EP3110795A1 - Neuartiges ökonomisches verfahren für vildagliptin - Google Patents

Neuartiges ökonomisches verfahren für vildagliptin

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Publication number
EP3110795A1
EP3110795A1 EP15754784.5A EP15754784A EP3110795A1 EP 3110795 A1 EP3110795 A1 EP 3110795A1 EP 15754784 A EP15754784 A EP 15754784A EP 3110795 A1 EP3110795 A1 EP 3110795A1
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EP
European Patent Office
Prior art keywords
formula
compound
acid
group
process according
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP15754784.5A
Other languages
English (en)
French (fr)
Other versions
EP3110795A4 (de
Inventor
Swapnil Surendra Mohile
Sandeep Rameshrao TAPKIR
Manoj Vinayak PATIL
Ashok Kumar Gangopadhyay
Peter David Nightingale
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hikal Ltd
Original Assignee
Hikal Ltd
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Filing date
Publication date
Application filed by Hikal Ltd filed Critical Hikal Ltd
Publication of EP3110795A1 publication Critical patent/EP3110795A1/de
Publication of EP3110795A4 publication Critical patent/EP3110795A4/de
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D207/00Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom
    • C07D207/02Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom
    • C07D207/04Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members
    • C07D207/10Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D207/16Carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/26Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing carboxyl groups by reaction with HCN, or a salt thereof, and amines, or from aminonitriles
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C229/00Compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C229/02Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton
    • C07C229/04Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being acyclic and saturated
    • C07C229/06Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being acyclic and saturated having only one amino and one carboxyl group bound to the carbon skeleton
    • C07C229/10Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being acyclic and saturated having only one amino and one carboxyl group bound to the carbon skeleton the nitrogen atom of the amino group being further bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings
    • C07C229/14Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being acyclic and saturated having only one amino and one carboxyl group bound to the carbon skeleton the nitrogen atom of the amino group being further bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings to carbon atoms of carbon skeletons containing rings
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • C07C253/30Preparation of carboxylic acid nitriles by reactions not involving the formation of cyano groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C255/00Carboxylic acid nitriles
    • C07C255/01Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms
    • C07C255/24Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms containing cyano groups and singly-bound nitrogen atoms, not being further bound to other hetero atoms, bound to the same saturated acyclic carbon skeleton
    • C07C255/25Aminoacetonitriles
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2603/00Systems containing at least three condensed rings
    • C07C2603/56Ring systems containing bridged rings
    • C07C2603/58Ring systems containing bridged rings containing three rings
    • C07C2603/70Ring systems containing bridged rings containing three rings containing only six-membered rings
    • C07C2603/74Adamantanes

Definitions

  • the present invention relates to a commercially viable novel process for manufacturing Vildagliptin in high yield with hi h chemical and chiral purity.
  • Vildagliptin is chemically known as l-[ ⁇ (3-hydroxy-l-adamantyl)amino ⁇ acetyl]-2-cyano(s)- pyrrolidine, which is a dipeptidylpeptidase IV (DPP-IV) inhibitor and found usefulness in the treatment of diabetes mellitus.
  • DPP-IV dipeptidylpeptidase IV
  • PCT Patent Publication WO 01/96295A2 the method described involve chloroacetylation in THF followed by dehydration with TFAA.
  • PCT Patent Publication WO 2006/10.0181 a process for the synthesis of l-(haloacetyl)-2- cyano pyrroloine is described wherein the proline amide was coupled with chloroacetyl chloride followed by dehydration of amide using Vilsmeier reagent and its variants e.g., POCl 3 -DMF, SOCl 2 -DMF, cyanuric chloride-DMF etc).
  • the main object of the present invention is to provide an improved process for the preparation of a compound of formula (I), which is simple, economical, user- friendly and commercially viable.
  • Another objective of the present invention is to provide a process for the preparation of a compound of formula (I), which would be easy to implement on commercial scale, and to avoid excessive use of reagent(s) and organic solvent(s), which makes the present invention eco-friendly as well.
  • Yet another objective of the present invention is to provide a process for the preparation of a compound of formula (I) in a greater yield with higher chemical purity.
  • Still another objective of the present invention is to provide a process for the preparation of a compound of formula (I), wherein the byproduct formed during the reaction can be reusable and thereby recyclable, which makes the process industrially more suitable.
  • the present invention provides an improved process for the preparation of Vildagliptin of formula (I),
  • R 2 is H using a suitable dehydrating agent in a suitable solvent
  • the substituent Ri is considered to constitute C[-C 3 linear, cyclic or branched chain or C7-C 1 0 alkyl aryl group;
  • R 2 is defined as H, C 2 -C 6 alkyl group containing a double bond optionally substituted with halogen (such as CI, Br, I etc), S, O, Si etc. or a group containing C 7 -C 1 0 alkyl aryl optionally substituted by atoms selected from N, O, S, halogen Si etc.
  • R 3 is defined as CpC 6 alkyl group optionally substituted with one or more atoms selected from among halogen (such as F, CI etc), S, O, Si or a group containing C 7 -C 15 alkyl aryl (monocyclic or polycyclic) both the types are optionally substituted by one or more atom(s) selected from N, O, S, halogen Si etc.
  • halogen such as F, CI etc
  • R4 is chosen from C 6 -C] 0 aryl or heteroaryl group optionally substituted with F, CI, N0 2 and the like;
  • X is halogen (CI, Br, I), CH 3 S0 2 , PhS0 2 , 4-Me- PhS0 2 and the like.
  • the present invention provides an improved process for the preparation of Vildagliptin of formula (I) via novel synthetic approach.
  • step (a) step (c) and step (f) are preferably selected from the group consisting of ethyl acetate, isopropyl acetate, dichloro methane, chloroform, tetrahydrofuran, 2-methyl tetrahydrofuran, acetonitrile, dioxane, dimethyl formamide, acetone and the like or the mixture thereof; more preferably dichloro methane or ethyl acetate or dimethyl formamide or acetone.
  • step (a), step (d), step (1) and step (m) are preferably selected from organic base or an inorganic base, which are selected from the group consisting of triethyl amine, diisopropylethyl amine, pyridine, potassium carbonate, sodium carbonate, sodium bicarbonate, potassium bicarbonate, alkali or alkaline earth metal hydroxides such as sodium hydroxide, potassium hydroxide, more preferably is potassium carbonate or sodium carbonate or triethyl amine.
  • the said catalyst in step (a) and step (m) is a phase transfer catalyst and or alkali metal iodides such as sodium iodide or potassium iodide and the like to accelerate the said reaction.
  • step (a) is carried out preferably at ambient temperature to reflux temperature, more preferably at reflux temperature, whilest most preferably at 40 °C to 80°C.
  • step (b) wherein the solvent used in step (b) are preferably selected from the group consisting of water, methanol, ethanol, isopropyl alcohol, n-butyl alcohol or a mixture thereof, more preferably water or methanol or a mixture thereof.
  • the said reaction of step (b) are carried out preferably at ambient temperature to 120°C, more preferably at 45°C to 1 10°C, most preferably at reflux temperature of the solvent.
  • step (b) are preferably selected from hydrochloric acid, sulfuric acid, nitric acid and the like, more preferably is hydrochloric acid.
  • the said base in step (b) are preferably selected from alkali or alkaline earth metal hydroxides selected from lithium hydroxide, sodium hydroxide, potassium hydroxide, calcium hydroxide, magnesium hydroxide, barium hydroxide, C C 5 quaternary ammonium hydroxide and the like, more preferably is sodium hydroxide.
  • the reagent for N protection in step (d) are preferably selected from the group consisting of methyl chloroformate, ethyl chloroformate, isobutyl chloroformate, carbobenzoxy chloride, di-t-butyl dicarbonate, 2,2,2- trifluoroethyl chloroformate, aryl sulfonyl chloride and the like, more preferably di-t-butyl dicarbonate under the standard reaction condition known for those skilled in the art.
  • the solvent used in step (d) are preferably selected from the group consisting of water, methanol, ethanol, isopropyl alcohol, dichloro methane, acetonitrile, tetrahydrofuran, 2-methyl tetrahydrofuran, dioxane or a mixture thereof, more preferably water or methanol or dichloro methane or isopropyl alcohol or a mixture thereof.
  • step (c) and step (f) can be selected from the prior knowledge which is well understood by those skilled in the organic synthesis. More preferably in step (c) and step (f) is propylphosphonic anhydride is used.
  • step (c) and step (f) are carried out preferably at the temperature in the range between - 20°C to 100°C.
  • the said ammonia is either liquid ammonia or 10 to 50 % alcoholic solution of ammonia.
  • step (e) and step (g) are preferably selected from the alcoholic solvent and group consisting of methanol, ethanol, n-propanol, isopropyl alcohol, n-butanol and the like or a mixture thereof, more preferably methanol.
  • step (e) and step (g) are carried out preferably at the temperature in the range of ambient to 100°C.
  • step (h) and step (j) are preferably selected from the group consisting of phosphorus pentoxide, phosphoryl chloride, thionyl chloride, oxalyl chloride, cyanuric chloride, trifluoroacetic acid-N,N-dicyclohexylcarbodiimide, acetic anhydride, trifluoroacetic anhydride, polyphosphoric acid, propylphosphonic anhydride and the like optionally in combination with additives selected from the group consisting of pyridine, triethylamine, ⁇ , ⁇ -diisopropylethylamine, l,8-Diazabicyclo[5.4.0]undec-7-ene, 1,5-Diazabicyclo[4.3.0] non-5-ene, l,5-Diazabicyclo[4.3.0]non-5-ene imidazole, dimethyl sulfoxide, 4- dimethylamino
  • step (h), step (i) step (j), step (k) and step (1) are preferably selected from the group consisting of acetone, dichloro methane, chloroform, esters, tetrahydrofuran, 2-methyl tetrahydrofuran, dimethyl formamide, methyl isobutyl ketone, acetone, acetonitrile, toluene, cyclohexane, tert butyl methyl ether, 1 ,4-dioxane, dimethyl sulfoxide and the like or combination thereof, more preferably selected from the group consisting of dichloro methane, tetrahydrofuran, 2-methyl tetrahydrofuran or combination thereof.
  • step (h) and step (j) are carried out preferably at 0°C to 100°C, more preferably at ambient to 50°C.
  • the said dehydrating agent used in step (i) is preferably selected from the group consisting of phosphorus pentoxide, phosphoryl chloride, oxalyl chloride, cyanuric chloride, trifluoroacetic acid-N,N- dicyclohexylcarbodiimide, acetic anhydride, trifluoroacetic anhydride, polyphosphoric acid, propylphosphonic anhydride and the like optionally in combination with additives selected from pyridine, triethylamine, ⁇ , ⁇ -diisopropylethylamine, l,8-Diazabicyclo[5.4.0]undec-7- ene, l,5-Diazabicyclo[4.3.0]non-5-ene, l,5-Diazabicyclo[4.3.0]non-5-ene imidazole, pyridine, sodium acetate, potassium acetate, sodium formate, more preferably the preferred dehydrating rea
  • step (i) is carried out preferably at 0°C to 100°C, more preferably at ambient to 60°C.
  • the said reagent used in step (k) and (1) are preferably selected in suitable molar ratios from the group consisting of hydrochloric acid, hydrobromic acid, boron tribromide, formic acid, acetic acid, para toluene sulfonic acid, trifluoro acetic acid, trifluoromethan sulfonic acid, piperidine, pyridine, thioanisole, zinc, zinc chloride, alumunium chloride nBu 4 N + F ⁇ , N-bromosuccinimide, N-chlorosuccinimide, hydrogen/nickel, hydrogen / palladium on carbon, Rhodium on carbon, hydrogen/palladium- barium sulfate, hydrogen/palladium-calcium carbonate and the like or in suitable, combination thereof.
  • the solvent used in step (m) is preferably selected from the group consisting of water, alcohols, acetone, ethyl acetate, isopropyl acetate, dichloro methane, chloroform, tetrahydrofuran, 2-methyl tetrahydrofuran, acetonitrile, dioxane, dimethyl formamide, toluene, cyclohexane, cyclohexane, chlorobenzene, dichlorobenzene and the like or combination thereof, more preferably selected from the group consisting of dichloro methane, tetrahydrofuran, 2 -methyl tetrahydrofuran or combination thereof, more preferably dichloro methane, toluene or ethyl acetate.
  • step (m) is carried out preferably at ambient temperature to 100°C or reflux temperature, more preferably at ambient to 80°C.
  • present inventor have surprisingly found an impurity of a compound of formula (16), wherein the definition of Ri is defined earlier. Moreover the removal process of the said impurity is also suggested by the present invention.
  • the said impurity is characterized by the known methods in the prior art.
  • the acid used is selected from the group consisting of acetic acid, formic acid, citric acid, tartaric acid, para toluene sulfonic acid, methanesulfonic acid and the like, more preferably acetic acid.
  • step (n) is carried out by procedure described for step (d).
  • step (o) is carried out by procedure described for step (1).
  • TP In a clean and dry 5.0 L 4 necks RBF equipped with liquid addition funnel, TP. Charged cone, sulphuric acid (300 mL, 2 V) and cooled the reaction mass to 5-10 °C. To the cooled mass 1-adamantyl amine (150 g, 1 eq.) was added lot wise at 5-10 °C. After complete addition, stirred the reaction mass to get clear (slightly hazy) solution and maintained the reaction mass at 5-15 °C. Meanwhile a nitrating mixture was prepared by adding 150 mL of 65-70 % nitric acid to 450 mL cone, sulphuric acid maintaining temperature at 0-10 °C).
  • the nitrating mixture was added to the reaction mass maintaining reaction temperature at 20 ⁇ 5 °C. After the addition was over, stirred the reaction mass at 20 ⁇ 5°C for 3 to 5 h. Completion of the reaction was confirmed by GC.
  • the reaction mass was cooled to 0 - 5 °C and added water (150 mL, I V) to the reaction mass maintaining 0-20 °C and again cooled reaction mass to 5-10 °C. Second lot of water (300 mL, 2 V) was added to the reaction mass maintaining 5-20 °C. The reaction mass was cooled again to 5-10 °C and added third lot of water (1050 mL, 7 V) to the reaction mass maintaining 5-20 °C.
  • reaction mass Cooled reaction mass to 35-40°C under N 2 and applied vacuum slowly. Methanol was distilled completely under reduced pressure. After complete removal of methanol, heated reaction mass (stirable thick oil) at 45 °C under reduced pressure for 30 min. Charged above crude product into 2 L RBF and rinsed with water (700 mL, 7 V) and stirred to dissolve. The reaction mass was cooled to 10-15°C and potassium bicarbonate (260.50 g, 3.0 eq.) was added carefully. After complete addition of potassium bicarbonate, stirred reaction mass for 5-10 min. Charged chloroacetyl chloride (103.6 mL, 1.50 eq.) slowly maintaining below 10°C.
  • acetic acid (30.2 mL, 3.1 eq.) in water (175 mL, 5 V) was added to above reaction mass. The reaction mass was stirred for 30 min. at 20-25°C. The organic layer and aq. Layer were separated. The organic layer was kept aside. The aqueous layer was extracted with dichloromethane (70 mL x 4, 2V x 4). [Collectively organic layers were concentrated to get a compound of formula (16) wherein the Rl is specifically methyl]. After dichloromethane wash, adjusted the pH of aqueous layer using aq. ammonia (3V). The aqueous layer was extracted with dichloromethane (70 mL ⁇ 4, 2V ⁇ 4).
  • Example 12.2 (S)-l-[2-(3-Hydroxy-adamantan-l-ylamino)-acetyl]-pyrrolidine-2- carboxylic acid amide.
  • Examplel4 [2-((S)-2-Carbamoyl-pyrrolidine-l-yl)-2-oxo-ethyI]-(3-hydroxy-damantan-l- yl)-carbamic acid tert butyl ester
  • the crude was further purified by crystallization by dissolving under reflux with ethyl acetate (255 mL, 6V w.r.t to crude wt.) and IPA (85 mL, 2V) and crude compound (42.4 g) under stirring It was allowed to cool to 20-25°C and then to 0-5°C and stirred for 1 h at 0-5°C. Filtered the solid formed and washed with chilled ethyl acetate (42.5 mL, 1 V).
  • the 2-Me THF layer was concentrated to isolate crude product.
  • aqueous citric acid solution citric acid - 98 g, 3.0 eq; water - 6V
  • DCM DCM extract obtained above
  • DCM-3 DCM extract obtained above
  • DCM DCM
  • the crude material (26.4 g) was dissolved by refluxing in ethyl acetate (158.4 mL, 6 V w.r.t to crude wt.) and IPA (52.8 mL, 2V) under stirring maintaining for 2 h. Cooled the reaction mass to 20-25°C and then to 0-5 °C and stirred for 1 h. Filtered the solid formed and wash with chilled ethyl acetate (26.4 mL, IV) dried the solid obtained for 3-4 h at 50°C in tray dryer. Unload the solid and weighed.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Pyrrole Compounds (AREA)
EP15754784.5A 2014-02-28 2015-02-24 Neuartiges ökonomisches verfahren für vildagliptin Withdrawn EP3110795A4 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IN708MU2014 2014-02-28
PCT/IB2015/000219 WO2015128718A1 (en) 2014-02-28 2015-02-24 Novel economic process for vildagliptin

Publications (2)

Publication Number Publication Date
EP3110795A1 true EP3110795A1 (de) 2017-01-04
EP3110795A4 EP3110795A4 (de) 2017-10-04

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EP15754784.5A Withdrawn EP3110795A4 (de) 2014-02-28 2015-02-24 Neuartiges ökonomisches verfahren für vildagliptin

Country Status (5)

Country Link
EP (1) EP3110795A4 (de)
JP (1) JP2017507934A (de)
KR (1) KR20160127025A (de)
CN (1) CN106029635A (de)
WO (1) WO2015128718A1 (de)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106432026A (zh) * 2016-09-12 2017-02-22 重庆医科大学 一类对糖尿病具有潜在治疗活性的化合物
CN107033054A (zh) * 2017-06-19 2017-08-11 河北富格药业有限公司 一种维格列汀的合成方法
CN107325010A (zh) * 2017-08-14 2017-11-07 四川众邦制药有限公司 一种金刚烷醇的安全制备方法及装置
WO2021116897A1 (en) * 2019-12-10 2021-06-17 Optimus Drugs (P) Ltd Process for the preparation of vildagliptin
WO2022003405A1 (en) 2020-07-03 2022-01-06 Savoi Guilherme One-pot process to obtain a pyrrolidine-2-carbonitrile intermediate compound and industrial scale telescopic process to prepare (2s)-1-[n-(3-hydroxyadamantan-1-yl)glycyl]-2-pyrrolidinecarbonitrile (vildagliptin) using same
CN112279809A (zh) * 2020-09-23 2021-01-29 山东省海洋化工科学研究院 一种2-氰基-4-氟吡啶的制备方法
CN112939837B (zh) * 2021-02-03 2022-07-19 海南通用三洋药业有限公司 一种多相复式连续生产制备维格列汀的方法
CN115108939A (zh) * 2021-03-17 2022-09-27 成都施贝康生物医药科技有限公司 反式-4-[(2-氨基-3,5-二溴苄基)氨基]-金刚烷-1-醇的中间体及制法

Family Cites Families (10)

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Publication number Priority date Publication date Assignee Title
AU2002360732A1 (en) * 2001-12-26 2003-07-24 Guilford Pharmaceuticals Change inhibitors of dipeptidyl peptidase iv
UA96283C2 (uk) * 2005-12-23 2011-10-25 Зіланд Фарма А/С Модифіковані міметики лізину
AR064833A1 (es) * 2007-01-10 2009-04-29 Medichem Sa Un procedimiento para la preparacion de vildagliptin
GB2445746A (en) * 2007-01-17 2008-07-23 Texcontor Ets Use of carbonated water as a solvent for freeze drying, and method of purification comprising dissolution of material in carbonated water and freeze drying
EP2145873A1 (de) * 2008-06-17 2010-01-20 Commissariat A L'energie Atomique Neue Verbindungen, die eine Schutzaktivität gegen die Wirkung von Toxinen und Viren über einen intrazellulären Wirkungsmechanismus entfalten
WO2011101861A1 (en) * 2010-01-29 2011-08-25 Msn Laboratories Limited Process for preparation of dpp-iv inhibitors
IT1400714B1 (it) * 2010-07-06 2013-06-28 Chemelectiva S R L Processo ed intermedi per la preparazione di un principio attivo.
ITMI20112224A1 (it) * 2011-12-06 2013-06-07 Chemelectiva S R L Nuovo processo ed intermedi per la sintesi di vildagliptin
CN103980175B (zh) * 2013-02-07 2016-06-01 山东威智医药工业有限公司 制备维达列汀的方法
CN103450083B (zh) * 2013-09-13 2015-12-23 杭州华东医药集团新药研究院有限公司 格尔德霉素衍生物及其制备方法和用途

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Publication number Publication date
JP2017507934A (ja) 2017-03-23
EP3110795A4 (de) 2017-10-04
KR20160127025A (ko) 2016-11-02
CN106029635A (zh) 2016-10-12
WO2015128718A1 (en) 2015-09-03

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