EP0564587A1 - Solution phase process for synthesis of peptide - Google Patents
Solution phase process for synthesis of peptideInfo
- Publication number
- EP0564587A1 EP0564587A1 EP92903706A EP92903706A EP0564587A1 EP 0564587 A1 EP0564587 A1 EP 0564587A1 EP 92903706 A EP92903706 A EP 92903706A EP 92903706 A EP92903706 A EP 92903706A EP 0564587 A1 EP0564587 A1 EP 0564587A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- boc
- trp
- lys
- phe
- ala
- 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- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
- C07K14/435—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
- C07K14/575—Hormones
- C07K14/60—Growth hormone-releasing factor [GH-RF], i.e. somatoliberin
-
- 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
- C07K1/02—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length in solution
-
- 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
- C07K1/061—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 protecting groups
- C07K1/064—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 protecting groups for omega-amino or -guanidino functions
Definitions
- This invention relates to a process for preparing the peptide:
- This peptide has pituitary growth hormone releasing activity.
- This invention also relates to intermediates used in the process of the invention.
- the method of preparing this peptide which is exemplified in U.S. 4,411,890 is a solid phase process in which the starting material amino acid is attached to a resin and is then coupled stepwise with the appropriate amino acids.
- the intermediates in the solid phase process are peptide-resin compounds.
- the desired peptide product is cleaved from the resin by treatment with hydrogen fluoride.
- This invention provides an advantageous process for preparing L-His-D-Trp-L-Ala-L-Trp-D-Phe-L-Lys-NH2.
- the process is a solution phase method which provides solid, recrystallizable intermediates which are readily isolated and purified. These solid intermediates are generally crystalline and may be purified by recrystallization. Solid, recrystallizable intermediates, particularly in all steps of a process, are rare in peptide chemistry and offer an advantage in purification.
- this invention is a process for preparing a compound of the formula:
- hich comprises : a) coupling L-Lys (BOO -NH2 with Z-D-Phe; b) removing the Z group and coupling the resulting D- Phe-L-Lys(BOC)-NH 2 with Z-L-Trp-NH 2 ; c) removing the Z group and coupling the resulting L- Trp-D-Phe-L-Lys (BOC)-NH 2 with Z-L-Ala; d) removing the Z group and coupling the resulting L- Ala-L-Trp-D-Phe-L-Lys(BOC)-NH 2 with Z-D-Trp; e) removing the Z group and coupling the resulting D- Trp-L-Ala-L-Trp-D-Phe-L-Lys (BOC)-NH 2 with (BOC) 2 -L-His; and f) removing the BOC groups to give L-His-D-Trp-L
- the intermediates are preferably recrystallized at each step in the process to prevent the build up of impurities.
- the purifi ⁇ * " -.ion of the final product is facilitated.
- the solution phase method of this invention avoids the use of corrosive hydrogen fluoride which is used in the solid phase procedure to cleave the product from the resin.
- the solution phase process of the invention requires only one acid treatment (at the end of the reaction process to remove the amino protecting groups) , thus minimizing decomposition of the tryptophan residues; whereas, the solid phase method involves repetitive acid treatments.
- Protected peptide intermediates in the process of this invention are also a feature of this invention.
- the intermediates are particularly useful in the process of this invention because they are solids, generally crystalline and are readily purified by recrystallization.
- the 'process of this invention may be represented as follows:
- L-Trp L-tryptophan
- L-Ala L-alanine
- WSC water soluble carbodiimide [1- (3-dimethylamino- propyl) -3-ethylcarbodiimide hydrochloride]
- intermediates (I) -(VI) are recrystallized before being used in the subsequent steps.
- Intermediates (II) -(VI) are prepared by removing the benzyloxycarbonyl group (Z) by catalytic hydrogenolysis and then coupling with the appropriate amino acid.
- N( ⁇ ) -benzyloxycarbonyl-N( ⁇ ) -t- butyloxycarbonyl-L-lysine amide (I) is prepared from N( ⁇ )- benzyloxycarbonyl-N( ⁇ )-t-butyloxycarbonyl-L-lysine by reacting with ammonia, water soluble carbodiimide [i.e. I- 3 (dimethylaminopropyl) -3-ethylcarbodiimide hydrochloride], and 1-hydroxybenzotriazole.
- the t-butyloxycarbonyl groups are removed using acid, optionally and a carbonium ion scavenger.
- Suitable acids for removing the t-butyloxycarbonyl group are well known in the art, and include mineral acids or strong organic acids, such as trifluoroacetic acid.
- Carbonium ion scavengers are also well known in the art, and include electrophilic aryl compounds and mercaptans, such as n-propylmercaptan.
- the hydrogenolysis to remove Z protecting groups is performed using an appropriate catalyst, for example palladium on carbon, such as 5-10% palladium on carbon. Preferably, 10% palladium on carbon is. used.
- the pressure at which the hydrogenolysis is performed is not critical, and may be performed at from atmospheric pressure up to several hundred psi. Typically, it is performed at atmospheric pressure up to 100 psi. Increasing the hydrogen pressure enhances the rate of reaction. Performing the reaction at about 100 psi is preferred. Vigorous stirring, such as about 600 rpm, in the autoclave is very advantageous to increase the reaction rate.
- Coupling reactions are well known in the art and may be accomplished by activating the carboxyl group of the intermediate, such as by formation of an acyl halide, activated ester or activated anhydride, or coupling with a coupling reagent such as a carbodiimide, for example dicyclohexylcarbodiimide or water soluble carbodiimide, PPA (1-propanephosphonic acid cyclic anhydride) , DPPA (diphenylphosphoryl azide) or BOP reagent (benzotriazol-1- yloxy-tris (dimethylamino)-phosphonium hexafluorophosphate) . Water soluble carbodiimide is preferred.
- the coupling reaction solutions are poured into aqueous base, for example, in the preparation of intermediates (II)-(V), the coupling reaction solutions are poured into aqueous potassium carbonate or potassium bicarbonate solution with vigorous stirring.
- the coupling reaction solution is, preferably, poured into aqueous potassium bicarbonate solution.
- the aqueous potassium bicarbonate is stirred vigorously.
- the rate of addition should be about 500 mL- 1 L/minute.
- the BOC protecting groups are removed with acid, optionally in the presence of a carbonium ion scavenger.
- Trifluoroacetic acid is a suitable acid for removing the BOC group.
- Use of a carbonium ion scavenger is preferred.
- Typical carbonium ion scavengers are anisole, dimethoxy benzene and mercaptans.
- n-Propyl mercaptan is suitable.
- reaction mixture was filtered through a DMF-washed bed of Celite®. In turn, the solids were rinsed with DMF (35 mL) and the filtrate and washings were combined.
- reaction mixture was filtered through a DMF-washed bed of Celite® and then was added slowly and with vigorous stirring into aqueous potassium carbonate solution (5% w/v, 1.6 L) .
- the solid which precipitated was collected on a Buchner funnel and the filter cake washed with deionized water (about 1.2 L) until the eluant was neutral to pH paper.
- the solid was dissolved in boiling isopropanol (240 mL) . To the boiling solution, deionized water (approximately 240 mL) was added to cloud point; the resulting solution was cooled at 0- 5°C overnight.
- reaction mixture was filtered through a DMF-washed bed of Celite®. In turn, the solids were rinsed with DMF (50 mL) and the filtrate and washings were combined.
- reaction mixture When the WSC had dissolved, the reaction mixture was allowed to stir at ambient temperature for 2.5 hours. At this time, TLC indicated the absence of D-Phe-L-Lys (BOC)-NH 2 .
- the reaction mixture was filtered through a DMF-washed bed of Celite® and then was added slowly and with vigorous stirring into aqueous potassium carbonate solution (5% w/v, 1.6 L) .
- the product separated as a solid which was collected at the pump and washed with deionized water (1.2 L) until the washings were no longer basic.
- the damp cake was dissolved in boiling methanol (500 mL) ; deionized water (150 mL) was added to cloud point. The solution was allowed to cool at 0- 5°C overnight .
- TLC indicated the absence of starting material; HPLC showed a trace to be remaining.
- the reaction mixture was filtered through a DMF-washed bed of Celite®. In turn, the solids were -rinsed with DMF (50-mL) and the filtrate and washings were combined.
- the reaction mixture was filtered through a DMF-washed bed of Celite® and then was added slowly and with vigorous stirring into aqueous potassium carbonate solution (5% w/v, 1.6 L) .
- the product separated as a solid, which was collected at the pump and washed with deionized water (1.6 L) until the washings were neutral.
- the damp filter cake was dissolved in boiling methanol (700 mL) ; deionized water (300 mL) was added to cloud point. The resulting solution was cooled overnight at 0-5°C.
- TLC indicated the absence of starting material; HPLC showed a trace to be remaining.
- the reaction mixture was filtered through a DMF-washed bed of Celite®. In turn, the solids were rinsed with DMF (50 mL) and the filtrate and washings were combined.
- reaction mixture was filtered through a DMF-washed bed of Celite®. In turn, the solids were rinsed with DMF (50 mL) and the filtrate and washings were combined.
- reaction mixture was evaporated to a gum which was dissolved in distilled water (300 mL) and re-evaporated twice. Then, the mixture was dissolved in distilled water (1 L) and the pH was adjusted to approximately 3 by the dropwise addition of dilute aqueous ammonium hydroxide solution.
- This material was purified by reverse phase liquid chromatography using YMC-type AS-5055, end-capped octadecyl silica, spherical in shape, with a particle size of 50 ⁇ and a pore size of 120 A 0 .
- the bed size was 5 cm i.d. x 50 cm length, corresponding to a bed volume of 981 mL, packed in a stainless steel HPLC column. There was also a guard column of 5 cm i.d. x 10 cm length containing the same packing material (196 mL) .
- This was equilibrated with 0.1 M aqueous ammonium acetate solution pH 4.5 (4 L) , utilizing a Beckman Prep-350 HPLC system, monitoring the eluant at 254 nm.
- the above pH adjusted reaction mixture was further diluted with distilled water (300 mL) and then applied to the column at a flow rate of 100 mL/min.
- the column was washed with 1.0 M ammonium acetate pH 8 (6.0 L), followed by 0.1 M ammonium acetate pH 4.5 (2.5 L) .
- the product was removed by step-wise elution with solutions of acetonitrile in 0.1 M aqueous ammonium acetate pH 4.5 as follows: 10% v/v (1 L) , 15% v/v (900 mL) , 17% v/v (1 L) , 20% v/v (2.5 L) , 25% v/v (2.5 L) .
- Fractions were collected, varying in size from 125 mL to 1 L.
- the column was washed with 50% v/v acetonitrile in 0.1 M aqueous ammonium acetate pH 4.5 (3.5 L) .
- A 1/4 v/v acetonitrile/water-0.1M ammonium dihydrogen phosphate- 0.8M phosphoric acid (adjusted to pH 3.0 with triethylamine)
- B 3/7 v/v acetonitrile/water-0.1M ammonium dihydrogen phosphate-0.8M phosphoric acid (adjusted to pH 3.0 with triethylamine), 0% B for 23 min, 0%-100% B over 37 min, UV detection at 210 nm) .
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Medicinal Chemistry (AREA)
- Biophysics (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Biochemistry (AREA)
- Molecular Biology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Analytical Chemistry (AREA)
- Endocrinology (AREA)
- Toxicology (AREA)
- Zoology (AREA)
- Gastroenterology & Hepatology (AREA)
- Peptides Or Proteins (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Procédé pour préparer, en phase de solution, le peptide L-His-D-Trp-L-Ala-L-Trp-D-Phe-L-Lys-NH2, qui fait preuve d'une activité libératrice de l'hormone de croissance hypophysaire.Process for preparing, in solution phase, the peptide L-His-D-Trp-L-Ala-L-Trp-D-Phe-L-Lys-NH2, which exhibits a liberating hormone activity pituitary growth.
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US62109490A | 1990-11-30 | 1990-11-30 | |
| US621094 | 1990-11-30 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0564587A1 true EP0564587A1 (en) | 1993-10-13 |
| EP0564587A4 EP0564587A4 (en) | 1994-08-24 |
Family
ID=24488689
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP9292903706A Withdrawn EP0564587A4 (en) | 1990-11-30 | 1991-11-25 | Solution phase process for synthesis of peptide |
Country Status (10)
| Country | Link |
|---|---|
| EP (1) | EP0564587A4 (en) |
| JP (1) | JPH06503578A (en) |
| KR (1) | KR930703345A (en) |
| AU (1) | AU9166491A (en) |
| CA (1) | CA2097305A1 (en) |
| IE (1) | IE914157A1 (en) |
| MX (1) | MX9102333A (en) |
| PT (1) | PT99654A (en) |
| WO (1) | WO1992009620A1 (en) |
| ZA (1) | ZA919440B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3480848B2 (en) * | 1992-06-19 | 2003-12-22 | タカラバイオ株式会社 | Method for synthesizing cyclic peptides |
| GB0814519D0 (en) * | 2008-08-08 | 2008-09-17 | Imp Innovations Ltd | Process |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4411890A (en) * | 1981-04-14 | 1983-10-25 | Beckman Instruments, Inc. | Synthetic peptides having pituitary growth hormone releasing activity |
| US4105652A (en) * | 1977-08-05 | 1978-08-08 | Hoffmann-La Roche Inc. | Synthesis of human β-endorphin |
| US4237046A (en) * | 1979-04-27 | 1980-12-02 | Miklos Bodanszky | Polypeptides and methods of preparation |
| JPH05508859A (en) * | 1990-07-24 | 1993-12-09 | イーストマン コダック カンパニー | Peptide synthesis method |
-
1991
- 1991-11-25 WO PCT/US1991/008863 patent/WO1992009620A1/en not_active Ceased
- 1991-11-25 JP JP4503322A patent/JPH06503578A/en active Pending
- 1991-11-25 CA CA002097305A patent/CA2097305A1/en not_active Abandoned
- 1991-11-25 EP EP9292903706A patent/EP0564587A4/en not_active Withdrawn
- 1991-11-25 KR KR1019930701616A patent/KR930703345A/en not_active Withdrawn
- 1991-11-25 AU AU91664/91A patent/AU9166491A/en not_active Abandoned
- 1991-11-29 PT PT99654A patent/PT99654A/en not_active Application Discontinuation
- 1991-11-29 ZA ZA919440A patent/ZA919440B/en unknown
- 1991-11-29 IE IE415791A patent/IE914157A1/en not_active Application Discontinuation
- 1991-12-02 MX MX9102333A patent/MX9102333A/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| CA2097305A1 (en) | 1992-05-31 |
| IE914157A1 (en) | 1992-06-03 |
| MX9102333A (en) | 1993-06-01 |
| JPH06503578A (en) | 1994-04-21 |
| WO1992009620A1 (en) | 1992-06-11 |
| PT99654A (en) | 1992-10-30 |
| ZA919440B (en) | 1992-12-30 |
| EP0564587A4 (en) | 1994-08-24 |
| KR930703345A (en) | 1993-11-29 |
| AU9166491A (en) | 1992-06-25 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
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| 17P | Request for examination filed |
Effective date: 19930602 |
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| AK | Designated contracting states |
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| A4 | Supplementary search report drawn up and despatched |
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| 17Q | First examination report despatched |
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| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
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| 18D | Application deemed to be withdrawn |
Effective date: 19960829 |