Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07D—HETEROCYCLIC COMPOUNDS
  • C07D241/00—Heterocyclic compounds containing 1,4-diazine or hydrogenated 1,4-diazine rings
  • C07D241/02—Heterocyclic compounds containing 1,4-diazine or hydrogenated 1,4-diazine rings not condensed with other rings
  • C07D241/06—Heterocyclic compounds containing 1,4-diazine or hydrogenated 1,4-diazine rings not condensed with other rings having one or two double bonds between ring members or between ring members and non-ring members
  • C07D241/08—Heterocyclic compounds containing 1,4-diazine or hydrogenated 1,4-diazine rings not condensed with other rings having one or two double bonds between ring members or between ring members and non-ring members with oxygen atoms directly attached to ring carbon atoms
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07K—PEPTIDES
  • C07K5/00—Peptides containing up to four amino acids in a fully defined sequence; Derivatives thereof
  • C07K5/04—Peptides containing up to four amino acids in a fully defined sequence; Derivatives thereof containing only normal peptide links
  • C07K5/12—Cyclic peptides with only normal peptide bonds in the ring
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07K—PEPTIDES
  • C07K5/00—Peptides containing up to four amino acids in a fully defined sequence; Derivatives thereof
  • C07K5/04—Peptides containing up to four amino acids in a fully defined sequence; Derivatives thereof containing only normal peptide links
  • C07K5/06—Dipeptides
  • C07K5/06008—Dipeptides with the first amino acid being neutral
  • C07K5/06017—Dipeptides with the first amino acid being neutral and aliphatic
  • C07K5/0606—Dipeptides with the first amino acid being neutral and aliphatic the side chain containing heteroatoms not provided for by C07K5/06086 - C07K5/06139, e.g. Ser, Met, Cys, Thr

Definitions

• the present invention relates to novel chemical syntheses of 2,6-bis (methionyl) -1,4-diketopiperazine.
• US Pat. No. 3,980,653 discloses a process for the preparation of 3,6-bis (2-methylmercaptoethyl) -2,5-piperazinedione (methioninediketopiperazine) by reacting methionine hydantoin with methionine at 160 ° C. and a pressure of initially 9, 5 bar. The corresponding diketopiperazine was isolated by crystallization.
• WO 2010/043558 discloses processes for the preparation of methioninediketopiperazine by reacting N-carbamoyl-methionine, N-carbamoylmethioninamide, methionylhydantoin, methionine amide, 3- (methylmercapto) propionaldehyde-cyanohydrin, 3- (methylmercapto) propionaldehyde or methioninitrile.
• the object of the present invention was to provide a new, simpler and less expensive, on a production scale feasible process for the preparation of 2,6-bis (methionyl) -1, 4-diketopiperazine available. Description of the invention
• the reaction temperature in the reaction of methionine to DKP is below 170.0 ° C.
• the processes described in the prior art are carried out at temperatures of 170-175 ° C or higher. At these high temperatures, many impurities are formed when using methionine, which must be depleted by a complex and on a production scale impractical work-up. Due to the milder reaction conditions at comparable reaction times significantly less by-products formed in the process according to the present invention, which can be seen in the color of the reaction mixture.
• a particular advantage of the process according to the invention is the purity of the diketopiperazine obtained. This allows an easy, fast and thus cost-effective purification from the reaction mixture by crystallization.
• the temperature in step a) is at most 169.5 ° C, preferably at most 169.0 ° C, more preferably at most 168.0 ° C, even more preferably at most 166.0 ° C and particularly preferably 165.0 ° C.
• the temperature in step a) be from 145.0 ° C to 169.5 ° C, preferably from 145.0 ° C to 169.0 ° C, more preferably from 145.0 ° C to 168.0 ° C, even more preferably from 145.0 ° C to 166.0 ° C, and more preferably from 145.0 ° C to 165.0 ° C. It is further preferred that the temperature in step a) is from 155.0 ° C to 169.5 ° C, preferably from 155.0 ° C to 169.0 ° C, more preferably from 155.0 ° C to 168.0 ° C is more preferably from 155.0 ° C to 166.0 ° C, and more preferably from 155.0 ° C to 165.0 ° C.
• the temperature in step a) is from 160.0 ° C to 169.5 ° C, preferably from 160.0 ° C to 169.0 ° C, more preferably from 160.0 ° C to 168 , 0 ° C, even more preferably from 160.0 ° C to 166.0 ° C, and more preferably from 160.0 ° C to 165.0 ° C.
• the initial concentration of methionine in the reaction mixture is 20% by weight to 60% by weight, more preferably 30% by weight to 50% by weight.
• the initial mixing ratio (w / w) of methionine to polar protic solvent is In the reaction mixture, preferably from 1: 4 to 4: 1, in particular from 1: 4 to 1, 5: 1. Compliance with these preferred parameters has a positive effect on the crystallization of the product described below, by diluting the reaction solution after the reaction is initiated.
• the kinetics of the reaction deteriorates significantly. This is due to the process, in which DKP is formed and crystallized in the same reactor. At higher concentrations of methionine, the volume during the reaction is lower and the efficiency of passing the inert gas is inferior.
• the initial concentration of methionine may also be above 60% by weight, with DKP being formed and crystallized in separate reactors.
• the reaction mixture used is a mixture consisting essentially of a polar protic solvent and methionine.
• the polar protic solvent is a polyhydric alcohol, in particular a dihydric or trihydric alcohol. More preferably, the polar protic solvent is a polyhydric alcohol, in particular a dihydric or trihydric alcohol having 2-4 carbon atoms, in particular 2 or 3 carbon atoms. Further preferred is the polar protic solvent selected from the group consisting of glycols, ethylene glycol, 1, 2-propanediol, 1, 3-propanediol, glycerol and butanediol, more preferably ethylene glycol. In addition, mixtures of polyhydric alcohols can be used as a polar protic solvent, in particular a mixture of ethylene glycol and glycerol.
• mixtures of one or more polyhydric alcohols, in particular dihydric or trihydric alcohols, having 2-4 carbon atoms, in particular 2 or 3 carbon atoms, with another organic solvent which has a boiling point of more than 180.degree. be used.
• the polar protic solvent used is at least partially recycled. It is further preferred that the polar protic solvent used be recycled to at least 80%, preferably at least 85%, more preferably at least 90% and most preferably at least 91% recycled. The high recovery rate of the solvent and its reuse reduces costs.
• the polar protic solvent in particular the above-described polyhydric alcohol, serves as activating reagent of the carboxyl group of a methionine molecule, possibly resulting in the intermediacy of the corresponding ester, which under the given reaction conditions abreacted with the amino group of a second methionine molecule.
• the subsequent cyclization to the corresponding diketopiperazine is carried out analogously. Since the intramolecular reaction to a six-membered ring under these reaction conditions is kinetically favored, the reaction can not be stopped at the intermediate of the dipeptide. Without being bound by theory, it can be assumed that first a methionine dipeptide is formed, which then cyclizes directly or after further activation to the DKP. At the beginning of the reaction, a suspension is present in the reaction mixture, from which a solution forms as the conversion progresses. From the solution, after completion of the reaction, as described below, the DKP is crystallized.
• step a) of the process according to the invention is carried out for 1 to 48 h, preferably for 1 to 24 h, more preferably for 1 to 15 h and particularly preferably for 4 to 7 h.
• an inert gas stream is passed over or through the reaction mixture.
• the inert gas stream is passed over (not through) the reaction mixture.
• the measure that an inert gas stream is passed "over the reaction mixture” means that this inert gas stream is passed above the liquid level of the reaction mixture, which means that the inert gas stream is not introduced into or through the reaction mixture.
• the inert gas stream is passed through the reaction mixture.
• the inert gas in the introduction into the reaction mixture has a temperature of at least 100, 0 ° C, preferably at least 120, 0 ° C, more preferably at least 145.0 ° C, even more preferably at least 155.0 ° C and more preferably at least 160.0 ° C on.
• This measure - passing an inert gas stream over the reaction mixture or above the reaction mixture or through the reaction mixture - serves to remove the water which is released in the double condensation by means of zeotropic distillation from equilibrium in order to realize acceptable reaction times. Without the application of an inert gas stream, the reaction times would unacceptably increase in terms of days.
• the inert gas stream it is preferable that nitrogen, carbon dioxide, oxygen-depleted air (lean air), combustion gases or noble gases such as argon or helium is used as the inert gas. In a particularly preferred method, nitrogen is used as the inert gas.
• a particular advantage of the process according to the invention is the purity of the dic-topiperazine obtained.
• the reaction mixture is diluted after completion or to complete the reaction with a polar solvent and water and cooled to below 100, 0 ° C. This crystallizes the 2,6-bis (methionyl) -1, 4-diketopiperazine.
• the crystallized 2,6-bis (methionyl) -1, 4-diketopiperazine can now be separated as a solid, and washed white with ethylene glycol, acetone or methanol and finally be freed from organic solvent residues with water. Typically, a off-white product is obtained.
• the solid can be separated in an advantageous manner via a pressure filter press, centrifuge, a belt filter or a comparable solid liquid separation apparatus. The solid separation is advantageously carried out and therefore preferably at room temperature.
• the polar solvent used for dilution of the reaction mixture is preferably the same solvent used in the reaction mixture in the reaction.
• the polar solvent is a polar protic solvent, more preferably a polyhydric alcohol, in particular a 2-valent or 3-valent alcohol.
• the polar solvent is a polyhydric alcohol having 2-4 carbon atoms, especially 2 or 3 carbon atoms.
• the polar solvent is selected from the group of glycols, ethylene glycol, 1, 2-propanediol, 1, 3-propanediol, glycerol and butanediol, preferably ethylene glycol.
• mixtures of polyhydric alcohols can be used as a polar solvent, in particular a mixture of ethylene glycol and glycerol.
• the reaction mixture is diluted after the reaction or to terminate the reaction with a polar solvent, more preferably with ethylene glycol, and then diluted with water and thereby below 95 ° C. to less than 100.0 ° C C to 98.0 ° C, whereby the 2,6-bis (methionyl) -1, 4-diketopiperazine crystallized.
• a polar solvent more preferably with ethylene glycol
• the reaction mixture is diluted with a polar solvent, very particularly preferably with ethylene glycol, and cooled to 125.0 ° C. to 135.0 ° C., and then diluted with water and in the process to below 100.0 ° C., Preferably, cooled to 95.0 ° C to 98.0 ° C, wherein the 2,6-bis (methionyl) -1, 4-diketopiperazine crystallized.
• a polar solvent very particularly preferably with ethylene glycol
• the ratio (w / w) of the added to the reaction mixture polar solvent, in particular ethylene glycol, to the added water preferably 1: 4 to 4: 1, in particular 4: 3 to 3: 1.
• the temperature of the reaction mixture before dilution or upon initiation of dilution with the polar solvent be at least 145.0 ° C, preferably at least 150.0 ° C, more preferably at least 155.0 ° C, even further preferably at least 160.0 ° C is.
• the crystalline 2,6-bis (methionyl) -1, 4-diketopiperazine can then be separated off as a solid and washed white with ethylene glycol, acetone or methanol and finally freed from organic solvent residues with water, which advantageously and therefore preferably takes place at room temperature.
• the reaction mixture upon completion or completion of the reaction, is cooled by dilution with water only without prior dilution with an organic solvent to crystallize 2,6-bis (methionyl) -1,4-diketopiperazine.
• the addition of the water may be adjusted so that the reaction mixture is in particular at 135.0 ° C or below, preferably at 120.0 ° C or below, more preferably at 110.0 ° C or below, and still more preferably below 100, 0 ° C cools.
• the addition of the water for dilution and cooling of the reaction mixture can be carried out with or without pressure maintenance. If the dilution and cooling of the reaction mixture only by adding
• the addition of the water is adjusted so that the reaction mixture in particular at temperatures above 100.0 ° C to 135.0 ° C, preferably above 100.0 ° C to 120.0 ° C, more preferably above 100.0 ° C to 110.0 ° C cools and the further cooling to below 100.0 ° C by depressurization to atmospheric pressure.
• the addition of the water for dilution and cooling of the reaction mixture is adjusted so that an overpressure of 0.0 to 7.0 bar, preferably an overpressure of 0.0 to 3.0 bar, more preferably an overpressure of 0 , 0 to 2.0 bar is applied.
• the advantage of the measure of the pressure maintenance in the addition of the water for dilution and for cooling is in particular that it is possible in this procedure to use less water for cooling the reaction mixture.
• the reason for this is that the reaction mixture is further cooled while being vented to atmospheric pressure. At the same time, this further reduces the residual amount of water in the mother liquor to be distilled.
• this process variant in which, after the reaction, the addition of water to cool the reaction mixture to a temperature above 100.0 ° C under pressure (preferably to 7.0 bar, more preferably to 3.0 and more preferably to 2 , 0 bar overpressure), less water must be added to cool the reaction mixture, as if directly to a temperature of below
• the temperature of the reaction mixture before dilution or when diluting with water is at least 145.0 ° C, preferably at least 150.0 ° C, more preferably at least 155.0 ° C more preferably at least 160.0 ° C.
• the reaction mixture is cooled or allowed to cool without addition of substances after completion or completion of the reaction until a temperature is reached, in particular from 135.0 ° C to less than 145.0 ° C, preferably from 138.0 ° C to 142, 0 ° C, at which the diketopiperazine begins to crystallize, and finally diluted by the addition of water and cooled further.
• the washing step carried out with water serves to deplete the polar solvent previously used for the extraction.
• the solvents used for washing the product can also be redistilled and recycled.
• the solvent used to wash the crystallized 2,6-bis (methionyl) -1,4-diketopiperazine is at least partially recycled.
• the can Recycling rates of the solvent used for washing at least 90%, preferably at least 95%, more preferably at least 97%.
• the solid obtained can be separated in an advantageous manner via a pressure filter press, centrifuge, a belt filter or a comparable solid liquid separation apparatus, which advantageously and therefore preferably takes place at room temperature.
• the solvent used may be used, but it is preferable to use a polar solvent different from that used in the reaction mixture.
• the polar solvent used to wash the crystallized 2,6-bis (methionyl) -1,4-diketopiperazine is a polar solvent selected from the group consisting of nitriles, especially acetonitrile; cyclic and acyclic carboxylic acid esters, especially ethyl acetate; aromatic solvents, especially toluene; cyclic and acyclic carboxylic acid amides, especially dimethylformamide (DMF) and A / methyl-2-pyrrolidone (NMP); Carbonic acid esters, in particular dimethyl carbonate; cyclic and acyclic ethers, especially tetrahydrofuran (THF) and 2-methoxy-2-methylpropane (MTBE); Ketones
• a particular advantage of the present invention is the purity of the diketopiperazine obtained by the process.
• the purity of the product at the end of the reaction allows easy and rapid purification from the reaction mixture by direct crystallization.
• the reaction mixture is diluted with either a polar solvent and water after completion or completion of the reaction and cooled to below 100.0 ° C or only diluted with water without a prior dilution with a organic solvent, or cooled without addition of substances or allowed to cool until a temperature is reached at which the diketopiperazine begins to crystallize, and finally diluted by the addition of water and cooled.
• the present invention provides a process for isolation of 2,6-bis (methionyl) -1, 4-diketopiperazine from a reaction mixture containing the following steps:
• a temperature in particular from 135.0 ° C to less than 145.0 ° C, preferably from 138.0 ° C to 142, 0 ° C, at which the diketopiperazine begins to crystallize, and finally dilution by addition water and thereby cooling to crystallize 2,6-bis (methionyl) -1,4-diketopiperazine.
• step B) serves to deplete the previously to
• Extraction used polar solvent which is obtained in a very simple and advantageous manner, a product of high purity.
• the solvents used in the washing steps (step B)) can also be redistilled and recycled. Therefore, in another preferred process, the solvent used to wash the crystallized 2,6-bis (methionyl) -1,4-diketopiperazine is at least partially recycled.
• Recycling rates of the solvent used for washing at least 90%, preferably at least 95%, more preferably at least 97%.
• the variant A1 is obtained in a simple manner and without additional effort and also in shorter residence times a product of high purity. Therefore, the variant A1 is particularly advantageous.
• the solid from step B) can be separated in an advantageous manner via a pressure filter press, centrifuge, a belt filter or a comparable solid liquid separation apparatus, which advantageously and therefore preferably takes place at room temperature.
• the reaction mixture essentially consists of 2,6-bis (methionyl) -1,4-diketopiperazine, the originally used polar protic solvent, and not because of the reaction already carried out converted methionine, and optionally water and by-products of the reaction.
• the polar solvent used for diluting the reaction mixture according to step A1) is preferably the same solvent that was used in the reaction mixture for the reaction.
• the polar solvent is preferably a polar protic solvent, particularly preferably a polyhydric alcohol, in particular a dihydric or trihydric alcohol. More preferably, the polar solvent is a polyhydric alcohol having 2-4 carbon atoms, especially 2 or 3 carbon atoms. More preferably, the polar solvent is selected from the group of glycols, ethylene glycol, 1, 2-propanediol, 1, 3-propanediol, glycerol and butanediol, preferably ethylene glycol.
• reaction mixtures of polyhydric alcohols can be used as a polar solvent, in particular a mixture of ethylene glycol and glycerol.
• the reaction mixture is diluted in step A1) with a polar solvent and then diluted with water and cooled to below 100.0 ° C., preferably to 95.0 ° C to 98.0 ° C. wherein the 2,6-bis (methionyl) -1, 4-diketopiperazine crystallized.
• reaction mixture is diluted in step A1) with ethylene glycol and then diluted with water and cooled to below 100.0 ° C., preferably to 95.0 ° C.
• the ratio (w / w) of the polar solvent added to the reaction mixture, especially ethylene glycol, to the added water is preferably 1: 4 to 4: 1, more preferably 4: 3 to 3: 1
• the temperature of the reaction mixture before dilution or initiation of the dilution according to step A1) is at least 145.0 ° C, preferably at least 150.0 ° C, more preferably at least 155.0 ° C, more preferably at least 160.0 ° C.
• the reaction mixture is cooled after completion or completion of the reaction by diluting with water only without preliminary dilution with an organic solvent to crystallize 2,6-bis (methionyl) -1, 4-diketopiperazine.
• the addition of the water may be adjusted so that the reaction mixture is more preferably 135 ° C or lower, preferably 120 ° C or lower to 110.0 ° C or below, and even more preferably below 100.0 ° C.
• step A2) the addition of the water for dilution and cooling of the reaction mixture can be carried out with or without pressure maintenance.
• the addition of the water is adjusted such that the reaction mixture is heated in particular to temperatures above 100.0 ° C. to 135.0 ° C., preferably above 100.0 ° C to 120.0 ° C, more preferably above 100.0 ° C to 110.0 ° C cools and the further cooling to below 100.0 ° C by depressurization to atmospheric pressure.
• the addition of the water for dilution and cooling of the reaction mixture is adjusted so that an overpressure of 0.0 to 7.0 bar, preferably an overpressure of 0.0 to 3.0 bar, more preferably an overpressure of 0 , 0 to 2.0 bar is applied.
• the crystallized 2,6-bis (methionyl) -1, 4-diketopiperazine can then be separated as a solid, and washed white with ethylene glycol, acetone or methanol and finally with water to remove organic solvent residues.
• the temperature of the reaction mixture before dilution or initiation of dilution with water is at least 145.0 ° C, preferably at least 150.0 ° C, more preferably at least 155.0 ° C , even more preferably at least 160.0 ° C.
• step A3) the reaction mixture is cooled or allowed to cool without addition of substances after completion or completion of the reaction until a temperature is reached, in particular from 135.0 ° C to less than 145.0 ° C, preferably from 138.0 ° C to 142, 0 ° C, at which the diketopiperazine begins to crystallize, and finally diluted by the addition of water and cooled further.
• a solvent different from that used in the reaction mixture is used becomes.
• a polar solvent for washing the crystallized 2,6-bis (methionyl) -1, 4-diketopiperazine in step B a solvent different from that used in the reaction mixture is used becomes.
• a polar solvent for washing the crystallized 2,6-bis (methionyl) -1, 4-diketopiperazine in step B a solvent different from that used in the reaction mixture is used becomes.
• a polar solvent selected from the group consisting of nitriles, in particular acetonitrile; cyclic and acyclic carboxylic acid esters, in particular ethyl acetate; aromatic solvents, especially toluene; cyclic and acyclic carboxylic acid amides, in particular dimethylformamide mamid (DMF) and A / methyl 2-pyrrolidone (NMP); Carbonic acid esters, in particular dimethyl carbonate; cyclic and acyclic ethers, especially tetrahydrofuran (THF) and 2-methoxy-2-methylpropane (MTBE); Ketones, in particular acetone; Sulfoxides, in particular dimethyl sulfoxide (DMSO); Amines, in particular triethylamine; Carboxylic acids, especially acetic acid; chlorinated hydrocarbons, especially dichloromethane and chloroform; Alcohols, in particular triethylamine; Carboxylic acids, especially acetic acid
• the present invention relates to a process for the preparation of 2,6-bis (methionyl) -1, 4-diketopiperazine and in a second aspect provides a process for the isolation of 2,6-bis (methionyl) -1, 4-diketopiperazine prepared from a reaction mixture.
• the present invention provides a method according to a combination of the first and second aspects of the present invention. Therefore, the present invention relates in particular to a process for the preparation of 2,6-bis (methionyl) -1,4-diketopiperazine having the formula (I)
• reaction mixture containing methionine and a polar protic solvent at a temperature of less than 170.0 ° C., wherein an inert gas stream is passed over or through the reaction mixture, preferably via the reaction mixture, to the water formed in the reaction remove the reaction mixture;
• This method according to the combination of the first and second aspects of the present invention also includes the preferred embodiments, features, technical effects and advantages described herein with respect to the first and second aspects, which are referred to here.
• DKP 2,6-bis (methionyl) -1,4-diketopiperazine
• the workup could be simplified so that the process can even be used on an industrial scale.
• the impurities occurring in the synthesis of the DKP can be minimized.
• Essential to the invention are two measures:
• the reaction temperature in the conversion of methionine to DKP in step a) is below 170.0 ° C.
• the temperatures are preferably at most 169.5 ° C, at most 169.0 ° C, at most 168.0 ° C, at most 166.0 ° C, at most 165.0 ° C.
• the following temperature ranges are particularly preferred: 160.0 ° C to 169.5 ° C, 160.0 ° C to 169.0 ° C, 160.0 ° C to 168.0 ° C, 160.0 ° C to 166 , 0 ° C; most preferably the temperature range is 160.0 ° C to 165.0 ° C.
• step a) of the process according to the invention an inert gas stream, in particular a nitrogen stream, is passed over or through the reaction mixture to remove the equilibrium water which is liberated in the synthesis of the DKP by zeotropic distillation.
• an inert gas stream in particular a nitrogen stream
• the lower temperatures applied in the process of the invention compared to the processes described in the prior art lead to milder reaction conditions with comparable reaction times. This measure has a direct positive effect on the product, since significantly fewer by-products are formed.
• the higher purity of the diketopiperazine obtained by the process according to the invention enables easier, faster and more cost-effective separation and purification from the reaction mixture by means of crystallization.
• the means for heating or the heating jacket of the existing in the prior art reactors and apparatus are usually designed to be vacuum-stable.
• Apparatuses which are designed to be vacuum-stable can as a rule also be operated up to a pressure in a range around 6 bar.
• the method according to the invention can advantageously be carried out in existing multipurpose plants with existing apparatus which are usually designed for this pressure.
• the process of the invention is further illustrated by the following example, which, however, is not intended to be limiting of the invention described herein.
• the suspension was suctioned off via a pressure filter press (filter paper MN 616). Alternatively, a centrifuge can be used. The wool white filter cake (0 29 cm) was on the

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• 2016
  • 2016-06-28 CN CN201680046910.0A patent/CN107922355B/zh not_active Expired - Fee Related
  • 2016-06-28 US US15/741,846 patent/US20180194804A1/en not_active Abandoned
  • 2016-06-28 SG SG11201800148VA patent/SG11201800148VA/en unknown
  • 2016-06-28 WO PCT/EP2016/064982 patent/WO2017005547A1/de active Application Filing
  • 2016-06-28 RU RU2018104882A patent/RU2018104882A/ru not_active Application Discontinuation
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