WO2006082228A1 - Method for synthesising cysteine derivatives, in particular thio carbaesters used in the form of intermediate products in drug synthesis - Google Patents
Method for synthesising cysteine derivatives, in particular thio carbaesters used in the form of intermediate products in drug synthesis Download PDFInfo
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- C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
- C07C319/14—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides
- C07C319/20—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of sulfides by reactions not involving the formation of sulfide groups
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- the invention relates to a new process for the preparation of cysteine derivatives, in particular thiocarbaester derivatives, in particular N-benzyloxycarbonyl-S-phenyl-L-cysteine methyl ester.
- cysteine derivatives are useful as intermediates in the synthesis of several pharmaceutically active compounds.
- thiocarbaester is involved in the synthesis of nelfmavir, an active anti-AIDS product of the class of HIV protease inhibitors (WO96 / 23756 and EP 604 185).
- the methods for synthesizing cysteine derivatives use three synthetic routes using, as raw materials, an esterified serine derivative whose amino function is protected by an appropriate radical (Z-Ser-OMe), a derivative of cysteine whose amino function is protected by a suitable radical and the thiol function is substituted by a phenyl radical (Z-Cys (Ph) -OH), or an esterified cysteine derivative whose amino function is protected by an appropriate radical (Z-Cys (H) -OMe).
- Z-Ser-OMe an esterified serine derivative whose amino function is protected by an appropriate radical
- Z-Cys (Ph) -OH a derivative of cysteine whose amino function is protected by a suitable radical and the thiol function is substituted by a phenyl radical
- Z-Cys (H) -OMe an esterified cysteine derivative whose amino function is protected by an appropriate radical
- Z represents a protective group for the amine function, in particular the benzyloxycarbonyl radical.
- the first synthetic route described involves a derivative of serine as a raw material: Z-Ser-OMe.
- the alcohol function of serine is then activated as a mesylate derivative in the presence of mesyl chloride before reacting with sodium thiophenate to yield thiocarbaester.
- This chemical route has been described for the first time by the team of the University of Nottingham in J. Chem. Soc; Perkin Trans. 1, 15, (1997), 2179-2187 and Tetrahedron Letters, 34 (41), (1993), 6607-6610.
- Patent applications EP 0 897 911 and US2002 / 008688 describe the synthesis of thiocarbaester from derivatives of serine Z-Ser-OMe. Processes displacing hydroxyl from serine, substitution of the hydroxyl radical or a leaving group by a thiophenyl radical, are of little economic interest because they employ elaborate reagents such as methanesulfonyl chloride. (US2002 / 008688) and they are also difficult to control, because of significant risks of elimination of the desired product in dehydroalanine and the risks of racemization.
- the second synthetic route described involves a derivative of cysteine as raw material: Z-Cys (Ph) -OH.
- the carboxylic acid function of the cysteine is then esterified.
- the protective group of the amino function Z is generally introduced under the Schotten-Bauman conditions carried out in an aqueous medium, which implies a careful isolation and drying of the intermediate product Z-
- the patent application EP 1 054 000 which describes this second synthetic route, teaches that it is preferable to carry out the protection of the amine function followed by the esterification reaction of the carboxylic function, in particular to avoid the formation of impurities such as N-benzyl-phenylcysteine methyl ester or dehydroalanine.
- the third route of synthesis described involves a derivative of cysteine as a raw material: Z-Cys (H) -OMe.
- the fhiol function of the cysteine derivative is then substituted with a phenyl radical.
- Methods for introducing a phenyl group onto cysteine are known methods such as the reaction of cysteine with a phenyldiazonium salt (J. Org.
- Another process for the synthesis of cysteine derivatives uses as raw material an alkyl derivative of cysteine (S-methylcysteine, S-hepylecysteine, S-hexyl cysteine).
- This alkyl derivative of cysteine is first esterified in the presence of methanol and an acid (HCl gas or SOCl 2 ). The esterification reaction is carried out at room temperature or at cold temperature (-10 ° C.).
- the amine function is then protected by a suitable protecting group. To do this, said isolated hydrochloride is reacted in a second reactor with said appropriate protective group.
- cysteine derivatives in particular thiocarbaester, using as starting material cysteine, the thiol function of which is substituted with an alkyl or aryl radical.
- the subject of the invention is therefore a process for the synthesis of cysteine derivatives of formula 1
- R 1 represents an alkyl radical
- R 2 represents a radical chosen from the group consisting of alkyl and aryl radicals
- R 3 represents a radical chosen from the group consisting of alkyl, aryl and arylalkyl radicals, characterized in that comprises the following successive steps: a) esterification of the compound of formula II
- alkyl denotes a hydrocarbon residue with a straight or branched chain containing from 1 to 10 carbon atoms, advantageously from 1 to 6 carbon atoms, more advantageously from 1 to 4 carbon atoms. such as methyl, ethyl, propyl, isopropyl and butyl, more preferably ethyl, propyl, isopropyl and butyl.
- aryl denotes an aromatic carbocyclic residue containing from 6 to 10 carbon atoms.
- aryl radical there may be mentioned phenyl and naphthyl, advantageously phenyl.
- aralkyl denotes a hydrocarbon residue containing from 1 to 6 carbon atoms bonded to an aryl radical, as defined above.
- an aralkyl radical there may be mentioned in particular benzyl and phenethyl.
- Steps a) and b) are carried out in one and the same reactor. This means that the compound of formula IV is not isolated. This is called “one pot” synthesis.
- Ri preferably represents an alkyl radical, linear or branched Ci -C O, even more preferably methyl.
- R 2 preferably represents an aryl radical C 6 -C O, still more preferably phenyl.
- R 3 advantageously represents the benzyl radical.
- the compound of formula I represents the compound of formula Ia below: in which R 1 and R 2 have the same meaning as for the compound of formula I.
- the process according to the invention advantageously makes it possible to conserve the enantiomer of the starting compound, more particularly of cysteine.
- the compound of formula II is in enantiomerically pure form (R or S)
- the compound of formula I is obtained in the same enantiomeric form.
- the process according to the invention thus makes it possible to obtain derivatives of cysteine, in particular thiocarbaester, with good chiral purity. If the starting compound is in enantiomerically pure form, the desired product is obtained with an enantiomeric excess greater than 90%, advantageously greater than 95%, still more preferably greater than 97%, still more preferably greater than 98%.
- the process according to the invention also makes it possible to obtain derivatives of cysteine, in particular thiocarbaester, with good chemical purity
- the desired product is obtained with a chemical purity greater than 90% by weight, advantageously greater than 95% by weight, and even more advantageously greater than 97% by weight, relative to the total weight of the compounds present.
- the esterification reaction of step a) can advantageously be carried out under anhydrous conditions, to promote the shift of equilibrium from the esterification reaction to the formation of the ester.
- the reaction of step a) can be catalyzed (acid catalysis): it can then be carried out in the presence of an acid, such as hydrochloric acid gas, or an acid chloride, such as thionyl.
- the alcohol of formula III is advantageously also used as a solvent for the esterification reaction of step a).
- the medium is advantageously heated to a temperature of between 40 ° C. and the reflux temperature of the solvent (156 ° C. for hexanol). ), more advantageously between 40 0 C and at a temperature located 5 0 C below the reflux temperature of the solvent, more advantageously between 50 and 60 0 C.
- the heating time of the medium of step a) varies from 2 to 36 hours, advantageously the medium is heated for 2 to 10 hours, even more advantageously for 3 to 5 hours.
- the medium is then cooled to room temperature, advantageously at 20 ° C.
- step a Following step a), excess acid and solvent are advantageously removed and the resulting residue is solubilized in water.
- the amino group may be functionalized by any method known to those skilled in the art.
- the term "functionalization of the amino group” means that the amine function of the compound of formula IV is substituted, under appropriate operating conditions well known to those skilled in the art, to form the compound of formula I.
- Step b) is advantageously carried out in an aqueous and basic medium by adding a compound R 3 OC (O) -X (formula V), in which X represents a halogen atom.
- halogen denotes chlorine, bromine, fluorine or iodine, advantageously fluorine or chlorine.
- the aqueous medium of step b) may also comprise a solvent selected from the group consisting of toluene, ethyl acetate (AcOEt), isopropyl acetate (AcOiPr) and dichloromethane (CH 2 Cl 2 ).
- a solvent selected from the group consisting of toluene, ethyl acetate (AcOEt), isopropyl acetate (AcOiPr) and dichloromethane (CH 2 Cl 2 ).
- the functionalization of the amino group is carried out under Schotten-Bauman conditions, that is to say by reaction of an acid chloride in the presence of alkali and water ( J. March, Advanced Organic Chemistry, p. 392).
- the medium of step b) is advantageously made basic by addition of a strong base such as sodium hydroxide.
- the medium of step b) is advantageously buffered by addition of a weak base, advantageously sodium hydrogencarbonate and / or potassium hydrogen carbonate.
- the pH of the aqueous medium of step b) is thus advantageously adjusted to values between 4 and 7, more advantageously between 5.5 and 6.5, still more advantageously at a value of 6 ⁇ 0.2.
- the addition of the compound of formula V is advantageously carried out at a temperature of between 0 and 20 ° C., advantageously between 0 and 10 ° C., and even more advantageously between 3 and 70 ° C. Then, the medium is advantageously stirred at this temperature for a time varying from 5 minutes to 1 hour, advantageously from 15 to 45 minutes, even more advantageously for about 30 minutes. Finally, the medium is advantageously stirred at ambient temperature (advantageously 20 ° C.) for a time varying from 5 minutes to 1 hour, advantageously from 15 to 45 minutes, even more advantageously for about 30 minutes.
- step b) is carried out by adding benzyl chloroformate in a basic medium in the presence of a weak base, such as sodium hydrogencarbonate and / or potassium hydrogencarbonate.
- a weak base such as sodium hydrogencarbonate and / or potassium hydrogencarbonate.
- the desired product can then be recovered by conventional methods known to those skilled in the art.
- the first step a) consists of preparing the H-Cys (Ph) -OMe, HCl by esterification reaction of the cysteine derivative H-Cys (Ph) -OH in methanol in the presence an acid chloride such as thionyl chloride or an acid such as hydrochloric acid gas. After removing the excess acid and the synthesis solvent, the residue is solubilized in water.
- the functionalization of the amino group (step b)) is carried out by adding benzyl chloroformate in a basic medium in the presence of sodium hydrogen carbonate and / or potassium hydrogen carbonate.
- the process is characterized in that 1 part of H-Cys (Ph) -OH is reacted with 1.2 parts of thionyl chloride in 4 to 10 volumes of methanol. .
- the product is obtained in the organic phase after decantation and precipitation by adding 3 to 5 volumes of heptane and cooling.
- the process according to the invention is characterized by the use of a weak base, during step b), making it possible to work in a buffered medium so as to avoid the secondary reaction of saponification, a reaction generally observed when using a strong base like soda or potash.
- a weak base such as soda or potash.
- the process according to the invention by the pH conditions and the selected temperature conditions avoid the decomposition of the chloroformate which is at the origin of the impurity N-benzyl-phenylcysteine methyl ester.
- the pH and temperature conditions of the process also make it possible to avoid the elimination reaction of thiophenol and thus to avoid the formation of the dehydroalanine impurity.
- the subject of the invention is also the use of the compounds of formula (I), obtained by the process according to the invention, as intermediates in the synthesis of medicinal products, in particular in the synthesis of active anti-AIDS products of the class of HIV protease inhibitors.
- the invention relates to the use of thiocarbaester IaI, obtained by the process according to the invention, as an intermediate product in the synthesis of active anti-AIDS products of the class of HIV protease inhibitors, in particular Nelfinavir. .
- the process according to the invention makes it possible to obtain thiocarbaester IaI with a good yield, a chiral purity of 99.8% and a chemical purity of 99.4%.
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Abstract
Description
Procédé de synthèse de dérivés de la cystéine, notamment du thiocarbaester, utiles en tant que produits intermédiaires dans la synthèse de médicaments Process for the synthesis of cysteine derivatives, especially thiocarbaester, useful as intermediates in drug synthesis
L'invention concerne un nouveau procédé de préparation de dérivés de la cystéine, notamment de thiocarbaester, en particulier du N-benzyloxycarbonyl-S- phényl-L-cystéine méthyl ester.The invention relates to a new process for the preparation of cysteine derivatives, in particular thiocarbaester derivatives, in particular N-benzyloxycarbonyl-S-phenyl-L-cysteine methyl ester.
Les dérivés de la cystéine sont utiles en tant qu'intermédiaires dans la synthèse de plusieurs composés pharmaceutiquement actifs. En particulier, le thiocarbaester entre dans la synthèse du nelfmavir, produit actif anti-sida de la classe des inhibiteurs de la protéase HIV (WO96/23756 et EP 604 185).The cysteine derivatives are useful as intermediates in the synthesis of several pharmaceutically active compounds. In particular, thiocarbaester is involved in the synthesis of nelfmavir, an active anti-AIDS product of the class of HIV protease inhibitors (WO96 / 23756 and EP 604 185).
Dans l'art antérieur, les procédés de synthèse des dérivés de la cystéine font appel à trois voies de synthèse utilisant comme matières premières un dérivé de la serine estérifié dont la fonction aminé est protégée par un radical approprié (Z-Ser-OMe), un dérivé de la cystéine dont la fonction aminé est protégée par un radical approprié et la fonction thiol est substituée par un radical phényle (Z-Cys(Ph)-OH), ou un dérivé de la cystéine estérifié dont la fonction aminé est protégée par un radical approprié (Z-Cys(H)-OMe).In the prior art, the methods for synthesizing cysteine derivatives use three synthetic routes using, as raw materials, an esterified serine derivative whose amino function is protected by an appropriate radical (Z-Ser-OMe), a derivative of cysteine whose amino function is protected by a suitable radical and the thiol function is substituted by a phenyl radical (Z-Cys (Ph) -OH), or an esterified cysteine derivative whose amino function is protected by an appropriate radical (Z-Cys (H) -OMe).
Les dérivés mentionnés précédemment et répondant aux formules Z-Cys(Ph)-OH, Z-Cys(Ph)-OMe et Z-Cys(H)-OMe répondent respectivement aux formules a, b ou c :The derivatives mentioned above and corresponding to the formulas Z-Cys (Ph) -OH, Z-Cys (Ph) -OMe and Z-Cys (H) -OMe respectively correspond to formulas a, b or c:
dans lesquelles Z représente un groupement protecteur de la fonction aminé, notamment le radical benzyloxycarbonyle. in which Z represents a protective group for the amine function, in particular the benzyloxycarbonyl radical.
Les dérivés mentionnés précédemment et répondant aux formules Z-Ser-OH et Z-Ser-OMe répondent respectivement aux formules d ou e : dans lesquelles Z représente un groupement protecteur de la fonction aminé, notamment le radical benzyloxycarbonyle.The derivatives mentioned above and corresponding to the formulas Z-Ser-OH and Z-Ser-OMe respectively correspond to formulas d or e: in which Z represents a protective group for the amine function, in particular the benzyloxycarbonyl radical.
La première voie de synthèse décrite fait intervenir un dérivé de la serine comme matière première : la Z-Ser-OMe. La fonction alcool de la serine est ensuite activée sous forme de dérivé mésylate en présence de chlorure de mésyle avant de réagir avec le thiophénate de sodium pour conduire au thiocarbaester. Cette voie chimique a été décrite pour la première fois par l'équipe de l'université de Nottingham dans les publications J. Chem. Soc ; Perkin Trans. 1, 15, (1997), 2179-2187 et Tétrahedron Letters, 34 (41), (1993), 6607-6610.The first synthetic route described involves a derivative of serine as a raw material: Z-Ser-OMe. The alcohol function of serine is then activated as a mesylate derivative in the presence of mesyl chloride before reacting with sodium thiophenate to yield thiocarbaester. This chemical route has been described for the first time by the team of the University of Nottingham in J. Chem. Soc; Perkin Trans. 1, 15, (1997), 2179-2187 and Tetrahedron Letters, 34 (41), (1993), 6607-6610.
Les demandes de brevet EP 0 897 911 et US2002/008688 décrivent la synthèse du thiocarbaester à partir de dérivés de la serine Z-Ser-OMe. Les procédés effectuant un déplacement de Phydroxyle de la serine, substitution du radical hydroxyle ou d'un groupe partant par un radical thiophényle, sont peu intéressant d'un point de vue économique car ils mettent en œuvre des réactifs élaborés tels que le chlorure de méthanesulfonyle (US2002/008688) et ils sont également difficiles à maîtriser, en raison d'importants risques d'élimination du produit désiré en déhydroalanine et des risques de racémisation.Patent applications EP 0 897 911 and US2002 / 008688 describe the synthesis of thiocarbaester from derivatives of serine Z-Ser-OMe. Processes displacing hydroxyl from serine, substitution of the hydroxyl radical or a leaving group by a thiophenyl radical, are of little economic interest because they employ elaborate reagents such as methanesulfonyl chloride. (US2002 / 008688) and they are also difficult to control, because of significant risks of elimination of the desired product in dehydroalanine and the risks of racemization.
La deuxième voie de synthèse décrite fait intervenir un dérivé de la cystéine comme matière première : la Z-Cys(Ph)-OH. La fonction acide carboxylique de la cystéine est ensuite estérifiée. Le groupement protecteur de la fonction aminé Z est généralement introduit dans les conditions de Schotten-Bauman réalisées en milieu aqueux, ce qui implique un isolement et un séchage soigné du produit intermédiaire Z-The second synthetic route described involves a derivative of cysteine as raw material: Z-Cys (Ph) -OH. The carboxylic acid function of the cysteine is then esterified. The protective group of the amino function Z is generally introduced under the Schotten-Bauman conditions carried out in an aqueous medium, which implies a careful isolation and drying of the intermediate product Z-
Cys(Ph)-OH pour la mise en œuvre de P estérifi cation qui requiert des conditions anhydres.Cys (Ph) -OH for carrying out esterification which requires anhydrous conditions.
La demande de brevet EP 1 054 000, qui décrit cette deuxième voie de synthèse, enseigne qu'il est préférable de réaliser la protection de la fonction aminé suivie de la réaction d'estérification de la fonction carboxylique, notamment pour éviter la formation d'impuretés telles que l'ester méthylique de N-benzyle-phénylcystéine ou la déhydroalanine. La troisième voie de synthèse décrite fait intervenir un dérivé de la cystéine comme matière première : la Z-Cys(H)-OMe. La fonction fhiol, du dérivé cystéine, est ensuite substituée par un radical phényle. Les procédés permettant d'introduire un groupe phényle sur la cystéine sont des procédés connus tels que la réaction de la cystéine avec un sel de phényldiazonium (J. Org. Chem., 23, (1958), 1251) ou la réaction de bromo ou iodobenzène avec la cystéine ou un dérivé de cystéine (Australian J. Chem., 38, (1985), 38 et EP 0 968 997). Ce type de procédé donne des rendements et des puretés médiocres.The patent application EP 1 054 000, which describes this second synthetic route, teaches that it is preferable to carry out the protection of the amine function followed by the esterification reaction of the carboxylic function, in particular to avoid the formation of impurities such as N-benzyl-phenylcysteine methyl ester or dehydroalanine. The third route of synthesis described involves a derivative of cysteine as a raw material: Z-Cys (H) -OMe. The fhiol function of the cysteine derivative is then substituted with a phenyl radical. Methods for introducing a phenyl group onto cysteine are known methods such as the reaction of cysteine with a phenyldiazonium salt (J. Org. Chem., 23, (1958), 1251) or the reaction of bromo or iodobenzene with cysteine or a cysteine derivative (Australian J. Chem., 38, (1985), 38 and EP 0 968 997). This type of process gives poor yields and purities.
Un autre procédé de synthèse de dérivés de la cystéine utilise comme matière première un dérivé alkyle de la cystéine (S-méthylcystéine, S-hepylecystéine, S- hexyl cystéine). Ce dérivé alkyle de la cystéine est dans un premier temps estérifié en présence de méthanol et d'un acide (HCl gaz ou SOCl2). La réaction d'estérification est réalisée à température ambiante ou à froid (-100C). L'hydochlorure de l'ester méthylique de la S-alkyl-cystéine (alkyle= méthyle, hexyle, heptyle), résultant de cette étape d'estérification est ensuite isolé. La fonction aminé est ensuite protégée par un groupement protecteur approprié. Pour ce faire, ledit hydrochlorure isolé est mis à réagir, dans un deuxième réacteur, avec ledit groupement protecteur approprié.Another process for the synthesis of cysteine derivatives uses as raw material an alkyl derivative of cysteine (S-methylcysteine, S-hepylecysteine, S-hexyl cysteine). This alkyl derivative of cysteine is first esterified in the presence of methanol and an acid (HCl gas or SOCl 2 ). The esterification reaction is carried out at room temperature or at cold temperature (-10 ° C.). The hydrochloride of the S-alkyl-cysteine methyl ester (alkyl = methyl, hexyl, heptyl) resulting from this esterification step is then isolated. The amine function is then protected by a suitable protecting group. To do this, said isolated hydrochloride is reacted in a second reactor with said appropriate protective group.
Un tel procédé est par exemple décrit dans les publications suivantes: CH.Such a method is for example described in the following publications: CH.
LEVENSON, design and synthesis of tetrahedral intermediate analogues as potential dihydroorotase inhibitors, J. Med. Chem., 1984, 27, 228-232 ; LEON A.G.M. VAN DENLevenson, design and synthesis of tetrahedral intermediate analogs as potential dihydroorotase inhibitors, J. Med. Chem., 1984, 27, 228-232; LEON A.G.M. VAN DEN
BROEK et al., lipophilic analogues of sparsomycin as strong inhibitors of protein synthesis and tumor growth : a structure-activity relationship study, J Med. Chem, 1989, 32, 2002-BROEK et al., Lipophilic analogues of sparsomycin as strong inhibitors of protein synthesis and tumor growth: a structure-activity relationship study, J Med. Chem, 1989, 32, 2002-
2015 et G. DESIMONI et al, Copper (II) in organic synthesis. XI. Evaluation of the ligand architecture on the efficiency of a copper (II) catalyst for enantioselective Michael reactions, Tetrahedron vol. 51, n°14, pp. 4131-4144, 1995.2015 and G. DESIMONI et al., Copper (II) in organic synthesis. XI. Evaluation of the ligand architecture on the efficiency of a copper (II) catalyst for enantioselective Michael reactions, Tetrahedron vol. 51, No. 14, pp. 4131-4144, 1995.
Ce procédé requiert l'isolation de l'hydochlorure de l'ester méthylique de la S- S- alkyl-cystéine (alkyle= méthyle, hexyle, heptyle). C'est donc un procédé en deux étapes, réalisé dans deux réacteurs différents.This process requires the isolation of the hydochloride from the S-S-alkyl-cysteine methyl ester (alkyl = methyl, hexyl, heptyl). It is therefore a two-step process, carried out in two different reactors.
De plus, ce procédé requiert la réalisation de la réaction d'estérification à une température inférieure ou égale à la température ambiante. Aussi existe t'il un besoin d'un procédé plus économique permettant l'obtention de dérivés de la cystéine, notamment du thiocarbaester, avec une bonne pureté chimique et chirale.In addition, this process requires the completion of the esterification reaction at a temperature below or equal to room temperature. There is also a need for a more economical process for obtaining derivatives of cysteine, especially thiocarbaester, with good chemical and chiral purity.
Or, les inventeurs ont découvert, d'une manière surprenante, qu'il était possible de réaliser la synthèse « one pot » de dérivés de la cystéine, notamment du thiocarbaester, en utilisant comme produit de départ la cystéine, dont la fonction thiol est substituée par un radical alkyle ou aryle.However, the inventors have discovered, surprisingly, that it is possible to carry out the "one pot" synthesis of cysteine derivatives, in particular thiocarbaester, using as starting material cysteine, the thiol function of which is substituted with an alkyl or aryl radical.
L'invention a donc pour objet un procédé de synthèse de dérivés de la cystéine de formule 1The subject of the invention is therefore a process for the synthesis of cysteine derivatives of formula 1
dans laquelle Ri représente un radical alkyle, R2 représente un radical choisi dans le groupe constitué par les radicaux alkyles, aryles et R3 représente un radical choisi dans le groupe constitué par les radicaux alkyles, aryles et arylalkyles, caractérisé en ce qu'il comprend les étapes successives suivantes : a) estérification du composé de formule II in which R 1 represents an alkyl radical, R 2 represents a radical chosen from the group consisting of alkyl and aryl radicals, and R 3 represents a radical chosen from the group consisting of alkyl, aryl and arylalkyl radicals, characterized in that comprises the following successive steps: a) esterification of the compound of formula II
avec un alcool de formule III with an alcohol of formula III
Ri-OH pour former le composé de foπnule IVR 1 -OH to form the compound of formula IV
les radicaux Ri et R2 ayant la même signification que pour le composé de formule I, b) puis, fonctionnalisation du groupement amino (du composé de formule IV) pour donner le composé de formule I, les étapes a) et b) étant réalisées dans un seul et même réacteur. Dans le cadre de la présente invention, le terme « alkyle » désigne un résidu hydrocarboné à chaîne droite ou ramifiée contenant de 1 à 10 atomes de carbone, avantageusement de 1 à 6 atomes de carbone, encore plus avantageusement de 1 à 4 atomes de carbone, tel que le méthyle, l'éthyle, le propyle, Pisopropyle et le butyle, plus avantageusement l'éthyle, le propyle, Pisopropyle et le butyle. the radicals R 1 and R 2 having the same meaning as for the compound of formula I, b) and then functionalization of the amino group (of the compound of formula IV) to give the compound of formula I, the steps a) and b) being carried out in one and the same reactor. In the context of the present invention, the term "alkyl" denotes a hydrocarbon residue with a straight or branched chain containing from 1 to 10 carbon atoms, advantageously from 1 to 6 carbon atoms, more advantageously from 1 to 4 carbon atoms. such as methyl, ethyl, propyl, isopropyl and butyl, more preferably ethyl, propyl, isopropyl and butyl.
Dans le cadre de la présente invention, le terme « aryle » désigne un résidu carbocyclique aromatique contenant de 6 à 10 atomes de carbone. Comme exemple de radical aryle, on peut notamment citer le phényle et le naphtyle, avantageusement le phényle. Dans le cadre de la présente invention, le terme « aralkyle » désigne un résidu hydrocarboné contenant de 1 à 6 atomes de carbone lié à un radical aryle, tel que défini précédemment. Comme exemple de radical aralkyle, on peut notamment citer le benzyle et le phénéthyle.In the context of the present invention, the term "aryl" denotes an aromatic carbocyclic residue containing from 6 to 10 carbon atoms. As an example of an aryl radical, there may be mentioned phenyl and naphthyl, advantageously phenyl. In the context of the present invention, the term "aralkyl" denotes a hydrocarbon residue containing from 1 to 6 carbon atoms bonded to an aryl radical, as defined above. As an example of an aralkyl radical, there may be mentioned in particular benzyl and phenethyl.
Les étapes a) et b) sont réalisées dans un seul et même réacteur. Cela signifie que le composé de formule IV n'est pas isolé. On parle alors de synthèse « one pot ».Steps a) and b) are carried out in one and the same reactor. This means that the compound of formula IV is not isolated. This is called "one pot" synthesis.
On considérait que les réactifs, solvants et sous-produits éventuels présents dans la première étape devaient être éliminés pour avoir un bon rendement et une bonne pureté du produit final. Or, la réalisation des étapes a) et b) dans un même réacteur (sans isolation du composé de formule IV et donc sans élimination des impuretés, solvants, réactifs de départ n'ayant pas réagi) n'affecte pas le rendement total du procédé (il est en effet comparable au rendement obtenu lorsque le composé IV est isolé) ni la pureté du produit final.The reagents, solvents and potential byproducts present in the first stage were considered to be removed for good yield and purity of the final product. However, performing steps a) and b) in the same reactor (without isolation of the compound of formula IV and thus without removal of impurities, solvents, unreacted starting reagents) does not affect the total yield of the process (It is indeed comparable to the yield obtained when compound IV is isolated) nor the purity of the final product.
Ri représente avantageusement un radical alkyle, linéaire ou ramifié, en Ci -CO, encore plus avantageusement le radical méthyle. R2 représente avantageusement un radical aryle en C6-CiO, encore plus avantageusement le phényle.Ri preferably represents an alkyl radical, linear or branched Ci -C O, even more preferably methyl. R 2 preferably represents an aryl radical C 6 -C O, still more preferably phenyl.
R3 représente avantageusement le radical benzyle.R 3 advantageously represents the benzyl radical.
Selon une variante avantageuse de l'invention le composé de formule I représente le composé de formule Ia suivante : dans laquelle Ri et R2 ont la même signification que pour le composé de formule I.According to an advantageous variant of the invention the compound of formula I represents the compound of formula Ia below: in which R 1 and R 2 have the same meaning as for the compound of formula I.
Le procédé selon invention permet avantageusement de conserver l'énantiomérie du composé de départ, plus particulièrement de la cystéine. Ainsi lorsque le composé de formule II est sous une forme énantiomériquement pure (R ou S), le composé de formule I est obtenu sous la même forme énantiomérique.The process according to the invention advantageously makes it possible to conserve the enantiomer of the starting compound, more particularly of cysteine. Thus, when the compound of formula II is in enantiomerically pure form (R or S), the compound of formula I is obtained in the same enantiomeric form.
Le procédé selon l'invention permet donc l'obtention de dérivés de la cystéine, notamment du thiocarbaester, avec une bonne pureté chirale. Si le composé de départ est sous une forme énantiomériquement pure, le produit désiré est obtenu avec un excès énantiomérique supérieur à 90%, avantageusement supérieur à 95%, encore plus avantageusement supérieur à 97%, encore plus avantageusement supérieur à 98%.The process according to the invention thus makes it possible to obtain derivatives of cysteine, in particular thiocarbaester, with good chiral purity. If the starting compound is in enantiomerically pure form, the desired product is obtained with an enantiomeric excess greater than 90%, advantageously greater than 95%, still more preferably greater than 97%, still more preferably greater than 98%.
Le procédé selon l'invention permet également l'obtention de dérivés de la cystéine, notamment du thiocarbaester, avec une bonne pureté chimiqueThe process according to the invention also makes it possible to obtain derivatives of cysteine, in particular thiocarbaester, with good chemical purity
Le produit désiré est obtenu avec une pureté chimique supérieure à 90% en poids, avantageusement supérieure à 95% en poids, encore plus avantageusement supérieur à 97% en poids, par rapport au poids total des composés présents.The desired product is obtained with a chemical purity greater than 90% by weight, advantageously greater than 95% by weight, and even more advantageously greater than 97% by weight, relative to the total weight of the compounds present.
La réaction d'estérification de l'étape a) peut avantageusement être réalisée dans des conditions anhydres, pour favoriser le déplacement de l'équilibre de la réaction d'estérification vers la formation de l'ester. La réaction de l'étape a) peut être catalysée (catalyse acide) : elle peut alors être réalisée en présence d'un acide, tel que l'acide chlorhydrique gaz, ou d'un chlorure d'acide, tel que le chlorure de thionyle. L'alcool de formule III est avantageusement également utilisé comme solvant de la réaction d'estérification de l'étape a).The esterification reaction of step a) can advantageously be carried out under anhydrous conditions, to promote the shift of equilibrium from the esterification reaction to the formation of the ester. The reaction of step a) can be catalyzed (acid catalysis): it can then be carried out in the presence of an acid, such as hydrochloric acid gas, or an acid chloride, such as thionyl. The alcohol of formula III is advantageously also used as a solvent for the esterification reaction of step a).
Lors de la réaction d'estérification de l'étape a), suite à l'ajout des réactifs, le milieu est avantageusement chauffé à une température comprise entre 400C et la température de reflux du solvant (156°C pour l'hexanol), plus avantageusement entre 400C et à une température située 50C en dessous de la température de reflux du solvant, encore plus avantageusement entre 50 et 600C. La durée de chauffage du milieu de l'étape a) varie de 2 à 36 heures, avantageusement le milieu est chauffé pendant 2 à 10 heures, encore plus avantageusement pendant 3 à 5 heures. Le milieu est ensuite refroidi à température ambiante, avantageusement à 200C.During the esterification reaction of step a), following the addition of the reagents, the medium is advantageously heated to a temperature of between 40 ° C. and the reflux temperature of the solvent (156 ° C. for hexanol). ), more advantageously between 40 0 C and at a temperature located 5 0 C below the reflux temperature of the solvent, more advantageously between 50 and 60 0 C. The heating time of the medium of step a) varies from 2 to 36 hours, advantageously the medium is heated for 2 to 10 hours, even more advantageously for 3 to 5 hours. The medium is then cooled to room temperature, advantageously at 20 ° C.
Suite à l'étape a), les excès d'acide et de solvant sont avantageusement éliminés puis le résidu obtenu est solubilisé dans de l'eau.Following step a), excess acid and solvent are advantageously removed and the resulting residue is solubilized in water.
Lors de l'étape b), le groupement amino pourra être fonctionnalisé par toute méthode connue de l'homme de l'art. Dans le cadre de la présente invention, l'expression « fonctionnalisation du groupement amino » signifie que la fonction aminé du composé de formule IV est substituée, dans des conditions opératoires appropriées bien connues de l'homme de l'art, pour former le composé de formule I.During step b), the amino group may be functionalized by any method known to those skilled in the art. In the context of the present invention, the term "functionalization of the amino group" means that the amine function of the compound of formula IV is substituted, under appropriate operating conditions well known to those skilled in the art, to form the compound of formula I.
L'étape b) est avantageusement effectuée en milieu aqueux et basique par ajout d'un composé R3O-C(O)-X (formule V), dans laquelle X représente un atome d'halogène. Dans le cadre de la présente invention, le terme « halogène » désigne le chlore, le brome, le fluor ou l'iode, avantageusement le fluor ou le chlore.Step b) is advantageously carried out in an aqueous and basic medium by adding a compound R 3 OC (O) -X (formula V), in which X represents a halogen atom. In the context of the present invention, the term "halogen" denotes chlorine, bromine, fluorine or iodine, advantageously fluorine or chlorine.
Le milieu aqueux de l'étape b) peut également comprendre un solvant choisi dans le groupe constitué par le toluène, l'acétate d'éthyle (AcOEt), l'acétate d'isopropyle (AcOiPr) et le dichlorométhane (CH2Cl2). Selon une variante avantageuse de l'invention, la fonctionnalisation du groupement amino est réalisée dans les conditions de Schotten-Bauman, c'est-à-dire par réaction d'un chlorure d'acide en présence d'alcali et d'eau (J. March, Advanced Organic Chemistry, p 392).The aqueous medium of step b) may also comprise a solvent selected from the group consisting of toluene, ethyl acetate (AcOEt), isopropyl acetate (AcOiPr) and dichloromethane (CH 2 Cl 2 ). According to an advantageous variant of the invention, the functionalization of the amino group is carried out under Schotten-Bauman conditions, that is to say by reaction of an acid chloride in the presence of alkali and water ( J. March, Advanced Organic Chemistry, p. 392).
Le milieu de l'étape b) est avantageusement rendu basique par addition d'une base forte telle que la soude. Le milieu de l'étape b) est avantageusement tamponné par ajout d'une base faible, avantageusement l'hydrogénocarbonate de sodium et/ou l'hydrogénocarbonate de potassium.The medium of step b) is advantageously made basic by addition of a strong base such as sodium hydroxide. The medium of step b) is advantageously buffered by addition of a weak base, advantageously sodium hydrogencarbonate and / or potassium hydrogen carbonate.
Le pH du milieu aqueux de l'étape b) est ainsi avantageusement ajusté à des valeurs comprises entre 4 et 7, plus avantageusement comprises entre 5,5 et 6,5, encore plus avantageusement à une valeur de 6 ± 0,2.The pH of the aqueous medium of step b) is thus advantageously adjusted to values between 4 and 7, more advantageously between 5.5 and 6.5, still more advantageously at a value of 6 ± 0.2.
L'ajout du composé de formule V est avantageusement réalisé à une température comprise entre 0 et 2O0C, avantageusement entre 0 et 100C, encore plus avantageusement entre 3 et 70C. Ensuite, le milieu est avantageusement agité à cette température pendant une durée variant de 5 minutes à 1 heure, avantageusement de 15 à 45 minutes, encore plus avantageusement pendant environ 30 minutes. Enfin, le milieu est avantageusement agité à température ambiante (avantageusement 2O0C) pendant une durée variant de 5 minutes à 1 heure, avantageusement de 15 à 45 minutes, encore plus avantageusement pendant environ 30 minutes.The addition of the compound of formula V is advantageously carried out at a temperature of between 0 and 20 ° C., advantageously between 0 and 10 ° C., and even more advantageously between 3 and 70 ° C. Then, the medium is advantageously stirred at this temperature for a time varying from 5 minutes to 1 hour, advantageously from 15 to 45 minutes, even more advantageously for about 30 minutes. Finally, the medium is advantageously stirred at ambient temperature (advantageously 20 ° C.) for a time varying from 5 minutes to 1 hour, advantageously from 15 to 45 minutes, even more advantageously for about 30 minutes.
Le composé de formule V est avantageusement le chloroformiate de benzyle. Selon une variante avantageuse de l'invention, l'étape b) est effectuée par ajout de chloroformiate de benzyle en milieu basique en présence d'une base faible, telle que Phydrogénocarbonate de sodium et/ou Phydrogénocarbonate de potassium.The compound of formula V is advantageously benzyl chloroformate. According to an advantageous variant of the invention, step b) is carried out by adding benzyl chloroformate in a basic medium in the presence of a weak base, such as sodium hydrogencarbonate and / or potassium hydrogencarbonate.
Le produit désiré peut ensuite être récupéré par des méthodes classiques connues de l'homme du métier.The desired product can then be recovered by conventional methods known to those skilled in the art.
Selon une variante avantageuse de l'invention, la première étape a) consiste à préparer la H-Cys(Ph)-OMe, HCl par réaction d'estérification du dérivé de cystéine H-Cys(Ph)-OH dans le méthanol en présence d'un chlorure d'acide tel que le chlorure de thionyle ou d'un acide tel que l'acide chlorhydrique gaz. Après élimination de l'excès d'acide et du solvant de synthèse, le résidu est solubilisé dans de l'eau. La fonctionnalisation du groupement amino (étape b)) est effectuée par ajout de chloroformiate de benzyle en milieu basique en présence d'hydrogénocarbonate de sodium et/ou d'hydrogénocarbonate de potassium.According to an advantageous variant of the invention, the first step a) consists of preparing the H-Cys (Ph) -OMe, HCl by esterification reaction of the cysteine derivative H-Cys (Ph) -OH in methanol in the presence an acid chloride such as thionyl chloride or an acid such as hydrochloric acid gas. After removing the excess acid and the synthesis solvent, the residue is solubilized in water. The functionalization of the amino group (step b)) is carried out by adding benzyl chloroformate in a basic medium in the presence of sodium hydrogen carbonate and / or potassium hydrogen carbonate.
Selon une variante encore plus avantageuse de l'invention, le procédé est caractérisé en ce que l'on fait réagir 1 partie de H-Cys(Ph)-OH avec 1,2 parties de chlorure de thionyle dans 4 à 10 volumes de méthanol. Après concentration, le milieu est dissous dans de l'eau en présence d'un solvant (AcOEt, AcOiPr, CH2Cl2) auquel on additionne de la soude jusqu'à pH = 6 suivie de 2 parties d'hydrogénocarbonate de sodium et 1 partie de chloroformiate de benzyle. Après réaction, le produit est obtenu dans la phase organique après décantation puis précipitation par addition de 3 à 5 volumes d'heptane et refroidissement.According to an even more advantageous variant of the invention, the process is characterized in that 1 part of H-Cys (Ph) -OH is reacted with 1.2 parts of thionyl chloride in 4 to 10 volumes of methanol. . After concentration, the medium is dissolved in water in the presence of a solvent (AcOEt, AcOiPr, CH 2 Cl 2 ) to which soda is added until pH = 6 followed by 2 parts of sodium hydrogencarbonate and 1 part of benzyl chloroformate. After reaction, the product is obtained in the organic phase after decantation and precipitation by adding 3 to 5 volumes of heptane and cooling.
Le procédé selon l'invention est caractérisé par l'utilisation d'une base faible, lors de l'étape b), permettant de travailler en milieu tamponné de façon à éviter la réaction secondaire de saponification, réaction généralement observée lorsque l'on utilise une base forte comme la soude ou la potasse. Ainsi, le procédé selon l'invention par les conditions de pH et les conditions de température choisies évitent la décomposition du chloroformiate qui est à l'origine de l'impureté ester méthylique de N-benzyle-phénylcystéine. Les conditions de pH et de température du procédé permettent également d'éviter la réaction d'élimination du thiophénol et ainsi d'éviter la formation de l'impureté déhydroalanine.The process according to the invention is characterized by the use of a weak base, during step b), making it possible to work in a buffered medium so as to avoid the secondary reaction of saponification, a reaction generally observed when using a strong base like soda or potash. Thus, the process according to the invention by the pH conditions and the selected temperature conditions avoid the decomposition of the chloroformate which is at the origin of the impurity N-benzyl-phenylcysteine methyl ester. The pH and temperature conditions of the process also make it possible to avoid the elimination reaction of thiophenol and thus to avoid the formation of the dehydroalanine impurity.
La réalisation de l'estérification, préalablement à la fonctionnalisation de la fonction aminé, permet de conserver le produit dans le même réacteur car il suffit d'éliminer l'excès d'alcool R]-OH par évaporation avant la mise en œuvre de la benzyloxycarbonylation. La synthèse "one pot" ne mobilise donc qu'un réacteur, elle permet ainsi de fabriquer le produit désiré en un minimum de manipulations et d'opérations unitaires, par exemple une seule filtration, un seul séchage de produit isolé, moins de nettoyage des équipements donc moins de solvants et moins de rejets.Performing the esterification, prior to the functionalization of the amine function, keeps the product in the same reactor because it is sufficient to remove the excess alcohol R] -OH by evaporation before the implementation of the benzyloxycarbonylation. The synthesis "one pot" therefore mobilizes only one reactor, it thus makes it possible to manufacture the desired product in a minimum of manipulations and unit operations, for example a single filtration, a single drying of isolated product, less cleaning of equipment therefore less solvents and fewer discharges.
La réalisation de l'estérification, préalablement à la fonctionnalisation de la fonction aminé, permet également d'éviter la formation d'impuretés dipeptidiques, qui peuvent être obtenues lors de la réaction de benzyloxycarbonylation des acides aminés, dont la fonction acide carboxylique est libre.The carrying out of the esterification, prior to the functionalization of the amine function, also makes it possible to avoid the formation of dipeptide impurities, which can be obtained during the benzyloxycarbonylation reaction of the amino acids, whose carboxylic acid function is free.
Les procédés permettant d'introduire un groupe phényle sur la cystéine donnant des rendements et des puretés médiocres, il est avantageux de placer ces réactions en début de synthèse pour réduire l'impact sur le coût et maîtriser les impuretés dès le début de la synthèse.The methods for introducing a phenyl group on cysteine yielding poor yields and purities, it is advantageous to place these reactions at the beginning of synthesis to reduce the impact on the cost and control impurities from the beginning of the synthesis.
Le composé de départ est avantageusement le S-Phényl cystéineThe starting compound is advantageously S-phenyl cysteine
qui permet d'accéder au thiocarbaester, (2R)-2-[(benzyloxycarbonyl)amino]-3- (phénylthio) propanoïque acide méthyl ester, de formule IaI which makes it possible to access thiocarbaester, (2R) -2 - [(benzyloxycarbonyl) amino] -3- (phenylthio) propanoic acid methyl ester, of formula IaI
avec conservation de l'excès énantiomérique de la cystéine de départ, ledit thiocarbaester étant ensuite utilisé dans la synthèse de médicaments, notamment le Nelfïnavir. with retention of the enantiomeric excess of the starting cysteine, said thiocarbaester being then used in the synthesis of drugs, especially Nelfinavir.
L'invention a également pour objet l'utilisation des composés de formule (I), obtenus par le procédé selon l'invention, en tant que produits intermédiaires dans la synthèse de médicaments, notamment dans la synthèse de produits actifs anti-sida de la classe des inhibiteurs de la protéase HIV. En particulier, l'invention concerne l'utilisation du thiocarbaester IaI, obtenu par le procédé selon l'invention, en tant que produit intermédiaire dans la synthèse de produits actifs anti-sida de la classe des inhibiteurs de la protéase HIV, notamment le Nelfïnavir.The subject of the invention is also the use of the compounds of formula (I), obtained by the process according to the invention, as intermediates in the synthesis of medicinal products, in particular in the synthesis of active anti-AIDS products of the class of HIV protease inhibitors. In particular, the invention relates to the use of thiocarbaester IaI, obtained by the process according to the invention, as an intermediate product in the synthesis of active anti-AIDS products of the class of HIV protease inhibitors, in particular Nelfinavir. .
Les exemples qui suivent illustrent l'invention sans toutefois la limiter.The following examples illustrate the invention without limiting it.
Exemple 1 : synthèse du thiocarbaester IaIExample 1 Synthesis of Thiocarbaester IaI
a) Mode opératoire :a) Procedure:
Dans un réacteur de 2 litres équipé, on introduit 100 g de L-(R)-S-phényl cystéine (H-Cys(Ph)-OH ; S-phényl cystéine lévogyre, de configuration R) et 400 ml de méthanol. Le milieu est chauffé à 55°C puis 70,8 g de chlorure de thionyle sont additionnés en maintenant la température inférieure à 600C. Un palier de 4 h à 600C est effectué puis le milieu est refroidi à 2O0C puis concentré sous vide réduit. 100 ml de toluène sont additionnés puis le milieu est de nouveau concentré sous vide réduit. 300 ml de toluène puis 300 ml d'eau sont additionnés, le pH de la phase aqueuse est ajusté à pH=6 par addition de soude aqueuse, puis 96 g d'hydrogénocarbonate de sodium sont additionnés. 82 g de chloroformiate de benzyle sont additionnés à 5°C. Le milieu est agité 30 min à 5°C puis 30 min à 2O0C.In a 2-liter reactor equipped, 100 g of L- (R) -S-phenyl cysteine (H-Cys (Ph) -OH; S-phenyl cysteine levorotatory, configuration R) and 400 ml of methanol are introduced. The medium is heated at 55 ° C. and then 70.8 g of thionyl chloride are added while maintaining the temperature below 60 ° C. A 4 hour run at 60 ° C. is then carried out, the medium is cooled to 20 ° C. and then concentrated under reduced vacuum. 100 ml of toluene are added and the medium is again concentrated under reduced vacuum. 300 ml of toluene and 300 ml of water are added, the pH of the aqueous phase is adjusted to pH = 6 by addition of aqueous sodium hydroxide, then 96 g of sodium hydrogencarbonate are added. 82 g of benzyl chloroformate are added at 5 ° C. The medium is stirred for 30 min at 5 ° C. and then 30 min at 20 ° C.
Le pH de la phase aqueuse est ajusté à pH = 3 par addition d'acide chlorhydrique 35%. Après décantation du milieu, les phases sont séparées. La phase toluénique est lavée deux fois à l'eau puis concentrée de moitié.The pH of the aqueous phase is adjusted to pH = 3 by addition of 35% hydrochloric acid. After decantation of the medium, the phases are separated. The toluene phase is washed twice with water and then concentrated by half.
420 ml d'heptane sont additionnés puis le milieu est refroidi à 10°C. Après un palier de 2h à 1O0C, le précipité est filtré, lavé à l'heptane.420 ml of heptane are added and then the mixture is cooled to 10 ° C. After a plateau of 2 h at 10 ° C., the precipitate is filtered and washed with heptane.
Après séchage, on obtient 130g de thiocarbaester sous forme d'un solide blanc, soit un rendement massique de 80%.After drying, 130 g of thiocarbaester are obtained in the form of a white solid, ie a mass yield of 80%.
b) analyseb) analysis
Les résultats de l'analyse du thiocarbaester synthétisé précédemment sont donnés dans le tableau 1 ci-dessous.The results of the thiocarbaester analysis synthesized previously are given in Table 1 below.
Tableau 1 Table 1
1 High Performance Liquid Chromatography = Chromatographie liquide haute performance 1 High Performance Liquid Chromatography = High Performance Liquid Chromatography
2 Infrarouge 2 Infrared
3 titrage selon la méthode Karl Fischer 3 titration according to the Karl Fischer method
Le procédé selon l'invention permet d'obtenir le thiocarbaester IaI avec un bon rendement, un pureté chirale de 99,8% et une pureté chimique de 99,4%. The process according to the invention makes it possible to obtain thiocarbaester IaI with a good yield, a chiral purity of 99.8% and a chemical purity of 99.4%.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0501192 | 2005-02-07 | ||
| FR0501192A FR2881741B1 (en) | 2005-02-07 | 2005-02-07 | PROCESS FOR THE SYNTHESIS OF CYSTEINE DERIVATIVES, IN PARTICULAR THIOCARBAESTER, USEFUL AS INTERMEDIATE PRODUCTS IN THE SYNTHESIS OF DRUGS |
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| WO2006082228A1 true WO2006082228A1 (en) | 2006-08-10 |
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| PCT/EP2006/050639 Ceased WO2006082228A1 (en) | 2005-02-07 | 2006-02-03 | Method for synthesising cysteine derivatives, in particular thio carbaesters used in the form of intermediate products in drug synthesis |
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| FR (1) | FR2881741B1 (en) |
| WO (1) | WO2006082228A1 (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0897911A1 (en) * | 1997-01-14 | 1999-02-24 | Kaneka Corporation | Process for producing cysteine derivatives |
| EP0968997A2 (en) * | 1998-06-29 | 2000-01-05 | F. Hoffmann-La Roche Ag | Process for S-aryl-L-cysteine and derivatives |
| EP1054000A1 (en) * | 1998-01-13 | 2000-11-22 | Kaneka Corporation | Process for producing optically active cysteine derivatives |
-
2005
- 2005-02-07 FR FR0501192A patent/FR2881741B1/en not_active Expired - Fee Related
-
2006
- 2006-02-03 WO PCT/EP2006/050639 patent/WO2006082228A1/en not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0897911A1 (en) * | 1997-01-14 | 1999-02-24 | Kaneka Corporation | Process for producing cysteine derivatives |
| EP1054000A1 (en) * | 1998-01-13 | 2000-11-22 | Kaneka Corporation | Process for producing optically active cysteine derivatives |
| EP0968997A2 (en) * | 1998-06-29 | 2000-01-05 | F. Hoffmann-La Roche Ag | Process for S-aryl-L-cysteine and derivatives |
Non-Patent Citations (4)
| Title |
|---|
| BROEK VAN DEN L A G M ET AL: "LIPOPHILIC ANALOGUES OF SPARSOMYCIN AS STRONG INHIBITORS OF PROTEIN SYNTHESIS AND TUMOR GROWTH: A STRUCTURE-ACTIVITY RELATIONSHIP STUDY", JOURNAL OF MEDICINAL CHEMISTRY, AMERICAN CHEMICAL SOCIETY. WASHINGTON, US, vol. 32, no. 8, 1 August 1989 (1989-08-01), pages 2002 - 2015, XP000617037, ISSN: 0022-2623 * |
| C.H. LEVENSON: "Design and synthesis of tetrahedral intermediate analogues as potential dihydroorotase inhibitors", J.MED.CHEM., vol. 27, no. 2, 1984, XP002352554 * |
| G. DESIMONI ET AL: "Copper (II) in organic synthesis. XI. Evaluation of the ligand architecture on the efficiency of a copper (II) catalyst for enantioselective Michael reactions", TETRAHEDRON, vol. 51, no. 14, 1995, pages 4131 - 4144, XP002352555 * |
| KNIGHT D W ET AL: "TOTAL SYNTHESIS OF (-)-SLAFRAMINE FROM (2R,3S)-HYDROXYPROLINE", JOURNAL OF THE CHEMICAL SOCIETY, PERKIN TRANSACTIONS 1, CHEMICAL SOCIETY. LETCHWORTH, GB, 1997, pages 2179 - 2187, XP001040653, ISSN: 0300-922X * |
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| FR2881741A1 (en) | 2006-08-11 |
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