Patent Application
20220048917
The present disclosure provides highly efficient process for the preparation of enantiomerically enriched Sitagliptin. More particularly, a direct rhodium catalyzed asymmetric hydrogenation in the presence of bis-phosphine chiral ligand has been developed to yield enantiopure Sitagliptin product with the highest enantiomeric excess of 85-99.9%.
Beta amino acids and its derivatives have lot of medicinal significance. Beta amino acids are also present in peptides and different heterocycles. In beta amino acids, the amino group is linked to the beta carbon. Different free forms and derivatives of beta amino acid exhibit interesting pharmacological effects. Many methods of syntheses and transformations have been explored to obtain enantiomerically pure product of beta amino acid derivative. Still it is a challenge in organic synthesis to develop a process for the preparation of beta amino acids with high enantiomeric excess, when different functional groups are bonded to the beta carbon in order to maintain the chirality.
Many API's exhibiting antibiotic, antifungal, cytotoxic, and other pharmacological properties comprise the product of the present disclosure, a chiral beta-amino acid derivatives. They are therefore frequently used chiral building blocks in organic synthesis.
Another important application is the substitution of unnatural alpha- and beta-amino acids in biologically active peptides, which greatly enhance the understanding of enzyme mechanisms, protein conformations and properties related to molecular recognition, and for obtaining peptides with increased potency and enzymatic stability.
More preferably, here the beta amino acid compound is Sitagliptin Formula Ia. Sitagliptin is chemically known as (R)-4-oxo-4-[3-(trifluoromethyl)-5,6-dihydro[1,2,4]triazolo-[4,3-a]pyrazin-7(8H)-yl]-1-(2,4,5-trifluorophenyl)butan-2-amine and marketed as a phosphate salt under trade name JANUVIA by Merck.
Sitagliptin is used possibly with other medications to control high blood sugar. It is used in people with type 2 diabetes. Controlling high blood sugar helps prevent kidney damage, blindness, nerve problems, loss of limbs, and sexual function problems. Proper control of diabetes may also lessen your risk of a heart attack or stroke. Sitagliptin is a diabetes drug that works by increasing levels of natural substances called incretins. Incretins help to control blood sugar by increasing insulin release, especially after a meal. It also decreases the amount of sugar in liver.
J. Org. Process Res. Dev. 2005, 9, 634-639 describes lengthy multi step reaction process giving only 52% yield of sitagliptin. However, in this transformation selective separation of (E/Z) isomers was problematic as well as overall approach was multi-step.
J. Am. Chem. Soc. 2009, 131(32): p. 11316-11317 reports direct asymmetric reductive amination to sitagliptin with 96% yield and 99.5% enantiomeric excess, which is achieved by using Ruthenium metal and (R)-dm-segphos as ligand in presence of acidic additives like acetic acid, benzoic acid, salicylic acid, chloroacetic acid etc.
PCT application WO2005097733 describes the process for the preparation of beta amino acid derivatives including sitagliptin using Ru catalyst in the presence of chiral mono- or bis-phosphene ligands. But this application specifically does not include ferrocenyl bisphosphene ligands with Ru catalyst for asymmetric hydrogenation, in its description.
Sitagliptin is an important active ingredient for diabetic patients. Therefore, highly enantioselective, low cost synthesis of this API is always in need. The present disclosure provides such atom economic single step protocol like asymmetric hydrogenation which provides an unprecedented enantiomeric excess of 90% and above. It reduces the cost of the process also by generating the desired active catalyst in-situ, circumventing the need of separate synthesis and isolation of active catalyst.
Main objectives of the present disclosure are to provide a highly efficient process for the preparation of enantiomerically enriched Sitagliptin.
Another objective of the present disclosure is to provide a direct rhodium catalyzed asymmetric hydrogenation in the presence of bis-phosphine chiral ligand to yield enantiopure Sitagliptin product with the highest enantiomeric excess of 85-99.9%.
An another objective of the present disclosure is to provide process for the preparation of beta amino acid derivatives of Formula (I), more preferably Sitagliptin of Formula (Ia), via highly enantioselective asymmetric hydrogenation with in-situ generated catalyst by using Rh-catalyst in the presence of ferrocenyl bisphosphene ligands, which provides enantiopure Sitagliptin of Formula (Ia) with the highest enantiomeric excess of 85-99.9%.
Accordingly, the present disclosure relates to a process for the preparation of sitagliptin, compound of Formula (Ia) by enantioselective asymmetric hydrogenation of dehydrositagliptin of Formula (IIa) employing rhodium catalyst on bisphosphine ferrocenyl ligands of Formula L, to obtain enantiomeric excess in the range of 85-99.9%;
In an embodiment, as described herein, the rhodium catalyst is [Rh(COD)2OTf].
In another embodiment, as described herein, the additive is selected from the group consisting of salicylic acid, acetic acid, ammonium chloride, phosphoric acid, ammonium salicylate, tetramethyl ammonium iodide, tetraethyl ammonium iodide, tetra butyl ammonium bromide, butyl phosphoric acid, dibutyl phosphate, tributyl phosphate.
In yet another embodiment, the solvent selected from the group consisting of methanol, dichloromethane, tetrahydrofuran, trifluoroethanol, toluene, 1,4-dioxane and ethyl acetate.
In another embodiment, the preparation of beta amino acid derivatives of Formula (I), more preferably Sitagliptin of Formula (Ia), with the highest enantiomeric excess of 85-99.9%,
The process, as described herein, relates to a highly enantioselective rhodium metal catalyzed asymmetric hydrogenation of a prochiral enamine of compound of structural Formula II in the presence of bisphosphine ferrocenyl ligand of Formula L to provide chiral beta amino acid derivatives of structural Formula I, more preferably compound of Formula Ia.
In still another embodiment, the bisphosphine ferrocenyl ligand of Formula L is selected from the group of ligands L1-L8;
In yet another embodiment, the present embodiment provides general process for the preparation of Sitagliptin, compound of Formula Ia. Asymmetric hydrogenation of dehydrositagliptin to sitagliptin of Formula Ia is shown below in synthetic scheme 1.
It is to be understood that the figures, schemes and descriptions of the present disclosure have been simplified to illustrate elements that are relevant for a clear understanding of the disclosure. The detailed description will be provided herein below with reference to the attached drawings, and schemes.
In view of the above, the present disclosure provides a process for the preparation of beta amino acid derivatives of Formula (I), more preferably Sitagliptin of Formula (Ia), with the highest enantiomeric excess of 85-99.9%,
The process, as described herein, relates to a highly enantioselective rhodium metal catalyzed asymmetric hydrogenation of a prochiral enamine of compound of structural Formula II in the presence of bisphosphine ferrocenyl ligand of Formula L to provide chiral beta amino acid derivatives of structural Formula I, more preferably compound of Formula Ia.
The general process to afford compound of Formula (I) comprises of following steps;
More particularly, the present embodiment provides above general process for the preparation of Sitagliptin, compound of Formula Ia. Asymmetric hydrogenation of dehydrositagliptin to sitagliptin of Formula Ia is shown below in synthetic scheme-1.
The bisphosphine ferrocenyl ligand of Formula L is selected from the group of ligands L1-L8 represented below;
In an aspect of the present embodiment involves a an additives at step (i) of the process, which may be selected from the group comprising of Salicylic acid, Acetic acid, Ammonium chloride, Phosphoric acid, Ammonium salicylate, Tetra methyl ammonium iodide, Tetraethyl ammonium iodide, Tetra butyl ammonium bromide, Butyl phosphoric acid, Dibutyl phosphate, Tributyl phosphate.
Another aspect of the present embodiment involves a suitable solvent at step (ii) of the process, suitable solvents may include alcohol solvents. Alcohol solvents, which may include methanol, ethanol, isopropanol, or mixtures thereof. In particularly useful embodiments, methanol is used as a solvent at step (ii).
Suitable temperature for stirring the reaction mass at step (ii) may be 20° C.-40° C., more preferably 25° C.-35° C.
Suitable temperature for maintaining the reaction mixture at step (iii) may be 35° C.-95° C., preferably 60° C.-80° C., more preferably 70°−80° C.
Suitable hydrogen pressure for maintaining reaction mixture at step (iii) may be 20 bar-40 bar, more preferably 30 bar.
Asymmetric hydrogenation of dehydrositagliptin is carried out using bis-phosphine ligands of Formulas L1 to L8, as shown above, with Rh precursor [Rh(COD)2OTf]. Several experiments have been conducted by using different reaction parameters and ligands L1 to L8. Results of these experiments are summarized in Table 1.
aConditions: Substrate (dehydrositagliptin) 85.11 mg; [Rh(COD)2OTf]: 1 mg (1 mol %); Ligand/Rh: 1.1; Additive/Rh: 1; Solvent: 2 ml; conversion and enantiomeric excess is determined by chiral HPLC.
All manipulations were carried out under an inert atmosphere of argon using standard Schlenk line techniques or m-Braun glove box. Solvents were dried by standard procedures unless otherwise mentioned. Ferrocene bis-phosphine ligands and [Rh(COD)2OTf] were purchased from Sigma-Aldrich. While 1,1′-Bis(2,5-di-isopropylphospholano)ferrocene was purchased from Stream chemicals. Hydrogen gas (H2) was supplied by Ms. Vadilal Chemicals Ltd., Pune, India. All other reagents/chemicals, solvents were purchased from local suppliers (Spectrochem Pvt. Ltd.; Avra Synthesis Pvt. Ltd.; Thomas Baker Pvt. Ltd. etc). Asymmetric hydrogenation was performed in Amar Equipment Pvt. Ltd. high-pressure reactor equipped with pressure regulators and safety rupture valve.
Solution NMR spectra were recorded on a Bruker Advance 200, 400 and 500 MHz instruments at 298 K unless mentioned otherwise. Chemical shifts are referenced to external reference TMS (1H). Coupling constants are given as absolute values. Multiplicities are given as follows s: singlet, d: doublet, t: triplet, m: multiplet. The enantiomeric excess and conversion to sitagliptin was determined by chiral HPLC on an Agilent Technologies 1260 Infinity instrument with Chiralpak IC column (250 mm×4.6 mm×5 μm).
The following high performance liquid chromatographic (HPLC) conditions were used to determine percent conversion to product & optical purity of the sitagliptin product:
The following examples, which include preferred embodiments, will serve to illustrate the practice of this disclosure, it being understood that the particulars shown are by way of example and for purpose of illustrative discussion of preferred embodiments as described herein.
In a 5 mL reaction vial equipped with septa and inlet needle, dehydrositagliptin (100 eq. 85.11 mg), [Rh(COD)2OTf] (1 eq. 1 mg), ligand L (1.05 eq.) and additive (1 eq.) were added in the glove box. Reaction vial was then transferred in a large Schlenk type container and was then taken out from the glove box. 2 mL dry methanol was added to the vial in inert atmosphere and the resultant reaction slurry was stirred for 1 hour at 25° C. After that, the reaction vial was kept in an autoclave and the autoclave was purged three times by using hydrogen gas pressure (40 bars). Finally, the autoclave was pressurized to 30 bar of hydrogen pressure and the hydrogenation was continued at 50-70° C. for 18 hrs. Then autoclave was cooled to 25° C., excess pressure was released and the autoclave was opened. The vials were taken out from autoclave reactor. The thus obtained reaction mixture was passed through neutral alumina bed, the filtrate was collect and dried to yield residue. The resultant residue was then analyzed by HPLC or NMR spectroscopy. 1H NMR (400 MHz CDCl3) δ=7.10 (m, 1H), 6.89 (m, 1H), 4.89 (s, 2H), 4.21 (t, 2H) 4.06 (t, 2H), 3.36 (t, 1H), 3.25 (t, 1H), 2.79 (s, 1H), 2.32 (t, 1H), 2.00 (t, 1H).
HPLC: (Ref:
In a 5 ml reaction vial equipped with septa and inlet needle, dehydrositagliptin (100 eq. 85.11 mg), [Rh(COD)2OTf] (1 eq. 1 mg), ligand L3 (1.05 eq.) and additive (1 eq.) were added in the glove box. Reaction vial was then kept in a large Schlenk type container and was then taken out from the glove box. 2 mL dry methanol was added to the vial in inert atmosphere and the resultant reaction slurry was stirred for 1 hour at 25° C. After that, the reaction vial was kept in an autoclave and the autoclave was purged three times by using hydrogen gas pressure (40 bars). Finally, the autoclave was pressurized to 30 bar hydrogen pressure and the hydrogenation was continued at 70° C. for 18 hrs period. After 18 hrs, the autoclave was cooled to 25° C., excess pressure was released and the autoclave was opened. The vials were taken out from autoclave reactor. The thus obtained reaction mixture was passed through neutral alumina bed, the filtrate was collect and dried to yield residue. The resultant residue was then analyzed by HPLC or NMR spectroscopy.
In a 5 ml reaction vial equipped with septa and inlet needle, dehydrositagliptin (100 mol %, 85.11 mg), [Rh(COD)2OTf] (1 mol %), ligand L7 (1.1 mol %.) and additive (150 mol %) were added in the glove box. Reaction vial was then kept in a large Schlenk type container and was then taken out from the glove box. 2 ml dry methanol was added to the vial in inert atmosphere and the resultant reaction slurry was stirred for 1 hour at 25° C. After that reaction vial was kept in an autoclave and the autoclave was purged three times by using hydrogen gas pressure (40 bars). Finally, the autoclave was pressurized to 30 bar hydrogen pressure and the hydrogenation was continued at 50° C. for 18 hrs period. After 18 hrs, the autoclave was cooled to 25° C., excess pressure was released and the autoclave was opened. The vials were taken out from autoclave reactor. The thus obtained reaction mixture was passed through neutral alumina bed, the filtrate was collect and dried to yield residue. The resultant residue was then analyzed by HPLC or NMR spectroscopy.
| Number | Date | Country | Kind |
|---|---|---|---|
| 201811046767 | Dec 2018 | IN | national |
This application is a national-stage application under 35 U.S.C. § 371 of International Application No. PCT/IN2019/050896, filed Dec. 9, 2019, which International Application claims benefit of priority to Indian Application No. 201811046767, filed Dec. 11, 2018.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IN2019/050896 | 12/9/2019 | WO | 00 |
