The present invention relates to a process for preparing a nucleoside phosphoramidate, in particular to a process for preparing sofosbuvir, wherein a phosphoramidate derivative is used as starting material.
Sofosbuvir according to the following formula
with IUPAC name (S)-isopropyl 2-(((S)-(((2R,3R,4R,5R)-5-(2,4-dioxo-3,4-dihydropyrimidin-1(2H)-yl)-4-fluoro-3-hydroxy-4-methyltetrahydrofuran-2-yl)methoxy) (phenoxy)phosphoryl) amino)propanoate is a drug inhibiting the RNA polymerase used by the hepatitis C virus to replicate its RNA.
For preparing sofosbuvir, WO 2008/121634 discloses a process wherein a nucleoside is reacted with a phosphoric acid amide having chloride as leaving group. N-methylimidazole is used in the displacement reaction. Due to the chirality of the phosphorous atom, two diastereoisomers are obtained which have the following formulas (I-1) and (1-2):
This displacement reaction taught in WO 2008/121634 A in the presence of N-methylimidazole is not selective, and a 1:1 mixture of the two diastereomers of formulas (I-1) and (1-2) is obtained. The reaction is further plagued with significant formation of the doubly phosphorylated side product (in positions 5′ and 3′), resulting in a tedious purification process and in low yield.
As an alternative to the phosphorochloridate of WO 2008/121634, WO 2010/135569 A, WO 2011/123668, WO 2012/012465 A, J. Org. Chem. 2011, 76, 8311, WO 2014/047117 A, and WO 2014/164533 A disclose crystalline phosphoramidating reagents which bear electron-poor phenolates and heterocycles as leaving groups. These reagents can be isolated in diastereomerically enriched form by fractional crystallization or chromatography. The process necessitates diastereomer separation of phosphoramidating reagents prior to the coupling reaction, which makes the process less than ideal.
Additionally, leaving groups, such as aryloxide substituted with at least one electron-withdrawing group such as a halogen or a nitro group, lead to the problem of the formation side-products such as 3′-O-phosphoramidate or 3′,5′-bis-O-phosphoramidate. In Example 15 of WO 2010/135569 A, in order to overcome the problem of the formation of 3′-O-phosphoramidate or 3′,5′-bis-O-phosphoramidate side products, it is proposed to protect position 3′ of the ribose ring with a levulinic anhydride and subsequently de-protect said position. Alternatively, position 3′ is protected with a tert-butyl-dimethylsilyl group. Therefore, comparatively complicated methods have to be applied to overcome said problems. WO 2011/123672 A describes a process for preparing nucleoside phosphoramidate compounds wherein the nucleoside phosphoramidate is prepared via displacement of the leaving group on a phosphoramidate to give the corresponding nucleoside-phosphoramidate. The leaving group is either aryloxide substituted with at least one electron-withdrawing group such as halogen or a nitro group or benzo[d]thiazole-2(3H)-thione. WO 2014/047117 A discloses a process for preparing nucleoside phosphoramidate compounds, in particular a complicated two-step process. The first step is the displacement of the leaving group such as p-nitrophenol on a phosphinoborane derivative or on a thio-phosphoramidate compound to give the corresponding nucleoside boran- or thio-phosphoramidate. The displacement occurs in basic conditions (Et3N, DBU (1,8-Diazabicyclo[5.4.0]undec-7-ene)). In a subsequent step, the nucleoside boran- or thio-phosphoramidate is oxidized to the corresponding nucleoside phosphoramidate. In addition to the problems regarding comparatively complicated process, there is the problem relating to the chemical nature of the leaving groups on the phosphoramidate. These leaving groups remain as trace impurity in the final nucleoside phosphoramidate compounds. However, many leaving groups such as p-nitrophenol or other aryloxide groups substituted with an electron-withdrawing group are considered to be toxic substances, in particular genotoxic substances, by FDA. Generally, difficulties may be encountered to purify the final API from these toxic leaving groups to meet the FDA requirements.
Therefore, the problem underlying the present invention is the provision of a novel process for preparing nucleoside phosphoramidates, in particular sofosbuvir, that starts from a phosphoramidate having the toxicologically harmless succinimide as leaving group, wherein the process exhibits an improved diastereoselectivity to the valuable product, in particular sofosbuvir. The diastereoselectivity achieved with the known process taught in the prior art making use of the phosphoramidates having chloride as leaving group and using N-methylimidazole (NMI) as the base is lower than the diastereoselectivity achieved with the process of the invention.
Further, it was surprisingly found that the problem of providing a diastereoselective process can be solved by a process for preparing nucleoside phosphoramidates, in particular sofosbuvir, which is carried out using a base preferably an organic base, more preferably an organic nitrogenous base in combination with a Lewis acid. In particular, the present inventors have surprisingly found that slightly enriched or completely P-racemic mixtures of the phosphoramidate derivative according to the present invention gave nucleoside phosphoramidate with high diastereoselectivity when reacted in the presence of a Lewis acid and a base according to the invention. Without being bound to any theory, it is believed that the high diastereoselectivity is because the phosphoramidating reagent undergoes dynamic kinetic resolution during the coupling reaction. In this case both diastereoisomers of the phosphoramidating reagent exist in equilibrium and only one goes on to form the desired diastereoisomer of sofosbuvir.
Hence, the process of the present invention advantageously avoids waste of material (such as non-useful diastereoisomers) and translates directly into a faster and more economical process.
It has further been found that the process according to the present invention leads to high yields.
Therefore, the present invention relates to a process for preparing of a compound of formula (I)
or a salt thereof, the process comprising
in the presence of a Lewis acid and a base, preferably an organic base according to the present invention, obtaining a mixture comprising the compound of formula (I).
Therefore, the present invention relates to a process for preparing of a compound of formula (I)
or a salt thereof, the process comprising
in the presence of a Lewis acid and a base, preferably an organic base according to the present invention, obtaining a mixture comprising the compound of formula (I).
Preferably (Y—)nRx is a leaving group for nucleophilic substitution reaction, wherein n is 0 or 1 and wherein Y is O, N or S.
Preferably, Rx is alkyl, aryl, or heteroaryl, each optionally substituted with one or more electron-withdrawing groups, preferably aryl optionally substituted with one or more electron-withdrawing groups, more preferably phenyl optionally substituted with one or more electron-withdrawing groups, more preferably phenyl substituted with one or more electron-withdrawing groups, wherein the one or more electron-withdrawing groups are preferably F, Cl, Br, I, or NO2; or
when n is 1, RR is
a residue of formula (A)
a residue of formula (B)
a residue of formula (C)
or a residue of formula (D)
or when n is 0,
Rx is a residue of formula (A1)
wherein at each occurrence
X1 and X2 are independently O or S;
R30 and R31 are independently H, OH, NH2, C1-C6 alkyl or C1-C6 alkoxy, or R30 and R31, together with the structure —C—N—C— according to formula (A), form an optionally substituted, 5-, 6-, or 7-membered saturated or partially unsaturated ring, wherein said ring is optionally fused to a 5- or 6-membered, optionally substituted ring which is a C5-C6 cycloalkyl, an aryl or a heterocycle comprising one or more heteroatoms independently being N, O or S;
R17 is an electron-withdrawing group, preferably F, Cl, Br, I, NO2, CHO, COOH, COO—(C1-C6)alkyl, CN, or COCl;
R18 and R18, are independently F, Cl, Br, I, or C1-C6 alkoxy;
each Q is independently C or N, wherein at least one Q is N;
R19 and R19, are independently H, OH, NH2, C1-C6 alkyl optionally substituted with at least one of OH and NH2, or C1-C6 alkoxy optionally substituted with at least one of OH and NH2; or
R19 and R19′ taken together form an optionally substituted 5-, 6-, or 7-membered saturated or partially unsaturated or aromatic ring, wherein the ring is optionally fused to a 5- or 6-membered, optionally substituted ring which is a C5-C6 cycloalkyl, an aryl, preferably benzo, or a heterocycle comprising one or more heteroatoms independently being N, O or S, the 5- or 6-membered optionally substituted ring preferably being heteroaryl;
R20, R21, R22 and R23 are each independently H, aryl, or C1-C6 alkyl optionally substituted with at least one of C1-C6 alkoxy optionally substituted with at least one of OH and NH2; or
R20 and R22, or R20 and R23, or R21 and R22, or R21 and R23 when taken together form an optionally substituted 5-, 6-, or 7-membered saturated or partially unsaturated or aromatic ring which is an aryl, preferably benzo, or a heterocycle comprising one or more heteroatoms independently being N, O or S, the 5-, 6-, or 7-membered saturated or partially unsaturated or aromatic ring preferably being heteroaryl.
It is further conceivable that when n is 0, Rx can also be Cl. In this case in the process according to the invention, it is preferred that the base is not NMI.
More preferably, when n is 1, Rx is a residue of formula (A), a residue of formula (B), a residue of formula (C), or a residue of formula (D), or when n is 0, Rx is a residue of formula (A1).
More preferably, when n is 0, Rx is a residue of formula (A1)
wherein R20, R21, R22 and R23 are each independently H, aryl, or C1-C6 alkyl optionally substituted with at least one of C1-C6 alkoxy optionally substituted with at least one of OH and NH2; or
R20 and R22, or R20 and R23, or R21 and R22, or R21 and R23 when taken together form an optionally substituted 5-, 6-, or 7-membered saturated or partially unsaturated or aromatic ring which is an aryl, preferably benzo, or a heterocycle comprising one or more heteroatoms independently being N, O or S, the 5-, 6-, or 7-membered saturated or partially unsaturated or aromatic ring preferably being heteroaryl.
According to the invention, at each occurrence, the substituent of the optionally substituted 5-, 6-, or 7-membered saturated or partially unsaturated or aromatic ring which is preferably an aryl, preferably benzo, or a heterocycle comprising one or more heteroatoms independently being N, O or S, is at least a substituent, preferably one substituent, selected from the group consisting of OH, C1-C6 alkoxy, aryl, heteroaryl, C3-C6 cycloalkyl, F, Cl, Br, I, COOH, CHO, C(O)(C1-C6 alkyl), C(O)(aryl), COO(C1-C6 alkyl), COONH2, COONH(C1-C6 alkyl), CN, NO2, —NH2, NR27R28, wherein R27 and R28 are independently selected from the group consisting of H, C1-C6 alkyl, C1-C6 alkoxy, aryl, heteroaryl, and wherein aryl at each occurrence is preferably phenyl. According to the invention, at each occurrence the aromatic ring is a benzo substituted with at least one, preferably with one substituent, wherein the substituent is selected from the group consisting of OH, C1-C6 alkoxy, aryl, heteroaryl, C3-C6 cycloalkyl, F, Cl, Br, I, COOH, CHO, C(O)(C1-C6 alkyl), C(O)(aryl), COO(C1-C6 alkyl), COONH2, COONH(C1-C6 alkyl), CN, NO2, —NH2, NR27R28, wherein R27 and R28 are independently selected from the group consisting of H, C1-C6 alkyl, C1-C6 alkoxy, aryl, heteroaryl, and wherein aryl at each occurrence is preferably phenyl.
Preferably, R22 and R23 are each independently H, aryl, or C1-C6 alkyl substituted with at least one of C1-C6 alkoxy optionally substituted with at least one of OH and NH2.
Preferably, when n is 1, Rx is a residue of formula (A)
wherein
X1 and X2 are independently O or S;
R30 and R31 are independently H, OH, NH2, C1-C6 alkyl or C1-C6 alkoxy, or R30 and R31, together with the structure —C—N—C— according to formula (A), form an optionally substituted, 5-, 6-, or 7-membered saturated or partially unsaturated ring, wherein said ring is optionally fused to a 5- or 6-membered, optionally substituted ring which is a C5-C6 cycloalkyl, an aryl or a heterocycle comprising one or more heteroatoms independently being N, O or S.
More preferably, Rx is a residue of formula (IIb)
wherein X1 is 0 and X2 is O.
More preferably, Rx is a residue of formula (IIc)
wherein X1 is O and X2 is O.
More preferably when n is 1 Rx is a residue of formula (B)
wherein R17 is preferably selected from the group consisting of F, Cl, Br, I, NO2, CHO, COOH, COO—(C1-C6)alkyl, CN and COCl.
More preferably when n is 1, Rx is a residue of formula (C)
wherein R18 and R18, are preferably independently F, Cl, Br, I, or C1-C6 alkoxy and each Q is independently C or N, wherein at least one Q is N.
More preferably, when n is 1, Rx is a residue of formula (D)
wherein R19 and R19′ are preferably independently H, OH, NH2, C1-C6 alkyl optionally substituted with at least one of OH and NH2, or C1-C6 alkoxy optionally substituted with at least one of OH and NH2; or R19 and R19′ taken together form an optionally substituted 5-, 6-, or 7-membered saturated or partially unsaturated or aromatic ring, wherein the aromatic ring is preferably benzo, wherein the ring is optionally fused to a 5- or 6-membered, optionally substituted ring which is a C5-C6 cycloalkyl, an aryl, preferably benzo, or a heterocycle comprising one or more heteroatoms independently being N, O or S, the 5- or 6-membered optionally substituted ring preferably being heteroaryl.
More preferably, n=1, Y═O and RR is a residue of formula (IIb)
wherein X1 and X2 are both O.
Preferably, the residue R4 is phenyl, naphthyl, quinolinyl, isoquinolinyl, quinazolinyl or quinoxalinyl, each optionally substituted with at least one of C1-C6 alkyl, C1-C6 alkoxy, C3-C6 cycloalkyl, aryl, halogen, C(O)OH, CHO, C(O)(C1-C6 alkyl), C(O)(aryl), C(O)O(C1-C6 alkyl), C(O)ONH2, C(O)ONH(C1-C6 alkyl) and CN. The term “C1-C6 alkyl” as used herein refers to alkyl residues having 1, 2, 3, 4, 5, or 6 carbon atoms. The term “C1-C6 alkoxy” as used herein refers to alkoxy residues having 1, 2, 3, 4, 5, or 6 carbon atoms. The term “C3-C6 cycloalkyl” as used herein refers to cycloalkyl residues wherein 3, 4, 5, or 6 carbon atoms constitute the ring structure.
Preferably, the residues R2 and R3 are independently H or C1-C6 alkyl optionally substituted with at least one of OH, C1-C6 alkoxy, aryl, heteroaryl, C1-C6 alkyl, C3-C6 cycloalkyl, F, Cl, Br, I, NO2, C(O)OH, CHO, C(O)(C1-C6 alkyl), C(O)(aryl), C(O)O(C1-C6 alkyl), C(O)ONH2, C(O)ONH(C1-C6 alkyl) and CN.
Preferably, the residue R6 is C1-C6 alkyl or C3-C10 cycloalkyl optionally substituted with at least one of C1-C6 alkyl and aryl.
Preferably, R1 is an optionally derivatized purinyl residue, including an adenine residue and a guanine residue, or an optionally derivatized pyrimidinyl residue, including a cytosine residue, a thymine residue and an uracil residue, linked to the furanose ring according to formula (III) through a carbon or nitrogen atom.
Preferably, R7 and R8 are independently H, OH, F, Cl, Br, I, azide, nitrile, NH2, NHR26, NR26R24, C(O)NH2, C(O)NHR26, C(O)NR26R24, C1-C6 alkyl optionally substituted with C1-C6 alkyl, or C3-C10 cycloalkyl optionally substituted with C1-C6 alkyl, wherein R26 and R24 are independently C1-C6 alkyl.
Preferably, R5 is H, OH, C1-C6 alkoxy, OC(O)R25, or C1-C6 alkyl optionally substituted with C1-C6 alkyl or aryl, wherein R25 is C1-C6 alkyl or aryl.
Preferably, the compound of formula (II) is
and the compound of formula (III) is
The P atom is a chirality center of the compound of formula (II) and (II-0). It is preferred that according to a), the compound of formula (II) comprises a compound of formula (II-A),
and a compound of formula (II-B),
wherein the molar ratio of the compound of formula (II-A) relative the compound of formula (II-B) is preferably in the range of from 45:55 to 72:28, more preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45. Preferably, the compound of formula (II) consists of the compound of formula (II-A) and the compound of formula (II-B).
Also preferably, the molar ratio of the compound of formula (II-A) relative the compound of formula (II-B) is in the range of from 55:45 to 45:55, more preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-A) relative the compound of formula (II-B) is 1:1. Preferably, the compound of formula (II) consists of the compound of formula (II-A) and the compound of formula (II-B).
It is preferred that according to a), the compound of formula (II) comprises a compound of formula (II-a)
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60: 40, more preferably in the range of from 45:55 to 55:45. More preferably, the compound of formula (II) consists of the compound of formula (II-a) and the compound of formula (II-b).
Also preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II) consists of the compound of formula (II-a) and the compound of formula (II-b).
Preferably, from step a) of the process of the present invention, a mixture is obtained which comprises the compound of formula (I) wherein the compound of formula (I) comprises a compound of formula (I-1)
and a compound of formula (I-2)
It is preferred that in the mixture obtained from a), the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20. It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 85:15 or at least 90:10 or at least 95:5 or at least 99:1 or at least 99.8:0.2. More preferably, the compound of formula (I) comprised in the mixture obtained from a) consists of the compound of formula (I-1) and the compound of formula (I-2).
It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) obtained in step a) is in the range of from 65:35 to 90:10, preferably in the range of from 75:25 to 90:10. It is conceivable that this molar ratio is further improved by crystallization or crystallization and recrystallization steps according to the present invention up to a molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) in the range of from 95:5 to 99.8:0.2, preferably in the range of from 99:1 to 99.8:0.2.
Preferably, one of R7 and R8 may be C1-C6 alkyl, preferably methyl, and one of R7 and R8 may be F, Cl, OH, CN, or NH2. Further preferably, R1 may be an optionally derivatized pyrimidinyl residue, preferably a uracil residue. Also preferably, R1 may be an optionally derivatized purinyl residue. Therefore, among others, the following compounds of formula (I) may be preferably prepared by the process of the present invention:
Preferably, regarding the compound of formula (III) employed in a), the residues R7 and R8 are independently selected from H, F, methyl or OH, more preferably the residues R7 and R8 are independently selected from F and methyl.
Preferably, the compound of formula (III) is
more preferably
more preferably
more preferably
Preferably, the compound of formula (II-a) is a compound of formula
and the compound of formula (II-b) is a compound of formula
Therefore, it is preferred that the compound of formula (I-1) is one of the compounds
more preferably
and the compound of formula (I-2) is one of the compounds
more preferably
More preferably, the compound of formula (III) employed in a) is a compound of formula
the compound of formula (II-0) is a compound of formula
and the compound of formula (I) is a compound of formula
Therefore, the present invention also relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
wherein the compound of formula (II-0) comprises a compound of formula (II-a)
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45.
Also preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, more preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
The base employed in a) is preferably an organic base, more preferably an organic nitrogenous base, more preferably a tertiary organic nitrogenous base. More preferably, the organic base comprises one or more of an amine, an amidine, and a heteroaromatic compound comprising a basic ring-nitrogen atom. More preferably, the organic base comprises, preferably consists of, one or more of ethyldiisopropylamine, triethylamine, diethylamine, 1,8-diazabicycloundec-7-ene, pyridine, quinoline, isoquinoline, acridine, pyrazine, imidazole, benzimidazole, ephedrine, piperidine, tetramethylguanidine, pyrazole. More preferably, the organic base comprises, preferably consists of, one or more of ethyldiisopropylamine, triethylamine, diethylamine, 1,8-diazabicycloundec-7-ene, pyridine, ephedrine, piperidine, tetramethylguanidine. More preferably, the base comprises, preferably consists of, one or more of ethyldiisopropylamine, triethylamine, 1,8-diazabicycloundec-7-ene, ephedrine, piperidine, tetramethylguanidine. More preferably, the base comprises, preferably consists, of ethyldiisopropylamine.
Therefore, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
Therefore, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
Therefore, the present invention relates to the process as defined above, wherein the compound of formula (II-0) employed in a) consists of the compound of formula (II-a) and the compound of formula (II-b), wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1.
Regarding methods to prepare the compound of formula (II), reference is made to examples 1.1 and 2.1 hereinbelow.
As mentioned above, the process of the present invention is characterized by an advantageous diastereoselectivity to the valuable product, the compound of formula (I-1), in particular the compound known as sofosbuvir. Thus, it is preferred that in the mixture obtained from a), the compound of formula (I) comprises a compound of formula (I-1)
and a compound of formula (I-2)
wherein the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20. It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 85:15 or at least 90:10 or at least 95:5 or at least 99:1 or at least 99.8:0.2. Preferably, the compound of formula (I) comprised in the mixture obtained from a) consists of the compound of formula (I-1) and the compound of formula (I-2).
It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) obtained in step a) is in the range of from 65:to 35 to 90:10, preferably in the range of from 75:25 to 90:10. It is conceivable that this molar ratio is further improved by crystallization, or crystallization and recrystallization, steps according to the present invention up to a molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) in the range of from 95:5 to 99.8:0.2, preferably in the range of from 99:1 to 99.8:0.2.
Therefore, the present invention relates to the process as defined above, wherein the compound of formula (II-0) employed in a) consists of the compound of formula (II-a) and the compound of formula (II-b), wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1, wherein the compound of formula (I) comprised in the mixture obtained from a) consists of the compound of formula (I-1) and the compound of formula (I-2), and wherein the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is in the range of from 75:25 to 90:10. It is preferred that after the crystallization of the compound of formula (I), the crystallized compound of formula (I) consists of the compound of formula (I-1) and the compound of formula (I-2), and wherein the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is in the range of from 95:5 to 99.8:0.2, preferably in the range of from 99:1 to 99.8:0.2.
Regarding the amount of the base relative to the amount of the compound of formula (III) employed in a), no specific restrictions exist. Preferably, prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 0.1:1 to 5:1. More preferably, prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 0.5:1 to 5:1, more preferably in the range of from 1:1 to 5:1, more preferably in the range of from 2:1 to 5:1. More preferably, prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 2:1 to 4:1, more preferably in the range of from 2.5:1 to 4:1, more preferably in the range of from 2.5:1 to 3.5:1. Also preferably, prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 1:1 to 3:1.
Therefore, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45.
More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
According to the present invention, it was found that the diastereoselectivity to the compound of formula (I-1), in particular the compound
is achieved if the compound of formula (III) is reacted with the compound of formula (II-0) in the presence of the base and a Lewis acid.
No specific restrictions exist with regard to the chemical nature of the Lewis acid employed in a). Preferably, the Lewis acid comprises a twice positively charged ion or a three times positively charged ion, more preferably a twice positively charged metal ion or a three times positively charged metal ion. Generally, it is also conceivable that the Lewis acid comprises a twice positively charged ion and a three times positively charged ion, preferably a twice positively charged metal ion and a three times positively charged metal ion. With regard to the twice positively charged ion, it is preferred that it comprises, more preferably is, a Zn ion, a Mg ion, a Cu ion, or an Fe ion. More preferably, the twice positively charged ion comprises, more preferably is, a Zn ion or an Mg ion. More preferably, the twice positively charged ion comprises, more preferably is, a Zn ion. With regard to the three times positively charged ion, it is preferred that it comprises, more preferably is, a Mn ion.
Regarding the Lewis acid comprising a twice positively charged ion comprising, more preferably being, a Zn ion, no specific restrictions exist. Preferred Lewis acids comprise, more preferably are, Zn halides. More preferably, the Lewis acid comprises, preferably is, one or more of ZnBr2, ZnCl2, and ZnI2. More preferably, the Lewis acid comprises, preferably is, ZnBr2.
It is also conceivable that the Lewis acid is one or more of ZnBr2, ZnCl2, ZnI2, MgBr2, MgBr2.OEt2, CuCl2, Cu(acetylacetonate)2, and Fe(II) fumarate.
Regarding the Lewis acid comprising a three times positively charged ion comprising, preferably being, a Mn ion, no specific restrictions exist. Preferred Lewis acids comprise, more preferably are, Mn(acetylacetonate)3.
Regarding the amount of the Lewis acid relative to the amount of the compound of formula (III) employed in a), no specific restrictions exist. Preferably, prior to the reaction according to a), the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.1:1 to 5:1. More preferably, prior to the reaction according to a), the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.2:1 to 5:1, preferably in the range of from 0.5:1 to 3:1, more preferably in the range of from 0.75:1 to 1.5:1, more preferably in the range of from 0.75:1 to 1.25:1.
Thus, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
Regarding the amount of the compound of formula (II) employed in a) relative to the amount of the compound of formula (III) employed in a), no specific restrictions exist. Preferably, prior to the reaction according to a), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.5:1 to 5:1, preferably in the range of 0.5 to 6:1. More preferably, prior to the reaction according to a), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.6:1 to 4:1, preferably in the range of from 0.7:1 to 3:1. More preferably, prior to the reaction according to a), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.8:1 to 2:1, preferably in the range of from 0.9:1 to 1.2:1.
It is further conceivable that the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 1.4:1 to 6:1, preferably in the range of from 1.4:1 to 4.9:1, more preferably in the range of from 2.1:1 to 5.5:1; more preferably in the range of from 2.1:1 to 4.9:1, more preferably in the range of from 3:1 to 5:1; 3:1 to 4.9:1, more preferably in the range of from 3:1 to 4:1.
It has been seen that a certain excess of the compound of formula (II) relative to the compound of formula (III) may further favour the resolution of compound of formula (I-1) thereby increasing the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2).
Thus, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 55:45, preferably the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1;
wherein prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 0.1:1 to 5:1, preferably in the range of from 2.5:1 to 4.5:1, more preferably in the range of from 2.5:1 to 4:1, more preferably in the range of from 2.5:1 to 3.5:1; more preferably, prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 1:1 to 3:1;
wherein prior to the reaction according to a), the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.5:1 to 3:1, preferably in the range of from 0.75:1 to 1.5:1;
wherein prior to the reaction according to a), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.9:1 to 1.2:1; wherein the compound of formula (I) comprises a compound of formula (I-1) and a compound of formula (I-2) wherein molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20. It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 85:15 or at least 90:10 or at least 95:5 or at least 99:1 or at least 99.8:0.2; more preferably the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) in the range of from 95:5 to 99.8:0.2, preferably in the range of from 99:1 to 99.8:0.2; More preferably, the compound of formula (I) comprised in the mixture obtained from a) consists of the compound of formula (I-1) and the compound of formula (I-2).
Thus, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 55:45, preferably the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1;
wherein prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 0.1:1 to 5:1, preferably in the range of from 2.5:1 to 4.5:1, more preferably in the range of from 2.5:1 to 4:1, more preferably in the range of from 2.5:1 to 3.5:1; more preferably, prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 1:1 to 3:1;
wherein prior to the reaction according to a), the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.5:1 to 3:1, preferably in the range of from 0.75:1 to 1.5:1;
wherein prior to the reaction according to a), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 1.4:1 to 6:1, preferably in the range of from 1.4:1 to 4.9:1, more preferably in the range of from 2.1:1 to 5.5:1; more preferably in the range of from 2.1:1 to 4.9:1, more preferably in the range of from 3:1 to 5:1; 3:1 to 4.9:1, more preferably in the range of from 3:1 to 4:1.
Generally, it may be conceivable that the reacting according to a) is carried in the absence of an additional solvent. According to the present invention, it is preferred that according to a), the compound of formula (II-0) is reacted with the compound of formula (III) in the presence of the base, in the presence of the Lewis acid, and in the presence of a solvent.
Preferably, the solvent comprises, preferably is, one or more organic solvents, preferably one or more aprotic organic solvents. Generally, every aprotic organic solvent can be employed which allows to carry out the reacting according to a). Preferably, the aprotic organic solvent Comprises, more preferably consists of, one or more of dichloromethane, methyl tert-butyl ether, tetrahydrofuran, dimethylsulphoxide, and dimethylformamide. More preferably, the solvent comprises, preferably is, tetrahydrofuran.
Thus, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1, wherein prior to the reaction according to a), the molar ratio of the base relative to the compound of formula (III) is in the range of from 1:1 to 3:1, the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.75:1 to 1.5:1, and the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 3:1 to 4.9:1, preferably in the range of from 3:1 to 4:1.
The temperature at which the reacting according to a) is carried out can be suitably chosen, depending on the chemical nature of components of the mixture which is subjected to reaction conditions according to a), and in particular, if present, the chemical nature of the solvent. Preferably, the reacting according to a) is carried out at a temperature in the range of from 0 to 80° C., preferably in the range of from 0 to 70° C., more preferably in the range of from 0 to 60° C., more preferably in the range of from 0 to 50° C., more preferably in the range of from 0 to 50° C., more preferably in the range of from 0 to 40° C., more preferably in the range of from 0 to 30° C., more preferably in the range of from 0 to 25° C. More preferably, the reacting according to a) is carried out at a temperature in the range of from 0 to 20° C., more preferably in the range of from 0 to 15° C., more preferably in the range of from 0 to 10° C., more preferably in the range of from 0 to 5° C.
It has been observed that the dynamic resolution occurs at any of the above disclosed temperatures. Room temperature further favors the dynamic resolution. A temperature lower than 15° C., preferably a temperature of 10° C. or less can further increase the efficiency of the process of dynamic resolution.
Generally, the compounds subjected to reacting in a) can be admixed in any sequence. Preferably, the compound of formula (II) is admixed with the compound of formula (III) wherein, if a solvent is used, the compound of formula (II) can be preferably employed dissolved in this solvent; it is further preferred that to the resulting mixture, the Lewis acid is added; it is further preferred that the resulting mixture is then cooled to a temperature in the range of from 0 to 25° C., preferably in the range of from 0 to 15° C., more preferably in the range of from 0 to 10° C., more preferably in the range of from 0 to 5° C. and to the thus cooled mixture, the base is added. After the addition of the base, the temperature is allowed to rise. For example if the addition of the base occurs at 0° C., the temperature is allowed to rise to reach a temperature in the range of from 15 to 25° C.
The period of time for which the reacting according to a) is carried out can be suitably chosen. Preferably, the reacting according to a) is carried out for a period of time in the range of from 0.5 to 48 h, preferably in the range of from 0.75 to 42 h, more preferably in the range of from 1 to 36 h. More preferably, the reacting according to a) is carried out for a period of time in the range of from 1.5 to 20 h, preferably in the range of from 2 to 24 h. Preferred ranges are from 2 to 6 h or from 6 to 10 h or from 10 to 14 h or from 14 to 19 h or from 19 to 24 h. The period of time for which the reacting according to a) is carried out is more preferably in the range of 15 to 24 h.
Preferably, during reacting according to a), the reaction mixture is agitated, preferably mechanically agitated, more preferably stirred. The term “agitation” as used herein relates to any motion of a macroscopic constituent of the reaction mixture which is induced from outside, relative to another macroscopic constituent of the reaction mixture. The term “mechanical agitation” as used herein relates to any motion of a macroscopic constituent of the reaction mixture which is induced from outside via a device, such as shaking or stirring or sonication, relative to another macroscopic constituent of the reaction mixture. The term “stirring” as used herein relates to any motion of a macroscopic constituent of the reaction mixture which is induced from outside via a stirring device, relative to another macroscopic constituent of the reaction mixture.
Preferably, the compound of formula (I) comprised in the mixture obtained from a) is suitably separated from said mixture. Generally, it is preferred that from said separating, a composition is obtained which comprises the compound of formula (I), in particular a composition comprising the compound of formula (I) comprising the compound of formula (I-1) and the compound of formula (I-1), preferably a composition comprising the compound of formula (I) consisting of the compound of formula (I-1) and the compound of formula (I-2). Therefore, the present invention also relates to the process as defined above, further comprising b) separating the compound of formula (I) from the mixture obtained in a).
It is preferred that the compound of formula (I) is separated from the liquid phase of the mixture obtained in a) wherein the separating preferably includes filtration or centrifugation, more preferably filtration. Further, it is preferred that the compound of formula (I) obtained from filtration or centrifugation, preferably filtration, is washed and/or dried, preferably washed and dried. No specific limitations exist regarding the chemical nature of the washing agent. Preferred washing agents include isopropyl acetate. No specific limitations exist for the drying conditions. Preferred drying conditions include a pressure below 1 bar, preferably drying in vacuo. Further, it is preferred that the compound of formula (I), preferably after drying, is further dissolved in one or more solvents, preferably in a solvent used for crystallization and recrystallization as disclosed below.
The thus dissolved compound of formula (I) can be further subjected to extraction, including, for example, extraction with aqueous sodium chloride, obtaining an organic phase from which the solvent is preferably removed whereafter the solid compound of formula (I) is preferably dissolved in one or more further solvents. If extraction is carried, it is, for example, preferred to dissolve the compound of formula (I), after separation from the liquid phase of the mixture obtained in a) and drying, in a first organic solvent, for example, isopropyl acetate, subject the thus obtained solution to extraction, for example with aqueous sodium chloride, obtaining an organic phase from which the solvent is suitably removed, and dissolve the thus obtained solid compound of formula (I) in a second organic solvent, for example toluene.
Therefore, the present invention also relates to the process as defined above, preferably further comprising
Further Steps
It is preferred that in the mixture obtained from b) preferably comprising the compound of formula (I) dissolved in a solvent, preferably an organic solvent, the compound of formula (I-1) is suitably crystallized. From this crystallization, the compound of formula (I) (I) is obtained in its mother liquor from which it is preferably suitably separated.
Therefore, the present invention also relates to the process as defined above, further comprising
Further, the present invention also relates to the process as defined above, further comprising
The compound of formula (I) after c) or after e) or after f) comprises a compound of formula (I-1)
and a compound of formula (I-2)
wherein the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20. It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 85:15 or at least 90:10 or at least 95:5 or at least 99:1 or at least 99.8:0.2. More preferably, the compound of formula (I) comprised in the mixture obtained from a) consists of the compound of formula (I-1) and the compound of formula (I-2).
It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) obtained in step a) and after b) is in the range of from 65:to 35 to 90:10, preferably in the range of from 75:25 to 90:10. It is conceivable that this molar ratio is further improved by crystallization step c) or crystallization step c) and recrystallization step e) up to a molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) in the range of from 95:5 to 99.8:0.2, preferably in the range of from 99:1 to 99.8:0.2.
Hence, it is preferred that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) after c) or e) is increased with respect to the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) of a) and of b). In other words, the crystallization step and the recrystallization steps may further improve the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2). The molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) from d) or from e) i.e. after the crystallization or after recrystallization is at least 95:5, preferably at least 97:3, more preferably at least 99:1, more preferably 99.8:0.2. The molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) from d) or from e) is in the range of from 95:5 to 99.8:0.2, in the range of from 97:3 to 99.8:0.2, more preferably in the range of from 99:1 to 99.8:0.2, more preferably is 99.8:0.2.
During crystallization in c), it can be preferred that suitable seed crystals are added, preferably seed crystals of the compound of formula (I-1).
During recrystallization in e), it can be preferred that suitable seed crystals are added, preferably seed crystals of the compound of formula (I-1).
After the crystallization in c) from which the crystallized compound of formula (I) comprising compounds (I-1) and (1-2) in the molar ratio disclosed above is obtained in its mother liquor, the crystallized compound of formula (I) comprising compounds (I-1) and (1-2) in the molar ratio disclosed above is preferably suitably separated from its mother liquor in d), for example by filtration or centrifugation. The thus separated crystallized compound of formula (I) comprising compounds (I-1) and (1-2) in the molar ratio disclosed above can be subjected to washing, wherein preferred washing agents include a solvent as disclosed below, and subject the optionally washed crystallized compound of formula (I) to drying. Preferred drying conditions include temperatures in the range of from 10 to 60° C., preferably in the range of from 30 to 50° C., and a pressure below ambient pressure.
Therefore, the present invention also relates to the process as defined above, further comprising
The compound of formula (I) comprises, preferably consists of a compound of formula (I-1) and a compound of formula (I-2). It is preferred that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) after c) or from d) or from d3) or from e) i.e. after the crystallization or recrystallization step is increased with respect to the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) from a). In other words, the crystallization step and the recrystallization step may further improve the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2). The molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) after c) or from d) or from d3) or from e) i.e. after the crystallization or recrystallization step is at least 95:5, preferably at least 97:3, more preferably at least 99:1, more preferably 99.8:0.2. The molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is in the range of from 95:5 to 99.8:0.2, preferably in the range of from 97:3 to 99.8:0.2, more preferably in the range of from 99:1 to 99.8:0.2, more preferably is 99.8:0.2.
For the purpose of obtaining the crystalline compound of formula (I) comprising compounds (I-1) and (1-2) with the molar ratio as disclosed above, it is preferred that the crystallization step c) and the recrystallization step of e) is carried in a solvent, preferably in an organic solvent, more preferably an organic solvent selected from the group consisting of a ketone, an ester, an ether, a C1-C7 alkane, a halo-alkane, a nitrile, an aromatic hydrocarbon solvent, an alcohol or a mixture thereof.
Regarding the ketone, it is preferably selected from the group consisting of acetone, methyl isobutyl ketone, diethyl ketone, methyl propyl ketone, methyl isopropyl ketone, acetophenone, and diethyl butyl ketone, optionally in combination with a solvent selected from the group consisting of methyl tert-butyl ether, isopropyl acetate, and toluene.
Regarding the ether, it is preferably selected from the group consisting of methyl tert-butyl ether and tetrahydrofuran.
Regarding the ester, it is preferably selected from the group consisting of ethyl acetate, isopropyl acetate and butyl acetate.
Regarding the C1-C7 alkane, it is preferably selected from a C5-C7 alkane wherein the C5-C7 alkane is selected from the group consisting of cyclohexane and n-heptane, optionally in combination with a solvent selected from the group consisting of methyl tert-butyl ether, isopropyl acetate and toluene.
Regarding the halo-alkane, it is preferably dichloromethane, optionally in combination with a solvent selected from the group consisting of toluene, tetrahydrofuran, acetone, and methyl isobutyl ketone.
Regarding the nitrile, it is preferably acetonitrile, optionally in combination with a solvent selected from the group consisting of diisopropyl ether and tert-butyl methyl ether.
Regarding the aromatic hydrocarbon solvent, it is preferably selected from the group consisting of anisole and toluene.
Regarding the alcohol it is preferably selected from a C1-C8 alcohol, more preferably the alcohol is n-butanol, optionally in combination with heptane.
Hence, it is preferred that the solvent of steps c) and e) is selected from the group consisting of acetone, methyl isobutyl ketone, diethyl ketone, methyl propyl ketone, methyl isopropyl ketone, acetophenone, diethyl butyl ketone, methyl tert-butyl ether, tetrahydrofuran, ethyl acetate, isopropyl acetate, butyl acetate, cyclohexane, a heptane, preferably n-heptane, dichloromethane, acetonitrile, anisole, toluene, n-butanol and a mixture thereof. More preferably the solvent is dichloromethane.
The solvents for crystallization are preferably also used as washing agents.
For the purpose of obtaining the crystalline compound of formula (I) with a molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) improved with respect to the molar ratio of compound of formula (I-1) relative to the compound of formula (I-2) after a), it preferred that the crystallization step c) and the recrystallization step of e) (step e) if carried out) is carried in a solvent, preferably an organic solvent selected from the group of dichloromethane, acetonitrile and anisole or mixture thereof, wherein more preferably the solvent is dichloromethane. In this case, after c) or after e), the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is preferably at least 95:5, more preferably at least 97:3, more preferably at least 99:1, more preferably 99.8:0.2. In this case after c) or after e) the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is in the range of from 95:5 to 99.8:0.2, preferably in the range of from 97:3 to 99.8:0.2, more preferably in the range of from 99:1 to 99.8:0.2, more preferably is 99.8:0.2. More preferably, the solvent is dichloromethane.
It is preferred that the crystallization step c) is carried out at a temperature range in the range of from −10 to 50° C.
It is preferred that recrystallization step of e) is carried out at a temperature range in the range of from −10 to 50° C.
Generally, the present invention also relates to a mixture which is obtainable or obtained by the process of the present invention, preferably obtainable or obtained from step a) of a process of the present invention. More preferably, the present invention relates to a mixture which is obtainable or obtained from step a) of a process as defined above, step a) comprising reacting a compound of formula (II-0)
with a compound of formula (III)
wherein the compound of formula (II-0) comprises a compound of formula (II-a)
and a compound of formula (II-b)
Yet further, the present invention relates to a mixture which may be obtainable or obtained from step a) of the process as defined above, wherein said mixture comprises the compound of formula (I) comprising a compound of formula (I-1)
and a compound of formula (I-2)
said mixture further comprising a base and a Lewis acid and wherein in the mixture, the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20. It is conceivable that in the mixture the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 85:15 or at least 90:10 or at least 95:5 or at least 99:1 or at least 99.8:0.2. More preferably, the compound of formula (I) comprised in the mixture obtained from a) consists of the compound of formula (I-1) and the compound of formula (I-2). It is further conceivable that in the mixture the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is in the range of from 65:to 35 to 90:10, preferably in the range of from 75:25 to 90:10, more preferably in the range of from 95:5 to 99.8:0.2, more preferably in the range of from 99:1 to 99.8:0.2.
Regarding further preferred embodiments of said mixture, reference is made to the disclosure above, in particular regarding preferred molar ratios disclosed above and preferred bases and preferred Lewis acid. Further reference is made to the respective disclosure in the embodiment section of the present application. A preferred mixture of the present invention comprises the compound of formula (I) comprising a compound of formula (I-1)
and a compound of formula (I-2)
wherein in the mixture, the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 85:15, said mixture further comprising a base which is ethyldiisopropylamine, a Lewis acid which is ZnBr2, and preferably a solvent which is preferably tetrahydrofuran.
Preferably, this mixture is used for obtaining the compound of formula
wherein obtaining the compound of formula (I-1) preferably comprises separating the compound of formula (I) from the mixture and crystallizing the compound of formula (I), obtaining the crystallized compound of formula (I) in its mother liquor and separating the crystallized compound of formula (I) from its mother liquor, wherein as mentioned above after the crystallization or recrystallization step the molar ratio of compound of formula (I-1) relative to the compound of formula (I-2) may be increased with respect to the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) of a). In other words, the crystallization step and recrystallization steps further improve the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2). The molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) after the crystallization or recrystallization is at least 95:5, preferably at least 97:3, more preferably at least 99:1, more preferably is 99.8:0.2.
As mentioned above, the process of the present invention allows the diastereoselective preparation of the compound of formula (I-1) based on a phosphoramidate derivative having a succinimide group as the leaving group. This reaction is based on a specific starting mixture which is subjected to reaction conditions. Therefore, the present invention also relates to this novel mixture which comprises a compound of formula (II-0)
and a compound of formula (III)
and a Lewis acid and a base, wherein the compound of formula (II-0) comprises a compound of formula (II-a)
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45.
Preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, preferably in the range of from 54:46 to 46: 54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
Regarding further preferred embodiments of said mixture, reference is made to the disclosure above, in particular regarding preferred molar ratios disclosed above and preferred bases and preferred Lewis acid. Further reference is made to the respective disclosure in the embodiment section of the present application. A preferred mixture of the present invention comprises a compound of formula (II-0)
and a compound of formula (III)
and a base which is ethyldiisopropylamine and a Lewis acid which is ZnBr2, wherein the compound of formula (II-0) comprises a compound of formula (II-a)
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45; more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1; wherein the molar ratio of the base relative to the compound of formula (III) is in the range of from 1.5:1 to 2:1, the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 2:1 to 6:1, and the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.25 to 1.5:1, the mixture preferably comprising a solvent, more preferably tetrahydrofuran.
Preferably, this mixture is used for obtaining the compound of formula
wherein obtaining the compound of formula (I-1) preferably comprises subjecting the mixture to reaction conditions obtaining a mixture comprising the compound of formula (I), separating the compound of formula (I) from the mixture and crystallizing the compound of formula (I-1), obtaining the crystallized compound of formula (I-1) in its mother liquor and separating the crystallized compound of formula (I-1) from its mother liquor.
As also mentioned above, the use of this mixture allows improving the diastereoselectivity to the compound of formula (I-1) when using the phosphoramidate derivative having a succinimide group as the leaving group as starting material. Thus, the present invention also relates to the use of this mixture for improving the selectivity of the reaction of a compound of formula (III) with a compound of formula (II-0) to the compound of formula (I-1)
obtained from said reaction,
wherein the compound of formula (II-0) comprises a compound of formula (II-a) and a compound of formula (II-b), wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45; more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51; more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1. More preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
Further, the present invention relates to a method for improving the selectivity of the reaction of a compound of formula (III) with a compound of formula (II-0) to the compound of formula (I-1)
obtained from said reaction,
wherein the compound of formula (II-0) comprises a compound of formula (II-a) and a compound of formula (II-b), wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45; more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51; more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1; wherein more preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b) and
wherein said method comprises employing the above-mentioned mixture as starting material in said reaction.
Generally, it was found that the Lewis acid and the base as disclosed above in combination lead to an increase of the diastereoselectivity of the compound of formula (I-1) relative to the compound of formula (I-2). It has been further seen that an excess of equivalents of compound (II) relative to compound (III) leads to an increase of the diastereoselectivity of the compound of formula (I-1) relative to the compound of formula (I-2). It was further found that a low temperature preferably a temperature lower than 15° C., more preferably in the range of from 10 to 0° C. further increases the diastereoselectivity of the reaction in favor of compound (I-1).
Generally, it was found that in particular an improved selectivity of the reaction of the compound of formula (II-0) with the compound of formula (III) to the compound of formula (I-1) is obtained when using a phosphoramidate derivative having a succinimide group as the leaving group as starting material.
Thus, the present invention also relates to the use of a combination of a Lewis acid and a base for improving the selectivity of the reaction of a compound of formula (III)
with a compound of formula (II-0)
to the compound of formula (I-1)
obtained from said reaction,
said compound of formula (II-0) comprising a compound of formula (II-a)
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45; more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51; more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1; and wherein more preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b).
Regarding further preferred combinations, reference is made to the disclosure above, in particular regarding preferred molar ratios disclosed above and preferred bases and preferred Lewis acids. Further reference is made to the respective disclosure in the embodiment section of the present application. According to preferred respective use of the present invention, the base is ethyldiisopropylamine and the Lewis acid is ZnBr2. Further, the present invention relates to a method for improving the selectivity of the reaction of a compound of formula (III)
with a compound of formula (II-0)
to the compound of formula (I-1)
obtained from said reaction,
said compound of formula (II-0) comprising a compound of formula (II-a)
and a compound of formula (II-b)
wherein the molar ratio of the compound of formula (II-a) relative to the compound of formula (II-b) is in the range of from 45:55 to 72:28, preferably in the range of from 45:55 to 60:40, more preferably in the range of from 45:55 to 55:45; wherein preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is in the range of from 55:45 to 45:55, preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51; wherein more preferably, the molar ratio of the compound of formula (II-a) relative the compound of formula (II-b) is 1:1 and wherein more preferably, the compound of formula (II-0) consists of the compound of formula (II-a) and the compound of formula (II-b);
wherein said method comprises employing a combination of a Lewis acid and a base as starting material in said reaction.
Further preferred mixtures, compounds, and uses are explicitly mentioned in the embodiment section hereinbelow.
The present invention further relates to a process for preparing of a compound of formula (I)
or a salt thereof, the process comprising
Preferably, in particular in case the compound of formula (II) is
and the compound of formula (III) is
the hydrogen chloride binding base according to a′) is not, preferably does not comprise, N-methylimidazole with the proviso that if according to a′), a Lewis acid is used in combination with the hydrogen chloride binding base, the hydrogen chloride binding base may comprise or may be N-methylimidazole.
Preferably, the residue R4 is phenyl, naphthyl, quinolinyl, isoquinolinyl, quinazolinyl or quinoxalinyl, each optionally substituted with at least one of C1-C6 alkyl, C1-C6 alkoxy, C3-C6 cycloalkyl, aryl, halogen, C(O)OH, CHO, C(O)(C1-C6 alkyl), C(O)(aryl), C(O)O(C1-C6 alkyl), C(O)ONH2, C(O)ONH(C1-C6 alkyl) and CN. The term “C1-C6 alkyl” as used herein refers to alkyl residues having 1, 2, 3, 4, 5, or 6 carbon atoms. The term “C1-C6 alkoxy” as used herein refers to alkoxy residues having 1, 2, 3, 4, 5, or 6 carbon atoms. The term “C3-C6 cycloalkyl” as used herein refers to cycloalkyl residues wherein 3, 4, 5, or 6 carbon atoms constitute the ring structure.
Preferably, the residues R2 and R3 are independently H or C1-C6 alkyl optionally substituted with at least one of OH, C1-C6 alkoxy, aryl, heteroaryl, C1-C6 alkyl, C3-C6 cycloalkyl, F, Cl, Br, I, NO2, C(O)OH, CHO, C(O)(C1-C6 alkyl), C(O)(aryl), C(O)O(C1-C6 alkyl), C(O)ONH2, C(O)ONH(C1-C6 alkyl) and CN.
Preferably, the residue R6 is C1-C6 alkyl or C3-C10 cycloalkyl optionally substituted with at least one of C1-C6 alkyl and aryl.
Preferably, R1 is an optionally derivatized purinyl residue, including an adenine residue and a guanine residue, or an optionally derivatized pyrimidinyl residue, including a cytosine residue, a thymine residue and an uracil residue, linked to the furanose ring according to formula (III) through a carbon or nitrogen atom.
Preferably, R7 and R8 are independently H, OH, F, Cl, Br, I, azide, nitrile, NH2, NHR26, NR26R24, C(O)NH2, C(O)NHR26, C(O)NR26R24, C1-C6 alkyl optionally substituted with C1-C6 alkyl, or C3-C10 cycloalkyl optionally substituted with C1-C6 alkyl, wherein R26 and R24 are independently C1-C6 alkyl.
Preferably, R9 is H, OH, C1-C6 alkoxy, OC(O)R25, or C1-C6 alkyl optionally substituted with C1-C6 alkyl or aryl, wherein R25 is C1-C6 alkyl or aryl.
Step a′)
The P atom is a chirality center of the compound of formula (II). It is preferred that according to a′), the compound of formula (II) comprises a compound of formula (II-1)
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, more preferably in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1. More preferably, the compound of formula (II) consists of the compound of formula (II-1) and the compound of formula (II-2).
Preferably, from step a′) of the process of the present invention, a mixture is obtained which comprises the compound of formula (I) wherein the compound of formula (I) comprises a compound of formula (I-1)
and a compound of formula (I-2)
It is preferred that in the mixture obtained from a′), the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, more preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20. It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) may be at least 85:15 or at least 90:10 or at least 95:5 or at least 99:1. More preferably, the compound of formula (I) comprised in the mixture obtained from a′) consists of the compound of formula (I-1) and the compound of formula (I-2).
Preferably, one of R7 and R8 may be C1-C6 alkyl, preferably methyl, and one of R7 and R8 may be F, Cl, OH, CN, or NH2. Further preferably, R1 may be an optionally derivatized pyrimidinyl residue, preferably a uracil residue. Also preferably, R1 may be an optionally derivatized purinyl residue. Therefore, among others, the following compounds of formula (I) may be preferably prepared by the process of the present invention:
Preferably, regarding the compound of formula (III) employed in a′), the residues R7 and R8 are independently H or methyl.
More preferably, the compound of formula (III) is
more preferably
more preferably
Preferably, the compound of formula (II-1) is a compound of formula
and the compound of formula (II-2) is a compound of formula
Therefore, it is preferred that the compound of formula (I-1) is a compound
and the compound of formula (I-2) is a compound
Even more preferably, the compound of formula (III) employed in a′) is a compound of formula
the compound of formula (II) is a compound of formula
and the compound of formula (I) is a compound of formula
Therefore, the present invention relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, with the proviso that if according to a, a Lewis acid is used in combination with the hydrogen chloride binding base, the hydrogen chloride binding base may comprise or may be N-methylimidazole.
The hydrogen chloride binding base employed in a′) is preferably an organic base, more preferably an organic nitrogenous base, more preferably a tertiary organic nitrogenous base. More preferably, the organic hydrogen chloride binding base comprises one or more of an amine, an amidine, and a heteroaromatic compound comprising a basic ring-nitrogen atom. More preferably, the organic hydrogen chloride binding base comprises one or more of ethyldiisopropylamine, triethylamine, diethylamine, 1,8-diazabicycloundec-7-ene, pyridine, quinoline, isoquinoline, acridine, pyrazine, imidazole, benzimidazole, and pyrazole. More preferably, the organic hydrogen chloride binding base consists of one or more of ethyldiisopropylamine, triethylamine, diethylamine, 1,8-diazabicycloundec-7-ene, pyridine, quinoline, isoquinoline, acridine, pyrazine, imidazole, benzimidazole, and pyrazole. More preferably, the hydrogen chloride binding base comprises triethylamine. More preferably, the hydrogen chloride binding base is triethylamine.
It is further contemplated that in the process as disclosed above, when step a′) is carried out in a solvent, the solvent is not an anhydrous solvents selected from dichloromethane, 2-methyl tetrahydrofuran, tetrahydrofuran, methyl-t-butyl ether, ethyl acetate, acetonitrile, cyclopentyl methylether, 1,4-dioxane, acetone, methyl ethyl ketone, methyl isobutyl ketone, diisopropyl ethyl amine, tripropylamine, tributylamine and their combinations or any functional equivalent thereof. In this embodiment the carrying out of step a′) preferably does not comprise the use of a Lewis acid.
In the process as disclosed above, it is further contemplated that the base is not selected from tripropyl amine, tributyl amine, diisopropyl ethyl amine, and their combinations, or any functional equivalent thereof. In this embodiment the carrying out of step a′) preferably does not comprise the use of a Lewis acid.
In the process as disclosed above, it is further contemplated that that the base selected from tripropylamine, tributylamine, diisopropylethylamine or any functional equivalent bases is not in combination with a solvent selected from dichloromethane, 2-methyl tetrahydrofuran, tetrahydrofuran, methyl-t-butyl ether, ethyl acetate, acetonitrile, cyclopentyl methylether, 1,4-dioxane, acetone, methyl ethyl ketone, methyl isobutyl ketone, diisopropyl ethyl amine, tripropylamine. In this embodiment the carrying out of step a′) preferably does not comprise the use of a Lewis acid.
In the process as disclosed above, it is further contemplated that that when the base is tripropylamine the solvent is not acetone or methyl-isobutyl-ketone or methyl-t-butyl ether or ethyl acetate or that when the base is diisopropylethylamine the solvent is not methyl-t-butyl ether or that when the base is THF the solvent is not tributylamine. In this embodiment the carrying out of step a′) preferably does not comprise the use of a Lewis acid.
Therefore, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably being 1:1.
Therefore, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably being 1:1.
Preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 54:46 to 46:54, more preferably in the range of from 53:47 to 47:53, more preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51. More preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1. It is preferred that the compound of formula (II) employed in (a′) consists of the compound of formula (II-1) and the compound of formula (II-2).
Therefore, the present invention relates to the process as defined above, wherein the compound of formula (II) employed in a) consists of the compound of formula (II-1) and the compound of formula (II-2), wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1.
Regarding possible methods to prepare the compound of formula (II), reference is made, for example, to WO 2008/121634 A, Example 25, the respective content of which document is included herein by reference. Regarding possible methods to prepare the compound of formula (III), reference is made, for example, to WO 2008/121634 A, Example 4, the respective content of which document is included herein by reference.
As mentioned above, the process of the present invention is characterized by an advantageous diastereoselectivity to the valuable product, the compound of formula (I-1). Thus, it is preferred that in the mixture obtained from a′), the compound of formula (I) comprises a compound of formula (I-1)
and a compound of formula (I-2)
wherein the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is greater than 55:45, preferably at least 60:40. More preferably, said molar ratio is at least 65:35, more preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20. It is conceivable that the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) may be at least 85:15 or at least 90:10 or at least 95:5 or at least 99:1. More preferably, the compound of formula (I) comprised in the mixture obtained from a′) consists of the compound of formula (I-1) and the compound of formula (I-2).
Therefore, the present invention relates to the process as defined above, wherein the compound of formula (II) employed in a′) consists of the compound of formula (II-1) and the compound of formula (II-2), wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1, wherein the compound of formula (I) comprised in the mixture obtained from a′) consists of the compound of formula (I-1) and the compound of formula (I-2), and wherein the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, preferably at least 80:20.
Regarding the amount of the hydrogen chloride binding base relative to the amount of the compound of formula (III) employed in a′), no specific restrictions exist. Preferably, prior to the reaction according to a′), the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is in the range of from 0.1:1 to 5:1. More preferably, prior to the reaction according to a′), the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is in the range of from 0.5:1 to 5:1, more preferably in the range of from 1:1 to 5:1, more preferably in the range of from 2:1 to 5:1. More preferably, prior to the reaction according to a′), the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is in the range of from 2:1 to 4:1, more preferably in the range of from 2.5:1 to 4.5:1, more preferably in the range of from 2.5:1 to 4:1, more preferably in the range of from 2.5:1 to 3.5:1.
Therefore, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably being 1:1, and wherein prior to the reaction according to a′), the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is in the range of from 0.5:1 to 5:1, preferably in the range of from 2.5:1 to 3.5:1.
Further according to the present invention, it was found that the diastereoselectivity to the compound of formula (I-1), in particular the compound
can be even more improved if the compound of formula (III) is reacted with the compound of formula (II) in the presence of the hydrogen chloride binding base and a Lewis acid.
No specific restrictions exist with regard to the chemical nature of the Lewis acid employed in a′). Preferably, the Lewis acid comprises a twice positively charged ion or a three times positively charged ion, more preferably a twice positively charged metal ion or a three times positively charged metal ion. Generally, it is also conceivable that the Lewis acid comprises a twice positively charged ion and a three times positively charged ion, preferably a twice positively charged metal ion and a three times positively charged metal ion. With regard to the twice positively charged ion, it is preferred that it comprises, more preferably is, a Zn ion, a Mg ion, a Cu ion, or an Fe ion. More preferably, the twice positively charged ion comprises, more preferably is, a Zn ion or a Mg ion. More preferably, the twice positively charged ion comprises, more preferably is, a Zn ion. With regard to the three times positively charged ion, it is preferred that it comprises, more preferably is, a Mn ion.
Regarding the Lewis acid comprising a twice positively charged ion comprising, more preferably being, a Zn ion, no specific restrictions exist. Preferred Lewis acids comprise, more preferably are, Zn halides. More preferably, the Lewis acid comprises, preferably is, one or more of ZnBr2, ZnCl2, and ZnI2. More preferably, the Lewis acid comprises, preferably is, ZnBr2.
It is also conceivable that the Lewis acid is one or more of ZnBr2, ZnCl2, ZnI2, MgBr2, MgBr2.OEt2, CuCl2, Cu(acetylacetonate)2, and Fe(II) fumarate.
Regarding the Lewis acid comprising a three times positively charged ion comprising, more preferably being, a Mn ion, no specific restrictions exist. Preferred Lewis acids comprise, more preferably are, Mn(acetylacetonate)3.
Regarding the amount of the Lewis acid relative to the amount of the compound of formula (III) employed in a′), no specific restrictions exist. Preferably, prior to the reaction according to a′), the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.1:1 to 5:1. More preferably, prior to the reaction according to a′), the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.2:1 to 5:1, preferably in the range of from 0.5:1 to 3:1, more preferably in the range of from 0.75:1 to 1.5:1, more preferably in the range of from 0.75:1 to 1.25:1.
Thus, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably being 1:1, wherein prior to the reaction according to a′), the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is preferably in the range of from 0.5:1 to 5:1, more preferably in the range of from 2.5:1 to 3.5:1, and wherein prior to the reaction according to a′), the molar ratio of the Lewis acid relative to the compound of formula (III) is preferably in the range of from 0.1:1 to 5:1, more preferably in the range of from 0.75:1 to 1.5:1.
Regarding the amount of the compound of formula (II) employed in a′) relative to the amount of the compound of formula (III) employed in a′), no specific restrictions exist. Preferably, prior to the reaction according to a′), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.5:1 to 5:1. More preferably, prior to the reaction according to a′), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.6:1 to 4:1, more preferably in the range of from 0.7:1 to 3:1. More preferably, prior to the reaction according to a′), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.8:1 to 2:1, more preferably in the range of from 0.9:1 to 1.2:1.
Thus, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably being 1:1, wherein prior to the reaction according to a′), the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is preferably in the range of from 0.5:1 to 5:1, more preferably in the range of from 2.5:1 to 3.5:1, wherein prior to the reaction according to a′), the molar ratio of the Lewis acid relative to the compound of formula (III) is preferably in the range of from 0.1:1 to 5:1, more preferably in the range of from 0.75:1 to 1.5:1, and wherein prior to the reaction according to a′), the molar ratio of the compound of formula (II) relative to the compound of formula (III) is preferably in the range of from 0.5:1 to 5:1, more preferably in the range of from 0.9:1 to 1.2:1.
Generally, it may be conceivable that the reacting according to a′) is carried in the absence of an additional solvent. According to the present invention, it is preferred that according to a′), the compound of formula (II) is reacted with the compound of formula (III) in the presence of the hydrogen chloride binding base, preferably in the presence of the Lewis acid, and in the presence of a solvent.
Preferably, the solvent comprises, preferably is, one or more organic solvents, preferably one or more aprotic organic solvents. Generally, every aprotic organic solvent can be employed which allows to carry out the reacting according to a′). Preferably, the aprotic organic solvent Comprises, more preferably consists of, one or more of methylene chloride, methyl tert-butyl ether, tetrahydrofuran, dimethylsulphoxide, and dimethylformamide. More preferably, solvent comprises, preferably is, tetrahydrofuran.
Thus, the present invention preferably relates to a process for preparing a compound of formula (I)
or a salt thereof, wherein the process comprises
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1, wherein prior to the reaction according to a′), the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is in the range of from 2.5:1 to 3.5:1, the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.75:1 to 1.5:1, and the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.9:1 to 1.2:1.
The temperature at which the reacting according to a′) is carried out can be suitably chosen, depending on the chemical nature of components of the mixture which is subjected to reaction conditions according to a′), and in particular, if present, the chemical nature of the solvent. Preferably, the reacting according to a′) is carried out at a temperature in the range of from 0 to 80° C., more preferably in the range of from 0 to 70° C., more preferably in the range of from 0 to 60° C., more preferably in the range of from 0 to 50° C., more preferably in the range of from 0 to 50° C., more preferably in the range of from 0 to 40° C., more preferably in the range of from 0 to 30° C., more preferably in the range of from 0 to 25° C. More preferably, the reacting according to a′) is carried out at a temperature in the range of from 0 to 20° C., more preferably in the range of from 0 to 15° C., more preferably in the range of from 0 to 10° C., more preferably in the range of from 0 to 5° C.
In particular in case the reaction according to a′) is carried out in the presence of the hydrogen chloride binding base without a Lewis acid, it may be preferred to carry out the reacting at two or more temperatures, preferably at two temperatures. In this case, it is preferred that in a first reacting stage, the reacting is carried out at a temperature in the range of from 0 to 10° C., preferably in the range of from 0 to 5° C., and that in a subsequent second reacting stage, the reacting is carried out at a temperature in the range of from 15 to 40° C., preferably in the range of from 20 to 30° C.
Generally, the compounds subjected to reacting in a′) can be admixed in any sequence. Preferably, in case no Lewis acid is employed, the compound of formula (II) is admixed with the compound of formula (III) wherein, if a solvent is used, the compound of formula (II) can be preferably employed dissolved in this solvent; it is further preferred that the resulting mixture is then cooled to a temperature in the range of from 0 to 15° C., more preferably in the range of from 0 to 10° C., more preferably in the range of from 0 to 5° C. and to the thus cooled mixture, the hydrogen chloride binding base is added. Preferably, in case a Lewis acid is employed, the compound of formula (II) is admixed with the compound of formula (III) wherein, if a solvent is used, the compound of formula (II) can be preferably employed dissolved in this solvent; it is further preferred that to the resulting mixture, the Lewis acid is added; it is further preferred that the resulting mixture is then cooled to a temperature in the range of from 0 to 15° C., more preferably in the range of from 0 to 10° C., more preferably in the range of from 0 to 5° C. and to the thus cooled mixture, the hydrogen chloride binding base is added.
The period of time for which the reacting according to a′) is carried out can be suitably chosen. Preferably, the reacting according to a′) is carried out for a period of time in the range of from 0.5 to 48 h, more preferably in the range of from 0.75 to 42 h, more preferably in the range of from 1 to 36 h. More preferably, the reacting according to a′) is carried out for a period of time in the range of from 1.5 to 20 h, more preferably in the range of from 2 to 24 h. Preferred ranges are from 2 to 6 h or from 6 to 10 h or from 10 to 14 h or from 14 to 19 h or from 19 to 24 h.
Preferably, during reacting according to a′), the reaction mixture is agitated, more preferably mechanically agitated, more preferably stirred. The term “agitation” as used herein relates to any motion of a macroscopic constituent of the reaction mixture which is induced from outside, relative to another macroscopic constituent of the reaction mixture. The term “mechanical agitation” as used herein relates to any motion of a macroscopic constituent of the reaction mixture which is induced from outside via a device, such as shaking or stirring or sonication, relative to another macroscopic constituent of the reaction mixture. The term “stirring” as used herein relates to any motion of a macroscopic constituent of the reaction mixture which is induced from outside via a stirring device, relative to another macroscopic constituent of the reaction mixture.
Step b′)
Preferably, the compound of formula (I) comprised in the mixture obtained from a′) is suitably separated from said mixture. Generally, it is preferred that from said separating, a composition is obtained which comprises the compound of formula (I), in particular a composition comprising the compound of formula (I) comprising the compound of formula (I-1) and the compound of formula (I-2), preferably a composition comprising the compound of formula (I) consisting of the compound of formula (I-1) and the compound of formula (I-2). Therefore, the present invention also relates to the process as defined above, further comprising b′) separating the compound of formula (I) from the mixture obtained in a′).
It is preferred that the compound of formula (I) is separated from the liquid phase of the mixture obtained in a′) wherein the separating preferably includes filtration or centrifugation, more preferably filtration. Further, it is preferred that the compound of formula (I) obtained from filtration or centrifugation, preferably filtration, is washed and/or dried, preferably washed and dried. No specific limitations exist regarding the chemical nature of the washing agent. Preferred washing agents include isopropyl acetate. No specific limitations exist for the drying conditions. Preferred drying conditions include a pressure below 1 bar, preferably drying in vacuo. Further, it is preferred that the compound of formula (I), preferably after drying, is further dissolved in one or more solvents, including, for example, toluene and/or isopropyl acetate.
The thus dissolved compound of formula (I) can be further subjected to extraction, including, for example, extraction with aqueous sodium chloride, obtaining an organic phase from which the solvent is preferably removed whereafter the solid compound of formula (I) is preferably dissolved in one or more further solvents. If extraction is carried, it is, for example, preferred to dissolve the compound of formula (I), after separation from the liquid phase of the mixture obtained in a′) and drying, in a first organic solvent, for example, isopropyl acetate, subject the thus obtained solution to extraction, for example with aqueous sodium chloride, obtaining an organic phase from which the solvent is suitably removed, and dissolve the thus obtained solid compound of formula (I) in a second organic solvent, for example toluene.
Therefore, the present invention also relates to the process as defined above, preferably further comprising
It is preferred that in the mixture obtained from b′) preferably comprising the compound of formula (I) dissolved in a solvent, preferably an organic solvent, the compound of formula (I-1) is suitably crystallized. From this crystallization, the compound of formula (I-1) is obtained in its mother liquor from which it is preferably suitably separated.
Therefore, the present invention also relates to the process as defined above, further comprising
Further, the present invention also relates to the process as defined above, further comprising
During crystallization in c′), it can be preferred that suitable seed crystals are added, preferably seed crystals of the compound of formula (I-1).
After the crystallization in c′) from which the crystallized compound of formula (I-1) is obtained in its mother liquor, the crystallized compound of formula (I-1) is preferably suitably separated from its mother liquor in d′), for example by filtration or centrifugation. The thus separated crystallized compound of formula (I-1) can be subjected to washing, wherein preferred washing agents include methyl tert-butyl ether, dichloromethane and mixtures thereof, and subject the optionally washed crystallized compound of formula (I-1) to drying. Preferred drying conditions include temperatures in the range of from 10 to 60° C., preferably in the range of from 30 to 50° C., and a pressure below ambient pressure.
Therefore, the present invention also relates to the process as defined above, further comprising
Generally, the present invention also relates to a mixture which is obtainable or obtained by the process of the present invention, preferably obtainable or obtained from step a′) of a process of the present invention. More preferably, the present invention relates to a mixture which is obtainable or obtained from step a′) of a process as defined above, step a′) comprising reacting a compound of formula (II)
with a compound of formula (III)
wherein the compound of formula (II) comprises a compound of formula (II-1)
and a compound of formula (II-2)
Yet further, the present invention relates to a mixture which may be obtainable or obtained from step s) of the process as defined above, wherein said mixture comprises the compound of formula (I) comprising a compound of formula (I-1)
and a compound of formula (I-2)
wherein the mixture, the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 65:35, preferably at least 70:30, more preferably at least 75:25, more preferably at least 80:20, said mixture further comprising a hydrogen chloride binding base, which is not N-methylimidazole, with bound hydrogen chloride. Regarding further preferred embodiments of said mixture, reference is made to the disclosure above, in particular regarding preferred molar ratios disclosed above and preferred hydrogen chloride bases and, preferably, preferred Lewis bases. Further reference is made to the respective disclosure in the embodiment section of the present application. A preferred mixture of the present invention comprises the compound of formula (I) comprising a compound of formula (I-1)
and a compound of formula (I-2)
wherein in the mixture, the molar ratio of the compound of formula (I-1) relative to the compound of formula (I-2) is at least 80:20, said mixture further comprising a hydrogen chloride binding base which is triethylamine with bound hydrogen chloride, a Lewis base which is ZnBr2, and preferably a solvent which is preferably tetrahydrofuran.
Preferably, this mixture is used for obtaining the compound of formula
wherein obtaining the compound of formula (I-1) preferably comprises separating the compound of formula (I) from the mixture and crystallizing the compound of formula (I-1), obtaining the crystallized compound of formula (I-1) in its mother liquor and separating the crystallized compound of formula (I-1) from its mother liquor.
As mentioned above, the process of the present invention allows the diastereoselective preparation of the compound of formula (I-1) based on a phosphoric acid chloride. This reaction is based on a specific starting mixture which is subjected to reaction conditions. Therefore, the present invention also relates to this novel mixture which comprises a compound of formula (II)
and a compound of formula (III)
and a hydrogen chloride binding base which is not N-methylimidazole, wherein the compound of formula (II) comprises a compound of formula (II-1)
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51, wherein more preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1.
Regarding further preferred embodiments of said mixture, reference is made to the disclosure above, in particular regarding preferred molar ratios disclosed above and preferred hydrogen chloride bases and, preferably, preferred Lewis bases. Further reference is made to the respective disclosure in the embodiment section of the present application. A preferred mixture of the present invention comprises a compound of formula (II)
and a compound of formula (III)
and a hydrogen chloride binding base which is triethylamine and a Lewis base which is ZnBr2, wherein the compound of formula (II) comprises a compound of formula (II-1)
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1, the molar ratio of the hydrogen chloride binding base relative to the compound of formula (III) is in the range of from 2.5:1 to 3.5:1, the molar ratio of the compound of formula (II) relative to the compound of formula (III) is in the range of from 0.9:1 to 1.2:1, and the molar ratio of the Lewis acid relative to the compound of formula (III) is in the range of from 0.75 to 1.5:1, the mixture preferably comprising a solvent, more preferably tetrahydrofuran.
Preferably, this mixture is used for obtaining the compound of formula
wherein obtaining the compound of formula (I-1) preferably comprises subjecting the mixture to reaction conditions obtaining a mixture comprising the compound of formula (I), separating the compound of formula (I) from the mixture and crystallizing the compound of formula (I-1), obtaining the crystallized compound of formula (I-1) in its mother liquor and separating the crystallized compound of formula (I-1) from its mother liquor.
As also mentioned above, the use of this mixture allows improving the diastereoselectivity to the compound of formula (I-1) when using the phosphoric acid chloride as starting material. Thus, the present invention also relates to the use of this mixture for improving the selectivity to the compound of formula (I-1)
of the reaction of a compound of a compound of formula (III) with a compound of formula (II) comprising a compound of formula (II-1) and a compound of formula (II-2) wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51, wherein more preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1. Further, the present invention relates to a method for improving the selectivity to the compound of formula (I-1)
of the reaction of a compound of a compound of formula (III) with a compound of formula (II) comprising a compound of formula (II-1) and a compound of formula (II-2) wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51, wherein more preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1, wherein said method comprises employing the above-mentioned mixture as starting material in said reaction.
Generally, it was found that in particular the combination of a Lewis acid and a hydrogen chloride binding base lead to such an improved selectivity to the compound of formula (I-1) when using the phosphoric acid chloride as starting material.
Thus, the present invention also relates to the use of a combination of a Lewis acid and a hydrogen chloride binding base which is not N-methylimidazole for improving the selectivity to the compound of formula (I-1)
of the reaction of a compound of a compound of formula (III)
with a compound of formula (II)
said compound of formula (II) comprising a compound of formula (I1)
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51, wherein more preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1. Regarding further preferred combinations, reference is made to the disclosure above, in particular regarding preferred molar ratios disclosed above and preferred hydrogen chloride bases and preferred Lewis bases. Further reference is made to the respective disclosure in the embodiment section of the present application. According to preferred respective use of the present invention, the hydrogen chloride binding base is triethylamine and the Lewis acid is ZnBr2. Further, the present invention relates to a method for improving the selectivity to the compound of formula (I-1)
of the reaction of a compound of a compound of formula (III)
with a compound of formula (II)
said compound of formula (II) comprising a compound of formula (II-1)
and a compound of formula (II-2)
wherein the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is in the range of from 55:45 to 45:55, preferably in the range of from 52:48 to 48:52, more preferably in the range of from 51:49 to 49:51, wherein more preferably, the molar ratio of the compound of formula (II-1) relative the compound of formula (II-2) is 1:1, wherein said method comprises employing a combination of a Lewis acid and a hydrogen chloride binding base which is not N-methylimidazole as starting material in said reaction.
Further preferred mixtures, compounds, and uses are explicitly mentioned in the embodiment section hereinbelow.
The present invention related to process carried out in the presence of a base and a Lewis acid is further illustrated by the following embodiments and combinations of embodiments as given by the respective dependencies and references.
The present invention, relating to a process wherein Cl is used as a leaving group, is further illustrated by the following embodiments and combinations of embodiments resulting from the given dependencies and back-references:
The present invention is further illustrated by the following examples, comparative examples, and references examples.
In a dry two-neck round bottom flask equipped with a dropping funnel was dissolved crude phosphoryl chloride (IV) prepared according J. Org. Chem 2011, 76, 8311 (20 g, 43.8 mmol, 1 equiv, 67% w/w purity by NMR) in dichloromethane (140 mL) and the solution was cooled to ca. 5° C. with an ice bath. N-hydroxysuccinimide (7.53 g, 65.4 mmol, 1 equiv) was added (only partial dissolution).
To this suspension, triethylamine (10 mL, 71.9 mmol, 1.1 equiv) in dichloromethane (20 mL) was added dropwise with stirring, and the dropping funnel was rinsed with a further 5 mL of dichloromethane, whereby all of N-hydroxysuccinimide dissolved and a precipitation of triethylamine hydrochloride was observed. The ice bath was removed, the reaction mixture was allowed to warm up to room temperature and extracted with 90 mL of distilled water. The organic phase was washed with a further 40 mL of distilled water and the volatiles were removed under reduced pressure. The crude solid was dissolved in 160 mL MTBE (methyl tert-butyl ether), charged with 5 mL triethylamine and left to stir overnight, upon which a solid agglomerate was formed. The mixture was diluted with 75 mL of MTBE and warmed up to 50° C. until all of the solid dissolved. Upon cooling, crystals formed which were filtered and dried to give 10.53 g of II-a′(dr 67:33).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added N-hydroxysuccinimide phosphoramidate II-a′ with dr=76:33 (Sp:Rp) (463 mg, 1.20 mmol, 1.56 equiv) prepared according to Example 1.1 and THF (2.5 mL, anhydrous) to obtain a clear solution.
To this solution was added 2′-deoxy-2′-fluoro-2′C-methyluridine III (200 mg, 0.77 mmol, 1 equiv), followed by ZnBr2 (173 mg, 0.77 mmol, 1 equiv), 4 Å molecular sieves (235 mg) and Et3N (320 mL, 2.31 mmol, 3 equiv). The mixture was stirred at room temperature for 4 hours. HPLC analysis with individual response factor correction indicated 3% of unreacted nucleoside III, 94% of sofosbuvir (I) with dr=87:13 (Sp:Rp), and 2% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added N-hydroxysuccinimide phosphoramidate II-a′ with dr=72:28 (Sp:Rp) (493 mg, 1.28 mmol, 1.67 equiv) prepared according to Example 1.1 (further crystallized in MTBE to obtain (Sp)-2 with a dr 72:28) and THF (2.5 mL, anhydrous) to obtain a clear solution.
To this solution was added 2′-deoxy-2′-fluoro-2′C-methyluridine III (200 mg, 0.77 mmol, 1 equiv), followed by ZnBr2 (173 mg, 0.77 mmol, 1 equiv), 4 Å molecular sieves (235 mg) and Et3N (320 mL, 2.31 mmol, 3 equiv). The mixture was stirred at room temperature for 4 hours. HPLC analysis with individual response factor correction indicated complete conversion of III, 95% of sofosbuvir (I) with dr=89:11 (Sp:Rp), and 5% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
In a jacketed reactor equipped with a mechanical stirrer, a nitrogen bubbler and a dropping funnel was dissolved L-alanine isopropyl ester (20.0 g, 119.3 mmol, 1 equiv) in THF (200 mL) and the internal temperature set to 0° C. To this solution, phenyl phosphorodichloridate (18.8 mL, 95% purity, 119.5 mmol, 1 equiv) was added at 20° C., followed by a dropwise addition of triethylamine (34.8 mL, 250 mmol, 2.1 equiv) over 2 h at 0-7° C., upon which a white precipitate was formed. The solution was stirred at 0° C. for 2 h 20 min. N-hydroxysuccinimide (17.8 g, 154.7 mmol, 1.3 equiv) was added, followed by additional triethylamine (24.8 mL, 177.9 mmol, 1.5 equiv) which was added dropwise over 56 min. The reaction was stirred at 0° C. for 17.5 h, diluted with MTBE (1200 mL), stirred at 0° C. for 1 h and filtered over a Nutsche filter twice. The filtrate was concentrated to 100 mL, diluted with MTBE to a total volume of 600 mL and filtered over a plug of silica (20 g). The resulting clear filtrate (650 mL) was cooled to 20° C. The solution was cooled gradually to −5° C., stirred for 2 h at this temperature and filtered over a Nutsche filter. The solid was dried at 40° C. under vacuum to afford 38.7 g II-0 (100.7 mmol, 84%, dr=49.8:50.2 as determined by 31P NMR in DMSO-d6:5.3 ppm (Rp-diastereomer), 4.3 (Sp-diastereomer)).
In a three-neck round bottom flask equipped with nitrogen bubbler, N-hydroxysuccinimide phosphoramidate II-0, prepared according to Example 2.1 (10 g, 25.7 mmol, 1.2 equiv, dr=50:50 (Sp:Rp)) was dissolved in THF (125 mL). To this solution were added 4 A mol. sieves (6.7 g), 2′-deoxy-2′-fluoro-2′C-methyluridine 1 (5.58 g, 21.4 mmol, 1 equiv), ZnBr2 (4.82 g, 21.4 mmol, 1 equiv) and triethylamine (5.93 mL, 42.8 mmol, 2 equiv). The resulting thick suspension was stirred at 28° C. for 16.5 h. HPLC analysis with individual response factor correction indicated 2% of III, 96% of sofosbuvir (I) with dr=78:22 (Sp:Rp), and 1% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined). The reaction was filtered over a Nutsche filter, washing with THF (10 mL) and charged with 1M HCl (100 mL). This solution was distilled at 45° C./80 mbar until no more distillate was observed to obtain a 2-phase water/oil mixture. This mixture was charged with dichloromethane (95 mL) and the phases were separated. The dichloromethane phase was concentrated to an end mass of 68 g, and transferred to a jacketed reaction vessel with a mechanical stirrer, pre-warmed to 35° C. The solution gradually cooled to 20° C., seeded with crystals of sofosbuvir at this temperature and stirred for 17 h at 15° C., 1 h at 0° C. and 2 h at −10° C. The crystal suspension was filtered over a Nutsche filter washing with chilled dichloromethane (2×5 mL) and dried under vacuum at 40° C. The product I (sofosbuvir) was obtained as white crystals (HPLC purity 99%, dr=97:3, 5.17 g, 9.76 mmol, 46%). Of this product, 4.5 g were dissolved in THF (45 mL) and charged with 1M HCl (40 mL). This solution was distilled at 40° C./80 mbar until an end mass of 37.8 g. This 2-phase mixture was charged with dichloromethane (36 mL) and the phases were separated. The dichloromethane phase was concentrated to an end mass of 23 g, warmed to 35° C., whereby it crystallized spontaneously, and cooled to 0° C. over 2 h. The crystal suspension was stirred for 1 h at 0° C. and 15.5 h at −10° C. The crystal suspension was filtered over a Nutsche filter washing with chilled dichloromethane (2×1 mL) and dried under vacuum at 40° C. The product I (sofosbuvir) was obtained as white crystals (HPLC purity >99%, dr=99.4:0.6, 4.01 g, 89%).
In a two-neck round bottom flask equipped with nitrogen bubbler, N-hydroxysuccinimide phosphoramidate II-0, prepared according to Example 2.1 (468 mg, 1.2 mmol, 5 equiv, dr=50:50 (Sp:Rp)) was dissolved in THF (1.5 mL). To this solution were added 4 A mol. sieves (152 mg), 2′-deoxy-2′-fluoro-2′C-methyluridine III (63.3 mg, 0.24 mmol, 1 equiv) and ZnBr2 (59 mg, 0.26 mmol, 1.1 equiv). The suspension was cooled to 10° C. and Hünig's base (82 mL, 0.24 mmol, 1 equiv) was added. The reaction mixture was stirred at 10° C. for 24 h. HPLC analysis with individual response factor correction indicated complete consumption of III, 97% of sofosbuvir (I) with dr=88:12 (Sp:Rp), and 3% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
The following syntheses were carried out following the procedure of example 2.2 (entry 8 of the table) with the conditions varied as specified in Table 1 below.
The reactions were monitored via 1H NMR. The 1H NMR experiments showed that the dr of the phosphorylating agent II-0 remains constant at 50:50, while sofosbuvir is formed with a diastereoisomeric excess as indicated in the dr SOFOS column of above table 1. This indicates that the dynamic resolution of III is occurring.
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added N-hydroxysuccinimide phosphoramidate II-0 with dr=50:50 (Sp:Rp) (177 mg, 0.46 mmol, 1.2 equiv) prepared according to example 2.1 and DMF (2.88 mL) to obtain a clear solution. To this solution was added 4 Å molecular sieves (67 mg), 2′-deoxy-2′-fluoro-2′C-methyluridine III (100 mg, 0.38 mmol, 1 equiv), ZnBr2 (86 mg, 0.38 mmol, 1 equiv), and Et3N (106 mL, 0.77 mmol, 2 equiv). The mixture was stirred at room temperature for 18.5 hours. HPLC analysis with individual response factor correction indicated 60% of unreacted nucleoside III, 39% of sofosbuvir (I) with dr=79:21 (Sp:Rp), and 1% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 2′-deoxy-2′-fluoro-2′C-methyluridine III (100 mg, 0.38 mmol, 1 equiv) followed by a THF solution of chlorophosphate II (dr=1:1, 1.15 mmol, 3 equiv in 3.52 mL THF). The slightly turbid solution was cooled to 0° C., charged with NMI (196 mL, 2.46 mmol, 6.4 equiv) and stirred at 0° C. for 15 min and at room temperature for 2.5 h. HPLC analysis with individual response factor correction indicated 78% of III, 9% of sofosbuvir (I) with dr=41:59 (Sp:Rp), and 13% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 2′-deoxy-2′-fluoro-2′C-methyluridine III (100 mg, 0.384 mmol, 1 equiv) followed by a THF (4 mL). The suspension was heated until most of the material dissolved and cooled to room temperature. To this solution were added 4 Å molecular sieves (130 mg) followed by N-hydroxysuccinimide phosphoramidate II-0 (dr=1:1, 221 mg, 0.58 mmol, 1.5 equiv). To this suspension was added t-BuMgCl (1M in THF, 422 mL, 0.42 mmol, 1.1 equiv), and the reaction was stirred at room temperature. After 18 h, HPLC analysis with individual response factor correction indicated 32% of III, 36% of sofosbuvir (I) with dr=61:39 (Sp:Rp), and 33% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 2′-deoxy-2′-fluoro-2′C-methyluridine III (1 g, 3.84 mmol, 1 equiv) followed by a THF (5 mL). The suspension was heated until most of the material dissolved and cooled to room temperature. To this solution was added consecutively t-BuMgCl (1M in THF, 7.98 mL, 7.98 mmol, 1.5 equiv), ZnBr2 (898 mg, 3.99 mmol, 1.05 equiv) [caution: exotherm!] and a solution N-hydroxysuccinimide phosphoramidate II-0 (dr=1:1, 2.07 g, 5.39 mmol, 1.42 equiv) in THF (5 mL). The reaction was stirred at room temperature. After 18 h, HPLC analysis with individual response factor correction indicated 65% of III, 5% of sofosbuvir (I) with dr=47:53 (Sp:Rp), and 29% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
As shown in Comparative Example 2.1, the coupling of the chloro-phosphoramidate in the presence of the NMI, as taught in the art, leads to a compound (I) with a dr of 41:59. Compared to Comparative Example 1, Examples 1.1, 1.2 and 2.2 and 2.3 the dr ratio of the compound I is quite higher in favor of the valuable stereoisomer. It was very surprising that when using the phosphoramidate derivative according to the invention in combination with a base, in particular the Hünig base and trimethylamine and with a Lewis acid better dr can be obtained compared to the use of a chloro-phosphoramidate in the presence of NMI. The use of a higher excess of compound (II) relative to compound (III) further improve the diastereoselectivity of the process. Furthermore, as shown in Comparative Example 2.2 and 2.3, the use of non-nitrogenous base (t-BuMgCl) with or without a Lewis acid leads to much lower yield and diastereoselectivity for the valuable stereoisomer of I.
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 20 wt % THF solution of chlorophosphate II (dr=1:1, 874 mg, 0.58 mmol, 1.5 equiv), followed by 2′-deoxy-2′-fluoro-2′C-methyluridine III (100 mg, 0.38 mmol, 1 equiv) and THF (1.8 mL). To this solution was added ZnBr2 (86 mg, 0.38 mmol, 1 equiv) and the suspension was cooled to 0° C. Triethylamine (160 mL, 1.15 mmol, 3 equiv) was added and the mixture was stirred at 0° C. for 10 min and allowed to warm up to room temperature. After 18.5 h, HPLC analysis with individual response factor correction indicated 4% of III, 89% of sofosbuvir (I) with dr=89:11 (Sp:Rp), and 7% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 20 wt % THF solution of chlorophosphate II (dr=1:1, 874 mg, 0.58 mmol, 1.5 equiv), followed by 2′-deoxy-2′-fluoro-2′C-methyluridine III (100 mg, 0.38 mmol, 1 equiv) and MIBK (1.8 mL). To this solution was added ZnBr2 (86 mg, 0.38 mmol, 1 equiv) and the suspension was cooled to 0° C. Triethylamine (160 mL, 1.15 mmol, 3 equiv) was added and the mixture was stirred at 0° C. for 10 min and allowed to warm up to room temperature. After 2 h, HPLC analysis with individual response factor correction indicated 38% of III, 58% of sofosbuvir (I) with dr=91:9 (Sp:Rp), and 4% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined). After 18 h, HPLC analysis with individual response factor correction indicated 33% of III, 62% of sofosbuvir (I) with dr=90:10 (Sp:Rp), and 5% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 2′-deoxy-2′-fluoro-2′C-methyluridine III (100 mg, 0.38 mmol, 1 equiv) followed by a THF solution of chlorophosphate II (dr=1:1, 0.96 mmol, 2.5 equiv in 2.94 mL THF). The slightly turbid solution was cooled to 0° C., charged with triethylamine (160 microL, 1.15 mmol, 3 equiv) and stirred at 0° C. for 2.5 h and at room temperature for 14.5 h. HPLC analysis with individual response factor correction indicated complete conversion of III, 97% of sofosbuvir (I) with dr=69:31 (Sp:Rp), and 3% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 2′-deoxy-2′-fluoro-2′C-methyluridine III (100 mg, 0.38 mmol, 1 equiv) followed by a DCM solution of chlorophosphate II (dr=1:1, 0.96 mmol, 2.5 equiv in 2.94 mL DCM). The solution was charged with ZnBr2 (86 mg, 0.38 mmol, 1 equiv), cooled to 0° C. and charged with NMI (92 microL, 1.15 mmol, 3 equiv). The resulting suspension and stirred at 0° C. for 2.5 h and at room temperature for 14.5 h. HPLC analysis with individual response factor correction indicated 66% of III, 18% of sofosbuvir (I) with dr=31:69 (Sp:Rp), and 16% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
To a two-neck round bottom flask equipped with a reflux condenser and purged with nitrogen was added 2′-deoxy-2′-fluoro-2′C-methyluridine 1 (100 mg, 0.38 mmol, 1 equiv) followed by a THF (4 mL). The suspension was heated until clear and cooled to room temperature. To this solution were added 4 Å molecular sieves (130 mg) and a 20 wt % solution of chlorophosphate 5 (dr=1:1, 874 mg, 0.58 mmol, 1.5 equiv). To this suspension was added t-BuMgCl (1M in THF, 422 mL, 0.42 mmol, 1.1 equiv), and the reaction was stirred at room temperature. After 17.5 h, HPLC analysis with individual response factor correction indicated 28% of 1, 13% of sofosbuvir (3) with dr=50:50 (Sp:Rp), and 59% of 3′,5′-bis-phosphoramidate impurity 4 (dr not determined).
Example 4 where a hydrogen chloride binding base which is not NMI and which is, in particular, trimethylamine, shows a very good result, illustrated by the dr of 69:31. If in addition to NMI a Lewis acid is employed (see Comparative Example 2.1), the result is even worse than when using NMI alone, illustrated by the dr of 31:69. Therefore, it was very surprising that when using a hydrogen chloride binding base which is not NMI and which is, in particular, trimethylamine, in combination with a Lewis acid (see Example 3.1 to 3.2), an even better dr can be obtained (80:20) compared to the use a hydrogen chloride binding base which is not NMI alone.
Number | Date | Country | Kind |
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15169168.0 | May 2015 | EP | regional |
16154143.8 | Feb 2016 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2016/061814 | 5/26/2016 | WO | 00 |