WO2019008594A1 - Procédé continu pour la préparation de 2-(1h-imidazol-4-yl) éthanamine et de ses sels pharmaceutiquement acceptables - Google Patents

Procédé continu pour la préparation de 2-(1h-imidazol-4-yl) éthanamine et de ses sels pharmaceutiquement acceptables Download PDF

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Publication number
WO2019008594A1
WO2019008594A1 PCT/IN2017/050610 IN2017050610W WO2019008594A1 WO 2019008594 A1 WO2019008594 A1 WO 2019008594A1 IN 2017050610 W IN2017050610 W IN 2017050610W WO 2019008594 A1 WO2019008594 A1 WO 2019008594A1
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WO
WIPO (PCT)
Prior art keywords
histamine
process according
pharmaceutically acceptable
acceptable salts
preparation
Prior art date
Application number
PCT/IN2017/050610
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English (en)
Inventor
Sanjeev Kumar
Rajesh Kumar
Brijesh Kumar Shukla
Rajendra Singh SHEKHAWAT
Sujay Biswas
Dharam Vir
Original Assignee
Jubilant Generics Limited
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jubilant Generics Limited filed Critical Jubilant Generics Limited
Publication of WO2019008594A1 publication Critical patent/WO2019008594A1/fr

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D233/00Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings
    • C07D233/54Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings having two double bonds between ring members or between ring members and non-ring members
    • C07D233/64Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings having two double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms, e.g. histidine

Definitions

  • the present invention discloses a commercially viable, cost effective and energy efficient process for the preparation of 2-(lH-Imidazol-4-yl) ethanamine or pharmaceutically acceptable salts thereof in high purity and yield via application of continuous flow technology.
  • 2-(lH-Imidazol-4-yl) ethanamine represented as compound of formula I, possesses significant biological activity and is used as standard in biological assays and as a component in certain allergy diagnostic kits. Histamine occurs widely in nature, but to take full advantage of its therapeutic properties, it is important to obtain large quantities of histamine of pharmaceutical grade by synthetic routes.
  • Histamine in therapeutic applications is used as its dihydrochloride salt, which can be conveniently synthesized by decarboxylation of histidine. Using this synthetic process, histidine is decarboxylated and subsequently treated to form the dihydrochloride salt form of the molecule.
  • Hashimoto et al in Chemistry Letters, 1986, 883-896 discussed the preparation of histamine, wherein histidine is decarboxylated using cyclohexanone as a catalyst in cyclohexanol solvent.
  • the process disclosed involves the decarboxylation reaction being carried out in 26 hours and used toluene and HC1 gas for the preparation of dihydrochloride salt.
  • the process disclosed is not industrially feasible as the reaction time is too long, which results in a lot of energy consumption and further the process fails in providing histamine dihydrochloride of pharmaceutical grade as it contains a number of impurities which makes the process unsuitable for large scale production.
  • JPH05255204 discloses use of acetophenone catalyst and diethylene glycol as solvent for the decarboxylation of histidine to histamine.
  • the said process is also reported to be inconsistent in providing histamine dihydrochloride in desired purity and yield.
  • the process disclosed suffered the incompatibility in terms of removal of traces of diethylene glycol as histamine and its dihydrochloride salt are highly soluble in water and none of the isolation techniques worked efficiently to remove the diethylene glycol solvent from the product.
  • it is rendered inapplicable on industrial scale.
  • the principal object of the present invention is to provide an improved and efficient process for the preparation of histamine or pharmaceutically acceptable salts thereof which is simple, economic and alleviates one or more problems of the prior art disclosed processes.
  • the present invention provide a process for the preparation of histamine or pharmaceutically acceptable salts thereof, comprising
  • step (b) performing the decarboxylation reaction by feeding solution of step (a) to a continuous reactor to obtain histamine and optionally converting the histamine to its pharmaceutically acceptable salts.
  • Chemical reactors are vessels, wherein chemical reactions are carried out; their performance determines the reliability and suitability of a process, its environment safety, the consumption of energy and the raw materials required.
  • a continuous reactor is a reactor where there are no moving parts other than pumps that deliver the reactants. To achieve efficient mixing of reactants the addition of static mixing elements such as glass beads inside the reactor is done that provides ideal conditions of radial mixing and continuous flow necessary to perform reactions.
  • One such example of a continuous reactor is plug flow reactor. In a plug flow reactor, the flow of reactants pumped in the reactor is laminar and the properties of the reaction medium i.e. pressure, temperature, reactant and product concentrations are the same throughout the entire cross section of flow.
  • Plug flow reactors usually operate in adiabatic and non-isothermal conditions. Consequently, from the standpoint of kinetic parameters of a chemical reaction under isothermal conditions, plug flow reactors are more efficient than stirred tank reactors.
  • the present invention provides an improved method for the preparation of histamine or pharmaceutically acceptable salts thereof using a continuous reactor.
  • the process has distinct advantages in regard to cycle time, energy consumption, yield and product purity over traditional methods.
  • the process employs application of continuous reactor technology for the preparation of desired product in high yield and high purity with enhanced in-process control on impurities with shorter reaction time.
  • the present invention provides a process for the preparation of histamine or pharmaceutically acceptable salts thereof, comprising
  • a solution of L-histidine is prepared using a solvent and a catalyst.
  • the solvent used is selected from the group comprising of alcohols such as ethylene glycol and the like; aromatic hydrocarbon such as toluene, xylene and the like; aprotic polar solvents such as N-methyl pyrrolidone, N,N-dimethylformamide, dimethylsulphoxide and the like; water or mixtures thereof.
  • the catalyst used is selected from the group comprising of acetophenone, 4-methylacetophenone, 4-nitroacetophenone, 4-bromoacetophenone, benzoyl peroxide, 2,2'-azobisisobutyronitrile, cyclohexanone and the like.
  • the solution of L-histidine and the catalyst is prepared at room temperature.
  • the catalyst is used in 0.5 to 1.5 mole equivalents of L-histidine.
  • the decarboxylation reaction of L-histidine is carried out by feeding the solution prepared in step (a) at the flow rate of 20-80 ml/min at reflux temperature to a continuous reactor.
  • the continuous reactor used is selected from the group comprising of plug flow reactor and the like.
  • the reaction is optionally carried out under inert atmosphere or under an inert gas stream at reflux temperature of the solvent of the solution. Examples of the inert gas include nitrogen, helium, neon, argon and the like.
  • the residence time necessary in the method according to the invention depends on various parameters, such as, for example, the temperature or reactivity of the starting materials.
  • the term "residence time" refers to the internal volume of the reaction zone within the continuous reactor occupied by the reactant fluid flowing through the space, at the temperature and pressure being used.
  • the residence time is between about 1 minute and about 10 minutes.
  • the resulting reaction mixture is subjected to various isolation techniques to isolate histamine such as extraction, filtration, distillation etc.
  • histamine obtained is optionally converted to its pharmaceutically acceptable salts selected from the group comprising of hydrochloride, hydrobromide, tartrate, oxalate and the like.
  • the final product is optionally purified by a suitable recrystallization procedure known in the literature.
  • the histamine hydrochloride obtained is having purity not less than 99 %.
  • Example 2 Purification of histamine dihydrochloride: To histamine hydrochloride (100 g), added methanol (800 ml) and raised the temperature of reaction mass to 60-70 °C and stirred to get a clear solution. To the clear solution added carbon (5 g) at 50-55 °C and stirred for another 30 minutes. The solution was filtered and the solvent was partially distilled out. The resulting reaction mass, added isopropyl alcohol (300 ml) and raised the temperature of reaction mass to 60-70 deg C, stirred at this temperature for about 1 hour. The reaction mass was cooled slowly to 10-15 °C while stirring. The solid so obtained was filtered and dried to obtain histamine dihydrochloride .

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

L'invention concerne un procédé commercialement viable, rentable et énergétiquement efficace pour la préparation de 2-(1H-imidazol-4-yl) éthanamine ou de ses sels pharmaceutiquement acceptables avec une pureté élevée et un haut rendement par l'application d'une technologie d'écoulement continu.
PCT/IN2017/050610 2017-07-03 2017-12-22 Procédé continu pour la préparation de 2-(1h-imidazol-4-yl) éthanamine et de ses sels pharmaceutiquement acceptables WO2019008594A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IN201711023282 2017-07-03
IN201711023282 2017-07-03

Publications (1)

Publication Number Publication Date
WO2019008594A1 true WO2019008594A1 (fr) 2019-01-10

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113045500A (zh) * 2021-03-31 2021-06-29 苏州园方生物科技有限公司 一种组胺二盐酸盐的制备方法

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6403806B1 (en) * 1998-12-23 2002-06-11 Maxim Pharmaceuticals, Inc. Synthesis of histamine dihydrochloride
US7485756B2 (en) * 2006-12-20 2009-02-03 Evonik Degussa Gmbh Continuous process for decarboxylating carboxylic acids

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6403806B1 (en) * 1998-12-23 2002-06-11 Maxim Pharmaceuticals, Inc. Synthesis of histamine dihydrochloride
US7485756B2 (en) * 2006-12-20 2009-02-03 Evonik Degussa Gmbh Continuous process for decarboxylating carboxylic acids

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113045500A (zh) * 2021-03-31 2021-06-29 苏州园方生物科技有限公司 一种组胺二盐酸盐的制备方法

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