IE893717L - A process for the preparation of tripeptides - Google Patents

A process for the preparation of tripeptides

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Publication number
IE893717L
IE893717L IE893717A IE371789A IE893717L IE 893717 L IE893717 L IE 893717L IE 893717 A IE893717 A IE 893717A IE 371789 A IE371789 A IE 371789A IE 893717 L IE893717 L IE 893717L
Authority
IE
Ireland
Prior art keywords
denotes
compound
general formula
formula
protective group
Prior art date
Application number
IE893717A
Other versions
IE67293B1 (en
Inventor
Hanswolfram Flemming
Manfred Rukwied
Manfred Schmidt
Original Assignee
Timothy Gerard Vaughan
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 Timothy Gerard Vaughan filed Critical Timothy Gerard Vaughan
Publication of IE893717L publication Critical patent/IE893717L/en
Publication of IE67293B1 publication Critical patent/IE67293B1/en

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Classifications

    • 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
    • C07K5/08—Tripeptides
    • C07K5/0821—Tripeptides with the first amino acid being heterocyclic, e.g. His, Pro, Trp
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/06—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length using protecting groups or activating agents
    • C07K1/08—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length using protecting groups or activating agents using activating agents
    • C07K1/082—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length using protecting groups or activating agents using activating agents containing phosphorus
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/55—Design of synthesis routes, e.g. reducing the use of auxiliary or protecting groups

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Biophysics (AREA)
  • Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Analytical Chemistry (AREA)
  • Peptides Or Proteins (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

Process for preparing tripeptides of the general formula I U-A-B-C-OH I in which U is hydrogen or a urethane protective group and A, B and C are amino acids, by reacting a compound of the general formula II U'-B-OH II in which U' is a urethane protective group which can be eliminated by hydrogenolysis, with a compound of the general formula III H-C-OR III in which R is alkyl, by the PPA method, eliminating U', reacting the compound obtained in this way with a compound of the general formula IV H-B-C-OR IV by the PPA method and subsequently eliminating R enzymatically.

Description

(rt- HOECHST AKTIENGESELLSCHAFT HOE 88/F 327 67293 Dr. MY/je Description A process for the preparation of tripeptides Tripeptides are important intermediates in the synthesis 5 of bioactive peptides such as, for example, the hypothalamus hormone gonadorelin and its analogs. For this purpose the tripeptides must be available in the most straightforward manner possible, on the one hand in good yields and, on the other hand, in high purity. The 10 processes hitherto disclosed for the preparation of tripeptides do not meet these requirements in an optimal manner and are associated with disadvantages, some of which are serious. Thus, for example, even the products prepared by the process described in EP-A 156,280 are 15 contaminated with byproducts which become disadvantageous ly evident in the subsequent synthetic steps. Thus the object of the present invention is to provide a process for the preparation of tripeptides which does not have the said disadvantages and provides, in a straight-20 forward manner, products of high purity in good yields.
Accordingly, the invention relates to a process for the preparation of tripeptides of the general formula I U-A-B-C-OH 1 in which 25 U denotes hydrogen or a urethane protective group A denotes a natural a-amino acid or derivatives thereof B denotes a natural a-amino acid or derivatives thereof and 30 C denotes an aromatic a-amino acid, which comprises reacting a compound of the general formula II V - B - OH II - 2 - in which D' is a urethane protective group which can be eliminated by hydrogenolys is, and B has the above-mentioned meaning, with a compound of the general formula III H - C - OR 5 III in which R represents alkyl having 1 to 4 carbon atoms, and C has the abovementioned meaning, in the presence of propylphosphonic anhydride, eliminating the protective group U' by hydrogenolysis, reacting the resulting 10 compound of the general formula IV H - B - C - OR IV with a compound of the general formula V U - A - OH V in the presence of propylphosphonic anhydride, and 15 finally eliminating R enzymatically.
The urethane protective groups representing U are preferably the urethane protective groups customary in peptide chemistry, as are described, for example, in Kontakte Merck 3/79, page 14. 20 The benzyloxycarbonyl and the tert.-butyloxycarbonyl groups are particularly preferred.
A urethane protective group U' which can be eliminated by hydrogenolys is is preferably the benzyloxycarbonyl group.
Natural a-amino acids or their derivatives representing 25 A and/or B are preferably Gly, Ala, Ser, Thr, Val, Leu, lie, Glu, Gin, p-Glu, Tyr, Phe, Trp and His. Ser, Thr, Trp and Phe are particularly preferred.
An aromatic a-amino acid representing C is preferably Tyr or Phe. - 3 - R in the general formula IV preferably denotes methyl.
A process in which U and V denote benzyloxycarbonyl, A denotes Trp, B denotes Ser, C denotes Tyr and R denotes methyl is very particularly preferred. 5 The formation of a peptide linkage in the presence of propylphosphonic anhydride is known as the PPA method (Angew. Chem. Int. Ed. 1&, 133 (1980)). This reaction is preferably carried out in polar solvents such as, for example, dimethylacetamide, dimethylformamide, dimethyl 10 sulfoxide, phosphoric tris(dimethylamide), N-methyl-pyrro1idone or water. However, chloroform, methylene chloride or ethyl acetate are also employed.
It is also possible in an advantageous manner to use mixtures of the said solvents with water. An ethyl 15 acetate/water mixture is particularly preferred. The synthesis can be carried out between -10°C and room temperature. It is preferable to start at about 0°C and subsequently to raise to room temperature.
The elimination of the U' protective group by hydrogeno-20 lysis is advantageously carried out in a known manner with hydrogen on a Pd/C catalyst.
The enzymatic esterolysis in the last reaction step is preferably carried out with trypsin and/or a-chymotrypsin (Hoppe-Seylers Zeitschrift f. physiol. Chemie, 336. 248 25 (1964)). Trypsin is particularly preferred. Where appropriate, enzymes which are immobilized by known methods on a support are also used, such as described, for example, in EP-A 178,553. In this case, the enzymes are advantageously employed in amounts of 0.01 to 20 % by 30 weight relative to the amount of substrate. An amount of 2 % by weight of enzyme is particularly preferred.
Examples of solvents which can be employed are water, dimethylformamide, methanol, ethanol, isopropanol, butanol, ethyl acetate, butyl acetate, toluene or - 4 - methylene chloride.
An ethyl acetate/water mixture is preferred. The temperatures are advantageously between 0 and 60°C. A temperature range from 20 to 35°C is preferred. The pH of the reaction 5 medium is preferably in the range between 4 and 10, particularly preferably between 4 and 8.
The process according to the invention can be carried out in such a way that each intermediate is isolated. However, it is preferably carried out in a one-pot process, 10 that is to say without isolation of the intermediates.
The starting compounds of the general formulae II, III and V are known and can be obtained by the customary methods.
The process according to the invention surprisingly 15 provides products of high chemical and optical purity, which can be employed without difficulty in further syntheses. The yields are likewise excellent and are between 40 and 50 % based on the amount of the compound of the general formula III employed. 20 It has to be regarded as particularly surprising that the process according to the invention is distinctly superior, in terms both of purity and of yield, to the process of BP-A 156,280, which has only three stages.
Example 25 Z-Trp-Ser-Tyr-OH a) 350 ml of water are placed in a 2 1 stirred apparatus, and 47.8 g (0.200 mol) of Z-Ser-QH, 46.4 g (0.200 mol) of H-Tyr-QMexHCl and 150 g of sodium chloride are introduced. Also added are 700 ml of 30 ethyl acetate and, after everything has dissolved, the pH of the mixture is adjusted to 5.0 by addition of about 25 ml of N-ethylmorpholine. During the addition of about 220 ml (0.42 mol) of PPA solution (w(PPA) in % = 50) in about 30 minutes at a maximum of 30°C (cool somewhat at the end), about 110 ml (0.86 mol) of N-ethylmorpholine are added via a pH-stat pump at pH 5.0. The PPA addition is terminated when a precipitate forms in the reaction mixture. The precipitate is redissolved by subsequent addition of 350 ml of water. The aqueous phase is separated off in a separating funnel and then the ester phase is washed with 700 ml of potassium bisulfate solution (w(KHS04) in % ■ 10) and 700 ml of sodium bicarbonate solution (w(NaHC03) in % = 5). The aqueous phase from the reaction and the wash phases are discarded.
About 700 ml of ester phase from the 1st coupling, 200 ml of water and 3.3 g of palladium on carbon w(Pd) in % = 2.5 are placed in a 2 1 stirred apparatus and a stream of hydrogen is passed in at 25-30°C. During the reaction the pH is maintained at 4.0 with a pH-stat pump and addition of about 160 ml (0.16 mol) of hydrochloric acid c(HCl) = 1 mol/1. After the reaction is complete, when no more hydrochloric acid is consumed, (about 30 minutes) the reaction mixture is filtered through a suction funnel, and the aqueous phase is separated from the ester phase in a separating funnel. The ester phase is discarded.
About 430 ml of aqueous phase from the hydrogeno-lysis and 700 ml of ethyl acetate are placed in a 2 1 stirred apparatus and 50.7 g (0.15 mol) of Z-Trp-OH and 125 g of sodium chloride are added. After everything has dissolved, the pH is adjusted to 5.0 with about 19 ml of N-ethylmorpholine. During the addition of about 220 ml (0.42 mol) of PPA solution (w(PPA) in % - 50) in about 30 minutes at a maximum of 30°C (cool somewhat at the end), about 110 ml (0.86 mol) of N-ethylmorpholine are added via a pH-stat pump at pH 5.0. The PPA addition is terminated when a precipitate forms in the reaction mixture. The precipitate is redissolved by subsequent addition of 350 ml of water. The aqueous phase is separated off in a separating funnel, and then the ester phase is washed with 700 ml of potassium bisulfate solution (w(KHS04) in % = 10) and several times with 700 ml portions of sodium bicarbonate solution (w(NaHC03) in % = 5) until Z-Trp-OH has been completely removed (according to TLC analysis). The aqueous phase from the reaction and the wash phases are discarded.
About 700 ml of ester phase from the 2nd coupling and 700 ml of water are placed in a 2 1 stirred apparatus and heated to 35-40°C, and 1 g of trypsin is initially added. The reaction starts immediately and, during it, the pH is maintained constant at pH 7.0 with about 110 ml (0.11 mol) of sodium hydroxide solution (c(NaOH) = 1 mol/1). The reaction lasts about 7 hours and, during this, the rate is increased now and again by further addition of 0.5 g of trypsin. It is complete when trypsin addition now brings about only a slight increase in the rate of absorption of sodium hydroxide solution, or TLC analysis shows hardly any starting material remaining. The reaction solution is clarified through a suction funnel, and the ester phase is separated from the aqueous phase in a separating funnel. The ester phase is discarded.
The aqueous phase is initially extracted by shaking twice at pH 5.8-6.0, by addition and dissolution of 4.0 g of potassium dihydrogen phosphate, with 700 ml of ethyl acetate each time. The ester phases are discarded. The aqueous phase is then extracted by shaking three times at pH 5.0, adjusted by addition of about 5 ml of glacial acetic acid, with 700 ml of ethyl acetate each time. The aqueous phase is discarded. The ester phases contain the tripeptide - 7 - which, on evaparation to dryness in vacuo, remains in the form of loosely packed crystals. The product is dried in a vacuum oven at 40°C.
Weights 51.2 g 5 Yields 42.0 % based on H-Tyr-OMexHCl Puritys 98.2 % (determined with HPLC LiChrosorb Si 60/peptide buffer) Comparison Example Z-Trp-Ser-Tyr-OH was prepared by the process specified in 10 EP-A 156,280.
Yields 30 % Puritys 78.8 % (determined with HPLC LiChrosorb Si 60/peptide buffer)

Claims (12)

Patent claims HOE 88/F 327
1. A process for the preparation of tripeptides of the general formula I U-A-B-C-OH 1 in which U denotes hydrogen or a urethane protective group A denotes a natural a-amino acid or derivatives thereof B denotes a natural a-amino acid or derivatives thereof and C denotes an aromatic a-amino acid, which comprises reacting a compound of the formula II U' - B - OH 11 in which U' is a urethane protective group which can be eliminated by hydrogenolys is, and B has the above-mentioned meaning, with a compound of the formula III H - C - OR in in which R represents alkyl having 1 to 4 carbon atoms, and C has the abovementioned meaning, in the presence of propylphosphonic anhydride, eliminating the protective group U' by hydrogenolysis, reacting the resulting compound of the formula IV H - B - C - OR IV with a compound of the formula V U - A - OH V in the presence of propylphosphonic anhydride, and finally eliminating R enzymatic ally.
2. The process as claimed in claim 1, wherein U denotes benzyloxycarbonyl or tert. -butyloxycarbonyl.
3. The process as claimed in claim 1 and/or 2, wherein A and/or B denote Gly, Ala, Ser, Thr, Val, Leu, lie, Glu, Gin, p-Glu, Tyr, Phe, Trp or His.
4. The process as claimed in one or more of claims 1 to 3, wherein A and/or B denote Ser, Thr, Trp or Phe.
5. The process as claimed in one or more of claims 1 to 4, wherein C denotes Tyr or Phe.
6. The process as claimed in one or more of claims 1 to 5, wherein U' denotes benzyloxycarbonyl.
7. The process as claimed in one or more of claims 1 to 6, wherein R denotes methyl.
8. The process as claimed in one or more of claims 1 to 7, wherein the reactions are carried out in the presence of propylphosphonic anhydride in an ethyl acetate/water mixture.
9. The process as claimed in one or more of claims 1 to 8, wherein the enzymatic esterolysis is carried out with trypsin and/or a-chymotrypsin.
10. The process as claimed in one or more of claims 1 to. 9, wherein U and U' denote benzyloxycarbonyl, A denotes Trp, B denotes Ser, C denotes Tyr and R denotes methyl.
11. A process according to claim 1 for the preparation of a tripeptide of the general formula I given and defined therein, substantially as hereinbefore described and exemplified.
12. A tripeptide of the general formula I given and defined in claim 1, whenever prepared by a process claimed in a preceding claim. - 10 - Dated this the 21st day of November, 198? F. R. KELLY & CO. pv-M|f t| — 4p EXECUTIVE ClVde 27 Clyde Road, pa-nTsbridge f Dublin 4. AGENTS FOR THE APPLICANTS.
IE371789A 1988-11-22 1989-11-21 A process for the preparation of tripeptides IE67293B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE3839379A DE3839379A1 (en) 1988-11-22 1988-11-22 METHOD FOR PRODUCING TRIPEPTIDES

Publications (2)

Publication Number Publication Date
IE893717L true IE893717L (en) 1990-05-22
IE67293B1 IE67293B1 (en) 1996-03-20

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Application Number Title Priority Date Filing Date
IE371789A IE67293B1 (en) 1988-11-22 1989-11-21 A process for the preparation of tripeptides

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EP (1) EP0370399B1 (en)
JP (1) JP2843618B2 (en)
AT (1) ATE124053T1 (en)
AU (1) AU626608B2 (en)
CA (1) CA1335493C (en)
DE (2) DE3839379A1 (en)
DK (1) DK173690B1 (en)
ES (1) ES2075028T3 (en)
IE (1) IE67293B1 (en)
IL (1) IL92368A0 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004029812A1 (en) 2004-06-19 2006-05-24 Clariant Gmbh Process for the preparation of nitriles from aldehyde oximes by reaction with alkylphosphonic anhydrides
DE102004029811A1 (en) * 2004-06-19 2006-01-12 Clariant Gmbh Process for the preparation of alkenes by elimination of water from alcohols with alkylphosphonic anhydrides

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE7801373L (en) * 1978-02-07 1979-08-08 Kabi Ab EASY SPLABLE SUBSTRATE FOR QUANTIFIATION OF PROTEASES
US4293648A (en) * 1979-12-12 1981-10-06 G. D. Searle & Co. Process for esterification of α-L-aspartyl-L-phenylalanine
DE3411224A1 (en) * 1984-03-27 1985-10-10 Hoechst Ag, 6230 Frankfurt METHOD FOR THE RACEMATAR PRODUCTION OF INTERMEDIATE PEPTIDE PRODUCTS OF THE GONADORELIN AND GONADORELINANALOGA SYNTHESIS AND NEW INTERMEDIATE PRODUCTS IN THIS METHOD
DE3438189A1 (en) * 1984-10-18 1986-04-24 Hoechst Ag, 6230 Frankfurt METHOD FOR PRODUCING AROMATICALLY SUBSTITUTED L-AMINO ACIDS
US4888385A (en) * 1987-04-30 1989-12-19 Millipore Corporation BOP reagent for solid phase peptide synthesis
US4946942A (en) * 1988-03-11 1990-08-07 Bioresearch, Inc. Urethane-protected amino acid-N-carboxyanhydrides

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AU626608B2 (en) 1992-08-06
IL92368A0 (en) 1990-07-26
DK173690B1 (en) 2001-06-25
ES2075028T3 (en) 1995-10-01
ATE124053T1 (en) 1995-07-15
IE67293B1 (en) 1996-03-20
JPH02219587A (en) 1990-09-03
DK584489A (en) 1990-05-23
CA1335493C (en) 1995-05-09
EP0370399B1 (en) 1995-06-21
DK584489D0 (en) 1989-11-21
DE58909308D1 (en) 1995-07-27
AU4532889A (en) 1990-05-31
EP0370399A2 (en) 1990-05-30
DE3839379A1 (en) 1990-05-23
JP2843618B2 (en) 1999-01-06
EP0370399A3 (en) 1991-09-18

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