction mixture. Then the silica gel is washed with MTBE before the filtrates are combined. The combined filtrate is then washed. More
- the filtrate is washed with 1M HC1, saturated sodium bicarbonate and brine. Then the filtrate is dried in magnesium sulfate, filtered through a short pad of silica gel and concentrated to give the compound of formula XXV.
- XXV may be recrystalized to give a crystalline product.
- the method for converting the compound of formula XXV to the compound of formula XXH utilizes some or all of the reagents and reaction conditions
- Tf 2 O is added to the solution of the compound of formula XXV in methylene chloride, followed by the slow addition of 2,6-lutidine.
- reaction is exothermic the temperature of the reaction mixture is preferably maintained
- reaction mixture the reaction mixture is stirred and allowed to warm for about 1 hour.
- the present invention also relates to novel compounds falling within the scope the compounds of formulae HA; XVIH; XVH; XV; TUB and HIA respectively.
- These particular compounds set forth below are particularly useful as intermediates in the process of the present invention to synthesize particularly useful antipicornaviral compounds of the general formula I, including AG7088:
- Another aspect of the present invention relates to improved processes for
- R 10 is a halogen or an alkyl group; comprising the steps of:
- Step A converting a compound of formula VI to a compound of formula V comprising the substeps of: (a) reacting a Rio substituted benzaldehyde of formula VI:
- Step B the enzymatic reduction of the compound of formula V to a compound of formula VH;
- Optional step C an esterification of the compound of formula VH to a compound of formula XH by reacting the compound of formula VH with a compound of formula
- R"-OH wherein R" is an alkyl or aryl
- step D the conversion of the compound of formula XH to the compound of
- the preferred amines have boiling points above that of the aqueous medium used.
- particularly preferable amine is l-amino-2-propanol.
- l-amino-2-propanol is particularly preferable.
- the alkali metal hydroxide used is sodium hydroxide.
- the molar ratios of sodium hydroxide to hydantoin are individually 5:1,
- the present invention also discloses that the addition of an alkali metal halide to the alkali metal hydroxide-treated solution increases the precipitation of
- the alkali metal halide is sodium chloride.
- sodium chloride When sodium chloride is used, almost all the sodium phenylpyruvate precipitates out as monohydrated sodium
- the collected monohydrated alkali-metal phenylpyruvate precipitate Preferably, the collected monohydrated alkali-metal phenylpyruvate precipitate
- washing agent Any suitable washing agent known in the art may be selected.
- a washing agent known in the art may be selected.
- a washing agent Preferably a
- the washing agent is methanol because the monohydrated alkali-metal phenylpyruvate precipitate is
- Step B Any suitable enzyme known in the art may be used in Step B to catalyze the
- the reduction reaction is a reduction reaction of the compound of formula V.
- the reduction reaction is a reduction reaction of the compound of formula V.
- Any suitable enzymatic reduction method known in the art may be used.
- the MEEC membrane-enclosed enzymatic catalysis method
- step B involves more than a small scale preparation
- a continuous membrane reactor is employed. More preferably, the continuous membrane reactor of the present invention is used.
- reagents and conditions preferably all or some of the following reagents and conditions are used: 1% NAD, 4 equivalents of ammonium formate, a pH of 7.3-7.4 for the effluents and a pH of 6.2-
- FDH/LDH 20/200 (U/mL) and lmM mercaptoethanol are used.
- the coimmobilization method is used, it is preferably carried out in four
- the first step is the preparation of N-acryloxysuccinimide.
- the second step is the preparation of N-acryloxysuccinimide.
- the copolymer is PAN 500 which may be prepared by a radical coploymerization.
- PAN 500 is a water soluble copolymer of
- the third step is the coimmobilization of the enzymes.
- the enzymes are formate dehydrogenase and lactate
- the fourth step is the enzymatic reduction of the reduction of the compound of formula V to give the compound of formula VH.
- the compound of formula VH may be isolated at this stage of the process and used in the process disclosed above for preparing the compound of formula HA.
- the compound of formula VH may be used to prepare the compound of formula XVIA as disclosed below.
- the present invention also discloses that if enantiomeric forms of a compound of formula VH is sought, the use of D-lactate dehydrogenase in Step B described above will yield an enantiomer of formula VHA:
- esterification reaction of optional step C may be performed with any one of
- esterification is performed at about room temperature in the presence of hydrochloric acid and dioxane.
- the enantiomers VHA and VHB may be converted to enantiomers
- Any suitable method may be used to convert the compound of formula XH to the compound of formula XVIA in optional step D of the present process.
- enantiomers XHA and XHB may be
- the second of the processes for preparing compounds of formulae VH and XVIA comprises the steps of:
- Step A' converting serine to the compound of formula VH comprising the substeps of: (a) converting serine to potassium glycidate by a standard process;
- step B' an esterification of the compound of formula V ⁇ to a compound of
- R"-OH wherein R" is an alkyl or aryl
- Optional step C the conversion of the compound of formula XH to the compound of
- serine is reacted with nitric acid at a suitable temperature to yield
- the nitrous acid comprises a
- alkali metal halide Any suitable alkali metal halide known in the art may be used. However, preferably, the alkali metal halide is potassium bromide or sodium bromide.
- the 2-bromo 3-hydroxy propanoic acid is then converted to potassium glycidate by reacting it with potassium hydroxide.
- the reaction is run at between about -40°C and room temperature.
- the present invention also discloses that the use of enantiomeric L-serine or D-serine as the starting material in the process described above will yield D-potassium glycidate and L-potassium glycidate respectively.
- the potassium glycidate from the process disclosed above may be converted directly into the compound of formula VH. Reacting potassium glycidate with a compound of formula Rio-phenyl-Q will cause a regioselective epoxide ring-opening
- Q is an -MgBr group and the regioselective ring-opening reaction is performed at between about -10°C and room temperature in the presence of copper
- the potassium glycidate may first be converted to glycidic acid before being converted
- the potassium glycidate may be converted to glycidic acid by any method known to
- the glycidic acid is prepared by reacting the
- H enantiomeric potassium glycidate is used in the methods described above, the
- the compound of formula VH may be isolated for use in the process disclosed above for preparing the compound of formula HA.
- the compound of formula VH may be used in the process disclosed below to prepare the
- Optional steps B' and C correspond to optional steps C and D of the first disclosed process for synthesizing the compound of formula XVIA from a compound of formula VI respectively.
- formula XVIA specifically a compound of formula XVIB, comprises the steps of:
- Step A' ' the preparation of a compound of formula XHA from a compound of formula
- Step B the conversion of the compound of formula XHA to the compound of formula
- the asymmetric dihydroxylation is a Sharpless asymmetric
- the palladium-mediated reduction step, Step A' ' (c) is performed by reacting the compound of formula XI with a mixture of hydrogen, palladium and
- Step B" corresponds to optional step D of the herein first disclosed process for synthesizing the compounds of formula XVIA from a compound of formula VI.
- Step B the same method, reagents, and reaction conditions disclosed for use in optional step D are preferably also used in Step B".
- the present invention also relates to the compounds of formula IV A, falling within the scope of the genus defined by formula IV as recited above. Accordingly, the compounds of formula IVA will also be useful intermediates in the processes of the present invention for the preparation of compounds of formula I.
- the present invention relates to a compound of formula IVA:
- Y is OH, OSO CF 3 , OSO 2 CH 3 , OSO 2 (p-tolyl), halide or any other leaving group;
- R' is H, alkyl or aryl group.
- Rio is a 4-fluoro group
- Y is OH or OTf
- R' is OH or Me.
- the present invention also relates to a continuous
- the continuous membrane reactor of the present invention is suitable for use in any reaction in which a catalyst of a relatively large molecular size is employed,
- the continuous membrane reactor of the present invention is of use in those catalytic reactions in which there is a desire to recycle the catalyst.
- the reactor of the present invention is useful for use in enzymatic reduction reactions utilizing either chemical or bio-catalysts.
- the continuous membrane reactor of the present invention having a reactor volume comprises a tangential flow filter unit, a reactor loop to circulate the reagents through the tangential flow filter, and a substrate feed pump for feeding the substrate into the reactor loop, wherein the reactor loop comprises:
- the tangential flow unit comprises a tangential flow membrane filter and a unit
- Any suitable tangential flow unit may be used.
- a suitable tangential flow unit may be used.
- tangential flow unit is one which allows the desired product, or permeate, to pass
- tangential flow unit is the Pellicon 2 Module commercially available from Millipore Corporation.
- the Pellicon 2 Module employs a cassette style
- the reactor loop in which the majority of the catalyzed reaction occurs, has an
- the internal volume is defined by the volume of reagents and catalyst the reactor loop can hold.
- the reactor volume is defined by the volume of reagents and
- the reactor loop of the reactor of the present invention has an internal volume of at least
- the reactor loop has an internal volume of at least about 60% of the reactor volume. More preferably, the reactor loop has an internal volume of at least about 70% of the reactor volume. Even more preferably, the reactor loop has an internal volume of at least about 80% of the reactor volume. In a more preferred embodiment of the present invention, the reactor loop has an internal
- the reactor loop has an internal volume of at least about 95%
- the reactor loop comprises a tube of any suitable size and made from any
- the reactor loop comprises tubing which is flexible.
- Flexible tubing allows for the tubing to be cut to any desired length as a means for
- tubing materials include polyethylene, polypropylene, polyurethane, polyvinyl, vinyl, nylon, butylene-polymer,
- silicone PTFE silicone PTFE, ETFE, PFA, Viton®, stainless steel, glass, PVDF, Teflon®, an alkyl
- Viton® is commercially available from Dupont
- silicon does tend to swell when used in the processes of the present invention which can lead to a fluctuation in the reaction conditions due to the consequential change in the residence time.
- Any suitable circulation pump and substrate feed pump may be employed in the reactor loop.
- suitable circulation pumps include peristaltic, bellows,
- diaphragm progressive cavity, piston, flexible linear, nutating disc, membrane, rotary lobe, flexible impeller, rotary vane, or any variable speed low shear type pump.
- a peristaltic, flexible linear, nutating disc, or membrane pump is used.
- suitable as the circulating pump or substrate feed pump is a gear type pump.
- the substrate feed pump operates at a greater speed than the circulation
- the reaction performs most efficiently if the substrate feed
- the reactor loop also comprises any of the following: a bubble trap, a
- the continuous membrane reactor comprises one or more substrate feed
- lines which comprise a substrate feed pump, and also more preferably comprise a check valve, a sterile filter, and a pressure gage.
- a preferred continuous membrane reactor is depicted in figure 1.
- a more preferred continuous membrane reactor of the present invention is depicted in figure 2, parts 1 and 2.
- Table 1 list of the parts of the continuous membrane reactor depicted in figure 2
- time is typically 3 hours.
- the solution was held at 0° C for 3 or more hours. It is important to maintain 0° C during and after the addition for at least this stipulated time
- reaction mixture was then warmed to ambient temperature over about 5 hours and held overnight. At this stage a white solid product, was seen floating in the
- Either the MEEC method (procedure Bl) or coimmobilization method (procedure B2) may be used to prepare 1A.
- Procedure Bl Preparation of 1A using the MEEC method Raw material Source(catalog #) Amount MW Moles
- tubing's (ca. 2 mL each) using an Eppendorf pipette. The other ends of the tubing's were tied and suspend in the reaction mixture. (Note: care was taken to exclude as
- Tris buffer pH 7.5, 5 mM
- N-acryloxysuccinimide The second was the preparation of PAN 500 by a radical copolymerization. The third was a coimmobilization of FDH and D-LDH. The last
- Step 1 Preparation of N-acryloxysuccinimide Raw material Source Amount MW Moles
- Step 3 coimmobilization of FDH and D-LDH Raw material Source Amount MW Moles triethylenetetramine
- NAD Sigma (N 7004) 167 mg 663.4 0.00025 sodium formate Sigma (S 2140) 4.10g 68.01 0.060 mercaptoethanol Sigma (M 6250) 19.5mg 78.13 0.00025
- the enzyme-containing gels can be reused by storage at 4° C in 50 mL of 5 mM
- Tris buffer pH 7.5, 5 mM dithiothreitol
- reaction mixture was heated to about 98°C. This solution was then carefully added to the yellow slurry. The reaction mixture was then refluxed for about 3 hours, before being allowed to cool to room temperature. Again the reaction mixture was monitoring by HPLC (254 nm) for the complete disappearance of the condensed intermediate peak. The resulting reaction mixture was in the form of a transparent orange/yellow solution.
- reaction mixture was cooled to about 20° C ⁇ 5° C, sodium chloride was added and the reaction mixture agitated. While maintaining the coolant flow a pH probe was inserted and concentrated hydrochloric acid added to adjust the pH to
- reaction temperature was maintained at a temperature under about 30° C by regulating the rate of acid addition. After about 4 hours, the resulting reaction mixture, in the form of a pale yellow slurry,
- Step B Preparation of compound 1A using the continuous membrane reactor of the present invention.
- the pH was then adjusted to about 6.2 to yield a substrate solution.
- the enzymes (Formate Dehydrogenase and Lactic Dehydrogenase) were then dissolved in 600 mL of the substrate solution.
- the substrate solution containing the enzymes was then put into the reactor by feeding the solution through the substrate feed line of the reactor.
- the remainder of the substrate mixture was then pumped into the reactor at a
- the feed rate may be adjusted as necessary to vary the conversion or throughput rate as desired.
- reaction mixture between 0° and 5° C to form a reaction mixture.
- the reaction mixture about was then
- the reaction was monitored by TLC (50% THF/hexanes, with ceric sulfate, phosphomolybdic acid stain) and HPLC (gluco method). The catalyst was then filtered
- DIPEA (2.1eq.) d 0.742 Aldrich 133 mL 129.3 0.764
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US15036599P | 1999-08-24 | 1999-08-24 | |
US150365P | 1999-08-24 | ||
PCT/US2000/023032 WO2001014576A2 (en) | 1999-08-24 | 2000-08-23 | Process and intermediates for the preparation of isoxazolecaroxamides and analogues |
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JP (1) | JP2003511350A (xx) |
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CN (2) | CN1524960A (xx) |
AU (1) | AU778062B2 (xx) |
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CA (1) | CA2376509A1 (xx) |
CZ (1) | CZ2002634A3 (xx) |
HK (1) | HK1051363A1 (xx) |
HU (1) | HUP0203315A3 (xx) |
IL (1) | IL147862A0 (xx) |
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DE69910762T2 (de) | 1998-04-30 | 2004-03-11 | Agouron Pharmaceuticals, Inc., La Jolla | Antipicornavirale verbindungen, deren herstellung und verwendung |
PL354030A1 (en) | 1999-08-04 | 2003-12-15 | Agouron Pharmaceuticals, Inc.Agouron Pharmaceuticals, Inc. | Antipicornaviral compounds and compositions, their pharmaceutical uses, and materials for their synthesis |
US6774243B2 (en) | 1999-08-24 | 2004-08-10 | Agouron Pharmaceuticals, Inc. | Efficient synthetic routes for the preparation of rhinovirus protease inhibitors and key intermediates |
PE20020157A1 (es) | 1999-12-03 | 2002-02-22 | Agouron Pharma | Compuestos derivados de piridona como inhibidores de proteasas de picornaviral 3c, composiciones, sus usos farmaceuticos y materiales para su sintesis |
PE20011277A1 (es) | 2000-04-14 | 2002-01-07 | Agouron Pharma | Compuestos y composiciones antipicornavirales, sus usos farmaceuticos y los materiales para su sintesis |
CN1525957A (zh) | 2000-06-14 | 2004-09-01 | ������ҩ������˾ | 抗细小核糖核酸病毒的化合物与组合物,它们的药物用途,以及用于其合成的物质 |
DE10208007A1 (de) * | 2002-02-26 | 2003-09-18 | Forschungszentrum Juelich Gmbh | Verfahren zur Herstellung von Alkoholen aus Substraten mittels Oxidoreduktasen, Zweiphasensystem umfassend eine wässrige Phase und eine organische Phase sowie Vorrichtung zur Durchführung des Verfahrens |
CN106831657B (zh) * | 2017-02-23 | 2019-07-16 | 江苏工程职业技术学院 | 一种环氧丙酸钾的制备方法 |
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DE2426651C3 (de) * | 1974-06-01 | 1982-04-08 | Bayer Ag, 5090 Leverkusen | (-)-Antipode des 3-(p-Chlorphenyl)-2-chlorpropionsäuremethylesters, Verfahren zu dessen Herstellung sowie dessen Verwendung als Herbizid |
DE2930087A1 (de) * | 1979-07-25 | 1981-02-26 | Biotechnolog Forschung Gmbh | Verfahren zur kontinuierlichen enzymatischen umwandlung von wasserloeslichen alpha -ketocarbonsaeuren in die entsprechenden alpha -hydroxycarbonsaeuren |
JPH0623131B2 (ja) * | 1984-08-07 | 1994-03-30 | 三井東圧化学株式会社 | α−ケト酸のアルカリ金属塩の製造法 |
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FR2686897B1 (fr) * | 1992-02-05 | 1995-07-13 | Sonertec | Procede en continu de fabrication d'acides organiques. |
US5360927A (en) * | 1994-01-24 | 1994-11-01 | Development Center For Biotechnology | Process for the preparation of monohydrated sodium phenylpyruvate |
US5869697A (en) * | 1994-05-02 | 1999-02-09 | Council Of Scientific & Industrial Research | Process for preparing diltiazem |
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CN1524960A (zh) | 2004-09-01 |
CN1157391C (zh) | 2004-07-14 |
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HK1051363A1 (en) | 2003-08-01 |
AU6797000A (en) | 2001-03-19 |
WO2001014576B1 (en) | 2001-09-27 |
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CN1382139A (zh) | 2002-11-27 |
HUP0203315A3 (en) | 2003-12-29 |
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JP2003511350A (ja) | 2003-03-25 |
CA2376509A1 (en) | 2001-03-01 |
CZ2002634A3 (cs) | 2002-09-11 |
WO2001014576A2 (en) | 2001-03-01 |
IL147862A0 (en) | 2002-08-14 |
ZA200200506B (en) | 2003-06-25 |
AU778062B2 (en) | 2004-11-11 |
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