SI9011225A - Improved production procedure of tripeptide aldehydes - Google Patents

Improved production procedure of tripeptide aldehydes Download PDF

Info

Publication number
SI9011225A
SI9011225A SI9011225A SI9011225A SI9011225A SI 9011225 A SI9011225 A SI 9011225A SI 9011225 A SI9011225 A SI 9011225A SI 9011225 A SI9011225 A SI 9011225A SI 9011225 A SI9011225 A SI 9011225A
Authority
SI
Slovenia
Prior art keywords
phe
pro
arg
lactam
formula
Prior art date
Application number
SI9011225A
Other languages
Slovenian (sl)
Inventor
Tibor Balogh
Eva Barabas
Maranna Dioszegi
Sandor Elek
Gyula Horvath
Lajos Ila
Attila Juhasz
Tibor Lang
Rihmer Zsuzsanna Lang
Attila Nagy
Erno Orban
Aranyosi Katalin Pal
Gyoergy Somogyi
Szabo Zsuzsa Pesti
Hasenoehrl Erzsebet Szell
Farago Katalin Szilagyi
Joszt Eva Tomori
Dievald Emilia Uskert
Original Assignee
Gyogyszerkutato Intezet
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 Gyogyszerkutato Intezet filed Critical Gyogyszerkutato Intezet
Publication of SI9011225A publication Critical patent/SI9011225A/en

Links

Landscapes

  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Peptides Or Proteins (AREA)

Description

POBOLJŠAN POSTUPAK ZA DOBIVANJE TRIPEPTIDNIH ALDEHIDAIMPROVED PROCEDURE FOR THE PREPARATION OF TRIPEPTID ALDEHYDS

OBLAST TEHNIKETECHNICAL FIELD

Pronalazak je iz oblasti hemije peptida.The invention is in the field of peptide chemistry.

TEHNIČKI PROBLEMTECHNICAL PROBLEM

Predmetni pronalazak se odnosi na poboljšan postupak za dobivnaje tripeptidnih aldehida formule I,The present invention relates to an improved process for the preparation of tripeptide aldehydes of formula I,

R-D-Phe-Pro-Arg-H.H2SO4 I gdeR-D-Phe-Pro-Arg-H.H2SO4 And where

R pedstavlja vodonik ili metil,R is hydrogen or methyl,

Phe označava fenilalanin grupu,Phe stands for the phenylalanine group,

Pro je L-prolinska grupa,Pro is an L-proline group,

Arg je L-argininska grupa u čistom stanju podesnom za farmaceutsko koriščenje.Arg is a pure L-arginine group suitable for pharmaceutical use.

/Skračenice L-prolina i L-arginina kao Pro i Arg su usaglasnosti sa prethodnom tehnikom,npr. Biochem.7,126,77311972),Biochemistry 14, 449(1975)/./ The abbreviations of L-proline and L-arginine such as Pro and Arg are in accordance with the prior art, e.g. Biochem.7,126,77311972), Biochemistry 14, 449 (1975) /.

STANJE TEHNIKEBACKGROUND OF THE INVENTION

Poznato je dasoli D-fenilalanin-L-prolil-L-arqinin aldehida (H-D-PHe-Pro-Arg-H)pokazuju antitrombinsku aktivnost.Medjutim, acetatna so opisana u Madjarskoj patentnoj specifikaciji br. 169 870 nije podesna za terapeutsko koriščenje jer gubi svojuThe known D-phenylalanine-L-prolyl-L-arqinin aldehydes (H-D-PHe-Pro-Arg-H) are known to exhibit antithrombin activity. However, the acetate salt described in Hungarian patent specification no. 169 870 is not suitable for therapeutic use because it is losing its own

2.2.

aktivnost vrlo brzo bilo da je u čvrstom ili tečnom obliku. Isti fenomen može biti opažen u slučaju drugih' šoli takvih kao hidro0 hlorid,citrat,tartarat,tozilat i N -karboksi .derivata tripeptid aldehida. Medjutim, sufatna so H-D-Phe-Pro-Arg-H i njen. .N-metil derivat, su.veoma.stabilni čak u obliku vodenog rastvora (Britanska patentna specifikacija br. 2 091 270 i publikovana evropske patentne prijava br. 185 390) i stoga mogu biti podesni za terapeutsko koriščenje .activity very quickly whether in solid or liquid form. The same phenomenon can be observed in the case of other schools such as hydrochloride, citrate, tartrate, tosylate and N-carboxy derivatives of the tripeptide aldehyde. However, sulphate with H-D-Phe-Pro-Arg-H and hers. .N-methyl derivative, very stable even in the form of an aqueous solution (British Patent Specification No. 2 091 270 and European Patent Application Publication No. 185 390) and may therefore be suitable for therapeutic use.

Gornje sulfatne soli se mogu dobiti kao što sledi:The above sulfate salts may be obtained as follows:

1. Sulfatna so H-D-Phe-Pro-Arg-H peptida se može dobiti prema britanskoj patentnoj specifikaciji br. 2 091 270 iz t^butoksikarbonilD-fenilalanil-L-prolil-L-arginin aldehid hemisulfata ili iz t-butoG ksikarbonil-D-fenilalanil-L-prolil-N -karboksi-L-arginin aldehida u prisustvu 1-12 ekvivalenata 1-12N vodene sumporne kiseline na temperaturi od 40-60°C. (Dobivanje polaznog prvog materijala je opisano u primeru 1 napred-citirane patentne specifikacije,dok je 0 dobivanje zaštičenog N -karboksi derivata dato Belgijskom paten.specif br. 880 844) .1. The sulphate salt of the H-D-Phe-Pro-Arg-H peptide is obtainable according to British Patent Specification no. 2 091 270 from t-butoxycarbonylD-phenylalanil-L-prolyl-L-arginine aldehyde hemisulfate or from t-butoxycarbonyl-D-phenylalanyl-L-prolyl-N-carboxy-L-arginine aldehyde in the presence of 1-12 equivalents 1- 12N aqueous sulfuric acid at 40-60 ° C. (Obtaining the starting first material is described in Example 1 of the previously cited patent specification, while 0 obtaining the protected N-carboxy derivative is given in Belgian Patent Spec. No. 880 844).

2. Sulfatna so H-D-Phe-Pro-Arg-H peptida se može dalje dobiti prema napred sitiranoj specifikaciji hidrogenolizom benziloksikarbonil-D0 fenilalani1-L-prolil-N -benziloksikarbonil-L-arginin. aldehida u prisustvu molarno ekvivalentne količine sumporne kiseline. (Dobivanje dvostruko-zaštičenog tripeptid aldehida koriščenog kao polazni materijal je opisano u Madjarskoj paten. specif. br. 169 870) .2. The sulphate salt of the H-D-Phe-Pro-Arg-H peptide can be further prepared according to the above specification by hydrogenolysis of benzyloxycarbonyl-D0 phenylalanyl-L-prolyl-N-benzyloxycarbonyl-L-arginine. of aldehydes in the presence of a molar equivalent amount of sulfuric acid. (Preparation of the double-protected tripeptide aldehyde used as starting material is described in the Hungarian Patent. Spec. No. 169 870).

3. Prema publikovanoj evropskoj patentnoj prijavi br. 185 3903. According to published European patent application no. 185 390

N-metil-D-fenilalanil-L-prolil-L-arginin aldehid sulfat (H-D-MePhe-Pro-Arg-H.H2SO4) je dobiven slično slobodnom tripeptid aldehidnom sulfatu uklanjanjem zaštitnih grupa iz N-benziloksikarbonil 0N-methyl-D-phenylalanil-L-prolyl-L-arginine aldehyde sulfate (HD-MePhe-Pro-Arg-HH 2 SO 4 ) was obtained similar to free tripeptide aldehyde sulfate by removing the protecting groups from N-benzyloxycarbonyl 0

N-metil-D-fenilalani1-L-prolil-N -benziloksikarbonil-L-arginin aldehida hidrogenolizom u prisustvu sumporne kiseline. (Dobivanje tripeptid aldehida koriščenog kao polazni materijal je takodje opisano u istoj patentnoj prijavi).N-Methyl-D-phenylalanyl-L-prolyl-N-benzyloxycarbonyl-L-arginine aldehyde by hydrogenolysis in the presence of sulfuric acid. (Preparation of a tripeptide aldehyde used as a starting material is also described in the same patent application).

Glavna mana gornjih postupaka je,naročito ako se proizvodnja vrši u večem obimu,da ne daje proizvod odgovarajuče čistoče.The main disadvantage of the above procedures, especially if the production is carried out on a large scale, is that it does not produce a product of adequate purity.

3.3.

Tako npr. proizvod dobiven pomoču postupka br.l obuhvata oko 4-6% kalcijum sulfata. Na osnovu naše slojno-hromatografske analize proizvod., tako dobiven može da obuhvataviše od oko 10% drugih nečifctoča (npr. tripeptid alkohol,-kiselinu,-acetal) sem kalcijumove soli; ovo znači da ukupna količina kontaminirajučih supstanci može da predje 20%. Dalja mana postupka je u torne što neutralizacija viška sumporne kiseline i tiltriranje staloženog kalcijam sulfata izaziva dalje teškoče.So e.g. the product obtained by method No. 1 comprises about 4-6% calcium sulfate. Based on our layer-chromatographic analysis, the product thus obtained may comprise up to about 10% of other impurities (e.g., tripeptide alcohol, -acid, -acetal) other than calcium salt; this means that the total amount of contaminants can exceed 20%. A further disadvantage of this process is that the neutralization of excess sulfuric acid and the filtration of calcium sulfate precipitates further difficulties.

Tripeptid aldehid sulfatna so dobivena postupkom br.2 (hidrogenoliza) obuhvata sem 5-10% zagradjivača deteltibilnih pomoču tanko-slojne hromatografije,daljih 10-15% tripeptid aldehid sulfata D-L-D konfiguracije prema HPLC analize: tako se gradi ukupno 15-25% zagadjivačkih sporednih proizvoda. Napred-pomenutih 5-10% zagadjivača je sastavljeno od sledečih supstanci: tripeptid kiselina nagradjena tokom sinteze tripeptid aldehida,tripetid alkohol,ciklični proizvod razlaganja strukture koja je opisana u publikovanoj Evropckoj patent, prijavi br.The tripeptide aldehyde sulfate salt obtained by process no. 2 (hydrogenolysis) comprises, except 5-10% of detellers, using thin layer chromatography, further 10-15% of the tripeptide aldehyde sulfate DLD configuration according to HPLC analysis: thus, a total of 15-25% of contaminants are constructed. product. The aforementioned 5-10% of contaminants are composed of the following substances: tripeptide acid rewarded during the synthesis of tripeptide aldehyde, tripetide alcohol, a cyclic decomposition product of the structure described in published European Patent Application no.

185 39u i supstanca nepoznate strukture nagradjena u raznim količinama mrlja koja se nalazi.ispod željeno jedinjenja na hromatogramu.185 39u and a substance of unknown structure rewarded in varying amounts of stain contained.under the desired compound on the chromatogram.

Opaženo je daprehidracija igra važnu ulogu u proizvodnji posledengeg sporednog proizvoda. Naime, ako se hidrogenoliza izvodi na poznat način,tj. u prisustvu lmolarnog ekvivalenta sumporne kiseline na sobnoj temperaturi i postupak se nastavlja posle završene hidrogenolize,dodatna mrlja (R^=0,39-0,44) koja odgovara zagadjivaču se uvek javlja ispod mrlje proizvoda ( u slučaju H-D-Phe-Pro-Arg-H.H2SO4) na tansko-slojnom hromatogramu (adsorbent: Kieselgel G,eluent: 25:20:6:11 smeša etilacetat/piridin/sirčetna kiselina/vodaj· razvijač: hlorptolidin), gde pomenuti zagadjivač,u nakim slučajevima,predstavlja glavnu nečistoču.It is noted that dahydration plays an important role in the production of the last by-product. Namely, if the hydrogenolysis is performed in a known manner, that is. in the presence of lmolar equivalent of sulfuric acid at room temperature and the process continues after complete hydrogenolysis, an additional stain (R ^ = 0.39-0.44) corresponding to the pollutant always occurs below the stain of the product (in the case of HD-Phe-Pro-Arg -H.H2SO4) on a thin-layer chromatogram (adsorbent: Kieselgel G, eluent: 25: 20: 6: 11 ethyl acetate / pyridine / acetic acid / water mixture · developer: chlorptolidine), in which cases the pollutant is, in some cases, the major impurity.

U cilju eliminisanja zagadjivanga,krajnji proizvod reakcije se mora detektovati veoma tačno i reakcija se mora zaustaviti kada se dostigne krajnja tačka.In order to eliminate contaminants, the end product of the reaction must be detected very accurately and the reaction must be stopped when the end point is reached.

Medjutim,kako krajnja tačka reakcije se odredjuje pomoču tankso-slojne hromatografske analize koja zahteva 20-30minuta rada pri koriščenju gornje eluentske smeše,reakcija se nemože zaustaviti na krajnjojHowever, as the reaction endpoint is determined by thin-layer chromatographic analysis, which requires 20-30 minutes of operation using the above eluent mixture, the reaction cannot be stopped at the final

4.4.

tačci naročito u industrijskim uslovima. Tako sporedni proizvod sa napred definisanom vrednošču se obično dobiva u količini od okopoint especially in industrial conditions. Thus a by-product with a predefined value is usually obtained in an amount of about

3-4% usled prehidracije. Pomenuti sporedni proizvod je toksičniji od krajnjeg proizvoda,stoga se mora eliminisati dobro iz ovog razloga3-4% due to overgrowth. The by-product mentioned is more toxic than the end product, so it must be eliminated well for this reason

Proizvod je vrlo osetljiv prema racemizaciji,stoga zagadjivačke supstance nagradjene tokom napred opisanih postupaka nemogu biti praktično uklonjene. Kako krajnji proizvod nemože biti prečiščen, u cilju postizanja čistoče krajnjeg proizvoda koja je podesna za farmaceutska koriščenje,proizvodnja intermedijera odgovarajuče čistoče i suzbijanje gradjenja sporednog proizvoda moraju biti rešeni OvO znači inhibiciju racemizacije tokom postupka.The product is highly sensitive to racemization, and therefore pollutants rewarded during the procedures described above cannot be practically removed. As the end product cannot be purified, in order to achieve purity of the end product which is suitable for pharmaceutical use, the production of intermediates of adequate purity and the suppression of construction of the by-product must be solved. This means to inhibit racemization during the process.

OPIS REŠENJA TEHNIČKOG PROBLEMA SA PRIMERIMA REALIZACIJEDESCRIPTION OF THE TECHNICAL PROBLEM SOLUTION WITH EXAMPLES

Cilj predmetnog pronalska je razvijanje postupka koji obezbedjuje suzbijanje gradjenja napred pomenutih sporednih proizvoda i dobivanje tripeptid aldehid soli formule I u čistoči od bar 95%.The object of the present invention is to develop a process that provides for the suppression of the construction of the above-mentioned by-products and the preparation of the tripeptide aldehyde salt of formula I in a purity of at least 95%.

Pronalazak je baziran na saznanju da gradjenje D-L-D proizvoda, tj. racemizacija je veoma zavisna od pH. U sredini koja ima alkalno pH, i čak u sredini sa neutralnim pH, krajnji proizvod i intermedijeri podležu racemizaciji. U sredini koja ima kiselo pH 6pH=2) krajnji proizvod je stabilan mesečima.Stoga mora se dati tehnologija koja obezbedjuje da pH reakcione smeše ne bude neutralno ili bazno čak ni kratko vreme. U cilju postizanja ovoga arginin laktam se oslobadja iz svoje soli in situ tokom mešane ahidridne kondenzacije GThe invention is based on the knowledge that the construction of D-L-D products, ie. racemization is highly pH dependent. In an environment that has an alkaline pH, and even in an environment with a neutral pH, the end product and intermediates are subject to racemization. In an environment that has an acidic pH of 6pH = 2) the end product is stable for months. Therefore, technology must be provided to ensure that the pH of the reaction mixture is not neutral or basic for even a short time. To achieve this, arginine lactam is released from its salt in situ during mixed anhydrous condensation G

N -benziloksikarbonll-L-arginin laktam hidrohlorida formule IVN-benzyloxycarbonyl-L-arginine lactam hydrochloride of formula IV

H.Arg(Z)-laktam.HCl (IV) gde Arg je isto kao što je definisano u uvodnom delu i Z označava benziloksikarbonil i dipeptida formule VH. Arg (Z) -lactam.HCl (IV) wherein Arg is as defined in the introductory part and Z denotes benzyloxycarbonyl and dipeptides of formula V

ZR(D-Phe)-Pro-OH (V) gde R,Phe i Pro su isti kao što je definisano u uvodnom delu,Z jeZR (D-Phe) -Pro-OH (V) where R, Phe and Pro are the same as defined in the introductory part, Z is

5.5.

isto kao što je definisano napred, na takav način da se baza zatim dodaje reakcionoj smeši. Pod takvim uslovima ,arginin laktam oslobodjen ln situ reaguje odjednom,in statu nascendl,sa mešanim anhidridom u odgovarajuč zaštičer. . tripeptid laktom formule IIIthe same as defined above, in such a way that the base is then added to the reaction mixture. Under such conditions, arginine lactam released in situ reacts at once, in a statue nascendl, with mixed anhydride to a suitable protector. . tripeptide by the elbow of formula III

ZR(D-Phe)-Pro-Arg(Z)-laktam (III) gde Z je isto kao što je definisano napred, a R,Phe,Pro i Arg su isti kao što je definisano u uvodnom delu, tako gradjenje bazne sredine koja daje racemizaciju biva eliminisano.ZR (D-Phe) -Pro-Arg (Z) -lactam (III) where Z is the same as defined above, and R, Phe, Pro and Arg are the same as defined in the introductory part, so building a base environment which gives racemization is eliminated.

Dalje, pronalazak je baziran na saznanju da ako kompleks nagradjen sa litijum aluminijum hidridom,dobiven tokom redukcije zaštičenog tripeptid laktama formule III dobivenog kao što je opisano napred, se razlaže na takav način da se reakciona sredina dodaje u razblaženu,poželjno lN,hladnu (0-5°C) sumpornu kiselinu koriščenu u višku nasuprot publikovane Evropske patentne prijave br. 185 390 u kojoj se sumporna kiselina dodaje reakcionoj smeši,kiselost pH reakcione smeše se može osigurati. Stoga, racemizacija zaštidenog prdpeptid aldehida se može izbeči ili zantno smanjiti.Further, the invention is based on the knowledge that if a complex rewarded with lithium aluminum hydride, obtained during the reduction of the protected tripeptide elbows of formula III obtained as described above, is decomposed in such a way that the reaction medium is added to the diluted, preferably 1 N, cold (0 -5 ° C) sulfuric acid used in excess in contrast to published European patent application no. 185 390 in which sulfuric acid is added to the reaction mixture, the acidity of the pH of the reaction mixture can be ensured. Therefore, racemization of the protected prdpeptide aldehyde can be avoided or significantly reduced.

vv

Pronalazak je baziran na daljem saznanju da hidrogenoliza tripeptid aledhida formule II dobivenog kao što je opisano napred se mora izvesti u prisustvu viška sumporne kiseline na niskoj temperaturi ispod 10°C,poželjno na 6-b°C.The invention is based on the further knowledge that the hydrogenolysis of the tripeptide aledhyde of formula II obtained as described above must be carried out in the presence of excess sulfuric acid at a low temperature below 10 ° C, preferably at 6-b ° C.

Prema našim eksperimentalnim podacima, ako se hidrogenoliza. Z-D-Phe-PrO-Arg(Z)-H izvodi na raznim temperaturma u prisustvu 1 molarnog ekvivalenta sumporne kiseline, nečistoče detektabilne pomoču tanko-slojno hromatografske-.analize tako dobivenog proizvoda su sledeče: 17% na 40°C, 10% na sobnoj temperaturi (20-25°C 4% na 6-10°C. D-L-D izomer sadržaji proizvoda detektibilnog pomoču HPLC su kao što sledi: 12%,5% i 2-3%,respektivno,tj. ukupni sadržaj nečistoča u proizvodu je bio 29%,15% i 6-7%,respektivno. Ovo znači da ako se hidrogenoliza izvodi na nižim temperaturama,količina sporednih proizvoda znatno opada dok vreme potrebno za hidrogenolizu se znatno ne uvečava pri smanjenju temperature.According to our experimental data, if hydrogenolysis. ZD-Phe-PrO-Arg (Z) -H is carried out at various temperatures in the presence of 1 molar equivalent of sulfuric acid, the impurities detectable by thin-layer chromatographic analysis of the product thus obtained are as follows: 17% at 40 ° C, 10% at room temperature (20-25 ° C 4% at 6-10 ° C. DLD isomer contents of HPLC detectable product are as follows: 12%, 5% and 2-3%, respectively, ie the total impurity content of the product is This means that if the hydrogenolysis is carried out at lower temperatures, the amount of by-products decreases significantly while the time required for the hydrogenolysis is not significantly increased as the temperature decreases.

6.6.

Ako se hidrogenoliza izvodi na nižim temperaturama u prisustvu viška sumporne kiseline,dalji veliki napredak nastaje tako da gradjenje sporednog proizvoda koji ima vrednost od 0,39-0,44 može biti znatno suzbijeno i tačna- detekcija krajnje tačke reakcije takodje se eliminiše. Prema našim eksperimentima ako se hidrogenoliza Z-D-Phe Pro-Arg(Z)-H izvodi u prisustvu 1,5-1,7 molarnih ekvivalenata sumporne kiseline u tetrahidrofuranu na temperaturi od 6-8°C, sporedni proizvod koji ima gornju R^ vrednost se gradi samo u tragovima čak posle 1 Časa prehidracije .If hydrogenolysis is carried out at lower temperatures in the presence of excess sulfuric acid, further great progress is made so that the construction of a by-product having a value of 0.39-0.44 can be substantially suppressed and accurate detection of the reaction endpoint is also eliminated. According to our experiments, if the hydrogenolysis of ZD-Phe Pro-Arg (Z) -H is carried out in the presence of 1.5-1.7 molar equivalents of sulfuric acid in tetrahydrofuran at a temperature of 6-8 ° C, a by-product having an upper R ^ value builds only in traces even after 1 hour of overtaking.

Dalje, poželjno je koriščenje sumporne kiseline u toku svih stupnjeva postupka tako ako se npr. koristi HCl,sulfatna so može biti zagadjena sa hloridnim jonima.Further, it is desirable to use sulfuric acid throughout all stages of the process so that e.g. uses HCl, the sulfate salt can be contaminated with chloride ions.

Kao rezultat izvodjenja reakcije kao što je opisano ovde,količina DLD izomera u krajnjem proizvodu formule I je najviše 2-4%,dok se drugi zagadjicači (tripeptid kiselina i -alkohol) grade u količini ispod 1%.As a result of the reaction as described herein, the amount of DLD isomers in the final product of formula I is at most 2-4%, while other contaminants (tripeptide acid and -alcohol) are built up in an amount below 1%.

Bazirano na gornjem,pronalazak se odnosi na poboljšan postupak za dobivanje tripeptid aldehida formule I, gde R,Phe,Pro i Arg su isti k< što je definisano napred,u farmaceutski čistom obliku, kondenzacijom laktama formule IV,gde Arg je kao što je opisano napred a Z označava benziloksikarbonil,sa dipeptidom formule V,gde R,Z,Phe i Pro su kao što je definisano napred u uvodnom delu i Z je isto kao što je definisano napred,preko mešanog anhidrida,redukciju tripeptid laktama formule III,gde R,Z,Phe,Pro i Arg su isti kao što je definisano napred,sa litijum aluminijum hidridom i hidrolize tako dobivenog 'zaštičenog tripeptid aldehida formule II,gde R,Z,Phe, i Arg su isti kao što je definisano napred u prisustvu sumporne kiseline, koji obuhvataBased on the above, the invention relates to an improved process for the preparation of a tripeptide aldehyde of formula I, wherein R, Phe, Pro and Arg are the same as defined above, in pharmaceutically pure form, by condensation of the elbows of formula IV, wherein Arg is as is described above and Z denotes benzyloxycarbonyl, with a dipeptide of formula V, wherein R, Z, Phe and Pro are as defined above in the introductory part and Z is the same as defined above, via mixed anhydride, reduction of the tripeptide lactams of formula III, where R, Z, Phe, Pro and Arg are the same as defined above, with lithium aluminum hydride and hydrolysis of the thus obtained 'protected tripeptide aldehyde of formula II, where R, Z, Phe, and Arg are the same as defined above in the presence of sulfuric acid, which includes

GMr

a..) oslobadjanje N -zašzičenog L-araginin laktama in situ u toku *- G kondenzacije N -zaštičenog L-arginin laktam hidrohlorida formulea ..) release of N-protected L-araginin lactam in situ during * - G condensation of N-protected L-arginine lactam hydrochloride of the formula

IV, gde Z je isto kao što je definisano napred, i dipeptida formuleIV, wherein Z is the same as defined above, of the dipeptide of the formula

V, gde R,Z,Phe i Pro su isti kao što je definisano napred,u mešani anhidrid u reakcionoj smeši zatim dodavanjem baze u smešu pomenutih komponenti,featim redukciju tako dobivenog zaštičenog tripeptid laktama formule III gde R,Z,Phe,Pro i Arg su isti kao što je definisano napred,razlaganje tako nagradjenog kompleksa dodavanjem reakcione smeše u višak IN sumporne kiseline na temperaturi od 0-5°C, zatim izvod jenje hidrogenolize zaštičenog tripeptida formule II, gde R,Z,Phe,Pro i Arg su isti kao što je definisano napred na temperaturi ispod 10°C u prisustvu 1-2 molarna ekvivalenta sumporne kiseline ,ili a2) posle redukcije tako dobivenog zaštičenog tripeptid laktama formule III, gde R, Z,Phe,.Pro i Arg su isti kao što je definisano napre razlaganje tako nagradjenog kompleksa dodavanjem reakcione smeše u višak IN H2SO^ na temperaturi od 0-5°C, zatim izvodjenje hidrogenoliz tako dobivenog zaštičenog tripeptida formule II, gde R,Z,Phe,Pro i Ar su isti kao što je definisano napred, na temperaturi ispod 10°C u prisustvu l-2molarnih ekvivalenata H~SO . ili z 4 a^) izvodjenje hidrogenolize zaštičenog tripeptida formule II, gde R, Phe,Pro i Arg su isti kao što je definisano napred,na temperaturi . ispod 10°C u prisustvu l-2molarna ekvivalenta H2SO^.V, where R, Z, Phe, and Pro are the same as defined above, to the mixed anhydride in the reaction mixture then adding a base to the mixture of said components, featim reduction of the thus obtained protected tripeptide elbows of formula III where R, Z, Phe, Pro and Arg are the same as defined above, decomposing the complex thus rewarded by adding the reaction mixture to excess IN sulfuric acid at a temperature of 0-5 ° C, then performing the hydrogenolysis of the protected tripeptide of formula II, where R, Z, Phe, Pro and Arg are the same as defined above at a temperature below 10 ° C in the presence of 1-2 molar equivalent of sulfuric acid, or a 2 ) after reduction of the thus obtained protected tripeptide elbows of formula III, where R, Z, Phe, Pro and Arg are the same as which is defined by decomposing the complex thus rewarded by adding the reaction mixture to excess INH 2 SO 4 at a temperature of 0-5 ° C, then performing the hydrogenolysis of the thus obtained protected tripeptide of formula II, where R, Z, Phe, Pro and Ar are the same as what is the def initiated at a temperature below 10 ° C in the presence of 1-2 molar equivalents of H ~ SO. or z 4 a ^) performing the hydrogenolysis of a protected tripeptide of formula II, wherein R, Phe, Pro and Arg are the same as defined above, at temperature. below 10 ° C in the presence of l-2molar equivalent of H 2 SO ^.

Prema predmetnom pronalsku,reakcija se poželjno izvodi kao što sledi:According to the present invention, the reaction is preferably carried out as follows:

GMr

Iz t-butoksikarbonil-N -benziloksikarbonil-L-arginin lattamaFrom t-butoxycarbonyl-N-benzyloxycarbonyl-L-arginine lattam

G_ t-butoksikarbonil zaštitna grupa se uklanja na poznat način. N benzilkarbonil-L-arginin laktam hidrohlorid:formule IV tako dobiven se drži u dimetil formamidnom rastvoru na temperaturi od -lb do -20°C.zatim se ovaj rastvor doda u mešan anhidrid nagradjen iz dipeptida formule V (benziloksikarbonil-D-fenilalanil-L-prolin ili N-metil-N-benziloksikarbonil-D-fenilalanil-L-prolin) i izobutil estra hlorokarbonske kiseline. Baza,poželjno trimetil amin se zatim dodaje reakcionoj smeši. Pod ovim sulovima, laktam os lobod jen in situ usled efekta baze,reaguje odjednom sa mešanim anhidridom radi gradjenja zaštičenog tripeptid .laktama, i tako gradjenje bazne sredine koja izaziva racemizaciju može biti izbegnuto. Ako se želi, proizvod tako dobiven se može prečistiti brzom filtracijom kroz sloj silika gela. Izborom gornje sekvence operacija,koja jeThe G_ t-butoxycarbonyl protecting group is removed in a known manner. N benzylcarbonyl-L-arginine lactam hydrochloride: Formula IV thus obtained is held in dimethyl formamide solution at a temperature of -1b to -20 ° C. Then this solution is added to a mixed anhydride rewarded with a dipeptide of formula V (benzyloxycarbonyl-D-phenylalanil- L-proline or N-methyl-N-benzyloxycarbonyl-D-phenylalanyl-L-proline) and chlorocarboxylic acid isobutyl ester. The base, preferably trimethyl amine, is then added to the reaction mixture. Under these sulums, the lactam os swan is in situ due to the effect of the base, reacts at once with mixed anhydride to build a protected tripeptide. Elbows, and thus the construction of a base environment that causes racemization can be avoided. If desired, the product thus obtained can be purified by rapid filtration through a pad of silica gel. By choosing the above sequence of operations, which is

8.8.

različita od pne iz prethodne tehnike,nema potrebe za skupim prečišča vanjem zaštičenog tripeptid laktama hromatografijom na koloni.different from the BC from the prior art, there is no need for expensive purification by tripeptide elbow protected by column chromatography.

Zaštičen tripeptid laktam formule III tako dobiven se redukuje sa Jitijum aliminijum hidridom u suvom tetrahidrofuranu. Kompleks tako dobiven se razlaže->na.. suprot publikovanoj Evropskoj patentno j prijavi br. 185 390 dodavanjem reakcione smeše u razblažen rastvor ,poželjno IN Η2θ°4 k°ri^en u višku uz hladjenje na temperaturi od 2-4°C. Krajnja pH vrednost od 2-3 se podešava po izboru dodatkom I^SO^. Zatim se reakciona smeša preradjuje na poznat način. Zaštičen tripeptid aldehid formule II tako dobiven se prečiščava filtriranjem kroz sloj silika gela.The protected lactam protected tripeptide of formula III thus obtained is reduced with Jitium aluminum hydride in dry tetrahydrofuran. The complex thus obtained is decomposed-> against .. published European Patent Application no. 185 390 by adding the reaction mixture to the diluted solution, preferably IN Η 2 θ ° 4 k ° r and ^ en in excess with cooling at 2-4 ° C. The final pH value of 2-3 is optionally adjusted by the addition of I ^ SO ^. The reaction mixture is then processed in a known manner. The protected tripeptide aldehyde of formula II thus obtained is purified by filtration through a layer of silica gel.

Hidr.ogenoliza se. požel jno izvodi u polarnom organskom rastvaraču, poželjno tetrahidrofuran ili niži alkanol,npr. metanol,etanol, i-propanol, poželjno u etanolu. Poželjno je ako se hidrogenoliza ne izvodi u zatvorenom sistemu,kvečbarbotiranjem vodonika kroz reakcionu smešu. Praktično vodonični gas se barbotira kroz sistem u fino izdeljenim obliku što se može obezbediti uvodjnjem gasa kroz Gj filter.Hydrogenolysis is. preferably carried out in a polar organic solvent, preferably tetrahydrofuran or lower alkanol, e.g. methanol, ethanol, i-propanol, preferably in ethanol. It is preferable that hydrogenolysis is not carried out in a closed system,kby bubbling hydrogen through the reaction mixture. Practically hydrogen gas is bubbled through the system in a finely divided form which can be provided by introducing gas through Gj filter.

Prema poželjnoj realizaciji postupka, zaštičen tripeptid .-aldehid formule II podesne čistoče tako dobiven se rastvara u tetrahidrofuranu i tako dobiven rastvor se dodaje u ohladjenu vodenu katalitičk suspenziju koja obuhvata 1,5 -1,7 molarnih ekvivalenata IN I^SO^· Odnos organskog rastvarača prema vodenoj frakciji je 70-50 : 30-50, poželjno 60:40. Kao katalizator, pože?10-30% mas. 10% paladijuma na uglju ili paladijuma je koriščeno.Hidrogenizacija se izvodi pod hladjenjem na temperaturi od 6-8°C barbotiranjem fino izdeljenog vodoničnog gasa kroz sistem. Napredovanje reakcije se prati pomoču tanko-slojno toromatografske analize.,According to a preferred embodiment of the process, the protected tripeptide.-Aldehyde of formula II of suitable purity is thus dissolved in tetrahydrofuran and the solution thus obtained is added to the cooled aqueous catalytic suspension comprising 1.5 -1.7 molar equivalents IN I ^ SO ^ · Organic ratio of the solvent to the aqueous fraction is 70-50: 30-50, preferably 60:40. As a catalyst, it burns? 10-30% wt. 10% of palladium on coal or palladium is used. Hydrogenation is carried out under cooling at 6-8 ° C by bubbling fine hydrogen gas through the system. The progress of the reaction is monitored by thin-layer toromatographic analysis.,

Prema drugoj poželjnoj realizaciji postupka pronalska,zaštičen tripeptid aldehid koriščen kao polazni materijal se rastvara u tetrahidrofuranu i katalizator koji obuhvata 10% pladijuma staloženog na barijumsulfatu ili alumimi jumi.oksidu kao nosaču, poželjno barijum sulfatu se koristi.According to another preferred embodiment of the method of the invention, the protected tripeptide aldehyde used as starting material is dissolved in tetrahydrofuran and a catalyst comprising 10% of the plarium deposited on barium sulfate or alum alum as the carrier, preferably barium sulfate is used.

Hidrogenizacija se izvodi na temperaturi od 6-8°C u prisustvu 1,5 molarnog ekvivalenta H2SO4 barbotiranjem fino izdeljenog vodoničnog gasa kroz sistem. Kraj reakcije se prati tanko-slojnom hromatografskon analizom.The hydrogenation is carried out at a temperature of 6-8 ° C in the presence of 1.5 molar equivalent of H2SO4 by bubbling fine hydrogen gas through the system. The end of the reaction is monitored by thin layer chromatographic analysis.

Prema daljej poželjnoj realizaciji postupka pronalska,zaštičen tripeptid koriščen kao polazni materijal se rastvara u etanolu, zatim se rastvor dodaje u ohladjenu suspenziju koja obuhvata 10% paladijum na uglju katalizatora i 1 molarni ekvivalent IN H-SO..According to a further preferred embodiment of the method of the invention, the protected tripeptide used as starting material is dissolved in ethanol, then the solution is added to a cooled suspension comprising 10% palladium on coal catalyst and 1 molar equivalent of IN H-SO ..

+4+4

Hidrogenizacija se izvodi na temperaturi od 6-8 C barbotiranjem fino iszdeljenog vodoničnog gasa kroz sistem i postupak se prati tanko-slojnom hromatografijom.Hydrogenation is carried out at 6-8 C by bubbling fine hydrogen gas through the system and the process is followed by thin layer chromatography.

vv

Proizvod može biti jednostavno izdvojen iz reakcione smeše filtriranje katalizatora i uparavanjem organskog rastvarača iz vodeno-organske smeše rastvarača na temperaturi ispod 40°c,poželjno 25-30°C, zatim suvim-zamrzavenjem vodenog rastvora direktno ili posle podešavanja pH na oko 4. pH se poželjno podešava koriščenjem jono-izmenjivačke smole hidroksi-faze ili koriščenjem O,1N H2SO4.The product can be simply separated from the reaction mixture by filtering the catalyst and evaporating the organic solvent from the aqueous-organic solvent mixture at a temperature below 40 ° C, preferably 25-30 ° C, then freezing the aqueous solution directly or after adjusting the pH to about 4. pH is preferably adjusted by the use of a hydroxy-phase ion exchange resin or by the use of O, 1N H2SO4.

Kada se postupak prema pronalsku izvodi na pilot postrojenju, maksimalno zagadjenje proizvoda tako dobivenog (D-fenilalanil-Lprolil-L-raginin aldehid sulfata i N-metil-D-fenilalanil-L-prolilL-arginin aldehid sulafata) detekabilno pomoču tanko-slojno hromatogarfske analize je najviše l%,dok D-L-D izmoreni njegov sadržaj detektabilan pomoču HPLC je najviše 2-4%. Tako ukupna količina nečistoča može biti smanjena na oko 3-5%,što je u saglasnosti sa zahtevima idatim za farmaceutske susptance i suprotno sadržaju nečistoča od 15-25% u slučaju požnatih postupaka.When the process according to the invention is carried out on a pilot plant, maximum contamination of the product thus obtained (D-phenylalanil-L-propyl-L-raginine aldehyde sulfate and N-methyl-D-phenylalanyl-L-prolyl-L-arginine aldehyde sulphate) is detectable by thin-layer chromatogarf analysis is at most l%, while DLD has its content detectable by HPLC is at most 2-4%. Thus, the total amount of impurities can be reduced to about 3-5%, which is in accordance with the requirements for pharmaceutical suspensions and contrary to the impurity content of 15-25% in the case of lean processes.

Postupak predmetnog pronalska je dalje ilustrovan sledečim ne-ograničavajučim primerima.The process of the present invention is further illustrated by the following non-limiting examples.

Rf vrednosti su odredjene tanko-sljnom hromatografijom na silika gelu (Kieselgel G,Reanal,Budapest) koriščenjem eluenstkih smeša datih u primerima. Razvijač: hlorinovane hromatografske ploče su tretirane s 0-tolidnim rastvorom (2,5g o-tolidina i lOml sirčetne kiseline rastvorenogu 500 ml vode) posle sušenja .R f values were determined by flash silica chromatography on silica gel (Kieselgel G, Reanal, Budapest) using the eluent mixtures given in the examples. Developer: Chlorinated chromatographic plates were treated with a 0-tolide solution (2.5 g o-tolidine and 10 ml acetic acid dissolved in 500 ml water) after drying.

PRIMER 1EXAMPLE 1

Dobivanje D-fenilalanil-L-prolil-L-arganin aldehid sulfataPreparation of D-Phenylalanil-L-prolyl-L-arganine aldehyde sulfate

GMr

201g (0,3 mola) benziloksikarbonil-D-fenilalanil-L-prolil-N banziloksikarbonil-L-arginin aldehida se rastvori u 2 litra tetrahidrofurana na sobnoj temperaturi. Istovremeno se 60g 10% paladijuma na uglju suspenduje u 0,6 litra dejonizovane vode,zatim se doda 900ml I^SO^ (0,45mola). Suspenzija koja obuhvata katalizator se ohladi do temperature od 2-50°C, i tetrahidrofuranski rastvor zaštičenog tripeptid aldehida i dodatnih o,21itra dejonizovane vode se doda uz mešanje. Zatim se vodonik barbotira kroz smešu čija se temperatura održava na 6-8°C uz mešanje.201g (0.3 mol) of benzyloxycarbonyl-D-phenylalanyl-L-prolyl-N-benzyloxycarbonyl-L-arginine aldehyde was dissolved in 2 liters of tetrahydrofuran at room temperature. At the same time, 60 g of 10% palladium-on-coal are suspended in 0.6 liters of deionized water, then 900 ml of 1 SO 2 (0.45 mol) is added. The suspension comprising the catalyst was cooled to 2-50 ° C, and a tetrahydrofuran solution of the protected tripeptide aldehyde and additional about 21 liters of deionized water was added with stirring. The hydrogen is then bubbled through a mixture whose temperature is maintained at 6-8 ° C with stirring.

Napredovanje reakcije se.prati pomoču tanko-slojne hromatografske analize koriščenjem 60:20:6:11 smeše etil acetat/piridin/airčetna kiselina/voda kao eluenta. (R^ vrednosti polaznih materijala,intermed jera i krajnjeg proizvoda su 0,92-0,96, 0,38-0,44 i 0,0-0,10, respektivno).The progress of the reaction is followed by thin layer chromatographic analysis using a 60: 20: 6: 11 ethyl acetate / pyridine / acetic acid / water mixture as eluent. (R ^ values of starting materials, intermediate and end product are 0.92-0.96, 0.38-0.44 and 0.0-0.10, respectively).

vv

Reakcija se zsrvršava za 3-8 časa. Na kraju reakcije,katalizator se odfiltrira i ispere 3 puta sa po lOOml dejonizovane vode. Filtrat i tečnost od ispiranja se sjedine,zatim se odestiluje tetrahidrofuran u rotirajučem uparivaču pod vakumom na temperaturi od 25-30°C.The reaction is complete for 3-8 hours. At the end of the reaction, the catalyst was filtered off and washed 3 times with 100 ml deionized water each. The filtrate and the rinsing liquid are combined, then distilled off with tetrahydrofuran in a rotary evaporator under vacuum at a temperature of 25-30 ° C.

Preostali vodeni rastvor se ekstrahuje sa 2xl00ml dihlorometana, zatim se pH vodene faze kontroliše. Ako se pH razlikuje od 4,tada se pH podesi na 4 dodatkom 0,lN H^SO^ ili OH -ciklirajuče jono-izmenjivačke smole (npr. AG 1x2).The remaining aqueous solution was extracted with 2x100 ml of dichloromethane, then the pH of the aqueous phase was controlled. If the pH differs from 4, then the pH is adjusted to 4 by the addition of 0, 1 N H 2 SO 4 or OH-cyclic ion exchange resins (eg AG 1x2).

Zapremina rastvora se dopuni do 1,5 litara dodavanjem dejonizovane vode,zatim se rastvor suvo smrzne. Tako se dobiva 125g (83,2%) željenog proizvoda.The volume of the solution is made up to 1.5 liters by the addition of deionized water, then the solution is freeze-dried. This gives 125g (83.2%) of the desired product.

Rf=0,52-0,57 (etilacetat/piridin/sirčetna kiselina/voda=25:20:6:11).Rf = 0.52-0.57 (ethyl acetate / pyridine / acetic acid / water = 25: 20: 6: 11).

/a/ ,20 / A /d =-117° (c=l,voda) ./ a /, 20 / A / d = -117 ° (c = 1, water).

Ukupni sadržaj nečistoča prema tanko—slojnoj hromatografskojTotal impurity content by thin-layer chromatography

11.11.

analizi: 3-5%, dok D-L-D izomerni sadržaj odredjen pomoču HPLC je oko 2-3%.analysis: 3-5%, while the D-L-D isomeric content determined by HPLC is about 2-3%.

GMr

Benziloksikarbonil-D-fenilalanil-L-lprolin-N -benziloksikarbonil-Larginin aldehid koriščen kao polazni materijal može se dobiti kao što sledi:Benzyloxycarbonyl-D-phenylalanyl-L-lproline-N-benzyloxycarbonyl-Larginine aldehyde used as starting material can be obtained as follows:

Stupanj 1Level 1

GMr

Benzilokaikarbonil-D-fenilalanii-prolil-N -benzioloksikarbonilL-arginin laktamBenzylocarbonyl-D-phenylalanyl-prolyl-N-benzyloxycarbonylL-arginine lactam

GMr

429,5g (1,1 mola) t-butoksikarbonil-N -benziloksikarbonil-arginin iaktama (publikovana Evropska patentna prijava br. 185 390, je suspendovano u 1300ml suvog hloroforma. Zatim se ukapavanjem uz mešanje dodaje l300ml lb9g/100ml (oko 5N, hidrohlorid etil acetata i uz hladjenje ledenom vodom pri brzini koja obezbedjuje izbegavanje porasta temperature iznad 15°C. Ubrzo odpočinje rastvaranje i taloženje kristalne supstance. Suspenzija se meša na sobnoj temperatu ri 3 časa, zatim se razblaži sa 3000ml suve 1:1 smeše etra i etil acetata. Staložena kristalna supstance se odfiltrira,ispere sa 2x1000 ml acetona i 5ooml etra, zatim se osuši iznad čvrstog kalijum hidroksida i fosfor pentoksida u vakumskom eksikatoru.429.5g (1.1 mol) of t-butoxycarbonyl-N-benzyloxycarbonyl-arginine actam (European Patent Application Publication No. 185 390, suspended in 1300ml of dry chloroform) Then l300ml of lb9g / 100ml (about 5N) was added dropwise. ethyl acetate hydrochloride and cooled with ice water at a rate that avoids temperature rise above 15 ° C. The dissolution and precipitation of the crystalline substance begins shortly. The suspension is stirred at room temperature for 3 hours, then diluted with 3000 ml of dry 1: 1 ether mixture and The crystalline solids were filtered off, washed with 2x1000 ml acetone and 5 [mu] l ether, then dried over solid potassium hydroxide and phosphorus pentoxide in a vacuum desiccator.

GMr

Posle oko 1 časa sušenja, N -benziloksikarbonil-L-arginin-laktam hidrohlorid se rastvori u lOOOml suvog dimetil formamida, ohladi se do temperature od -15° do -20°C i doda se mešanom anhidridu dobivenom kao što s\edl:After about 1 hour of drying, the N-benzyloxycarbonyl-L-arginine-lactam hydrochloride was dissolved in 100 ml of dry dimethyl formamide, cooled to -15 ° C and -20 ° C, and added to the mixed anhydride obtained as in ED:

306g (1 mol) N-benziloksikarbonil-D-fenilalanil-L-prolina (Nicolaides E. et al: J.Med.Chem. 11, 74 (1968) i,,publikovana Evropska patentna prijava br. 185 396) se rastvori u 1000 ml anhidrovanog dimetil foraamida i doda se lllml (1 mol) N-metil morfolina. Zatim se smeša ohladi do temperature od -15°C ukapavanjem se doda 132ml (lmol) izobutil estra..hlorokarbonske kiseline na istoj temperaturi uz mešanje 5-10minuta. Mešani anhidrid se ohladi do temperature od -20 C do -2b°C posle 10 minuta mešanja i sjedini se sa dimetil306g (1 mol) of N-benzyloxycarbonyl-D-phenylalanil-L-proline (Nicolaides E. et al: J.Med.Chem. 11, 74 (1968) and European Patent Application Publication No. 185 396) are dissolved in 1000 ml of anhydrous dimethyl foraamide and 11 ml (1 mol) of N-methyl morpholine are added. The mixture was then cooled to -15 [deg.] C. and 132 ml (1mol) of isobutyl ester of chlorocarboxylic acid were added dropwise at the same temperature with stirring for 5-10 minutes. The mixed anhydride was cooled to -20 C to -2b ° C after 10 minutes of stirring and combined with dimethyl

12.12.

Q foramidnim rastvorom N -benziloksikarbonil-L-arginin laktam nidrohlorida dobivenog napred. Zatim se ukapalzanjem doda 308ml (2,2ml) trietil amina reakcionoj smeši na istoj temperaturi tokom oko 3o minuta, suspenzija se tada meša dalji čas na temperaturi od -20 do -15°C. pH parnog prostora se kontroliše vlažnim pH-papirom: ako pH pada ispod 8, dodaje se dalja količina trietil amina. Zatim se smeša razblaži sa 2 litra benzena,staložene soli se odfiltriraju i isperu 2 puta sa po 500ml benzena.Q foramide solution of N -benzyloxycarbonyl-L-arginine lactam nitrochloride obtained above. Then 308ml (2.2ml) of triethyl amine was added dropwise to the reaction mixture at the same temperature for about 3 minutes, the suspension was then stirred for a further hour at -20 to -15 ° C. The pH of the vapor space is controlled by wet pH paper: if the pH drops below 8, a further amount of triethyl amine is added. The mixture is then diluted with 2 liters of benzene, the precipitated salts are filtered off and washed twice with 500 ml of benzene each.

U benzen-dimetil formamidni filtrat doda se 1,5 litar vode i faze se razdvoje. Vodeni dimetil formamidni sloj se ekstrahuje sa 2x500ml benzena. Sjedinjeni benzenski rastvori se isperu sa 2x0,5 litra vode, 0,5, 11-tra o,IN-H2S.O4 ,zatim sa 3x0,5 litra vode,osuše iznad anhidrova nog natrijum sulfata i upare do 2 litra pod vakumom na temperaturi od najviše 40°C.To the benzene dimethyl formamide filtrate was added 1.5 liters of water and the phases were separated. The aqueous dimethyl formamide layer was extracted with 2x500ml of benzene. The combined benzene solutions were washed with 2x0.5 liters of water, 0.5, 11 tra, IN-H 2 SO 4 , then with 3x0.5 liters of water, dried over anhydrous sodium sulfate and evaporated to 2 liters under vacuum at maximum temperature of 40 ° C.

360g Kieselgel_G adsorbensa se suspenduje u benzen i formira se filterski sloj,gde je odnos prečnika prema višini 8:1 do 4:1. Benzenski rastvor se isisa kroz fltferski sloj pod slabim vakumom, zatim se filterski sloj ispere sa 4,8 litara benzena na isti način, Sjedinjeni benzenski rastvori se koncentruju do oko 600ml zapremine pod vakumom na temperaturi od najviše 40°C, zatim se uz intezivno mešanje doda 31itra diizopropil etra.360g of Kieselgel_G adsorbent is suspended in benzene and a filter layer is formed, where the diameter to height ratio is 8: 1 to 4: 1. The benzene solution is aspirated through a flatter layer under low vacuum, then the filter layer is washed with 4.8 liters of benzene in the same way, the combined benzene solutions are concentrated to about 600ml volume under vacuum at a temperature of up to 40 ° C, then with vigorous stirring added 31 liters of diisopropyl ether.

Talog< se odflltrira, ispere sa 2x600 ml diizopropil etra i osuši u vakumskom ek sikatoru iznad Ρ2 ος 1 parafinskih ljuspica. Tako se dobiva 5l0g (76%) željenog proizvoda. Ukupan sadržaj zagadjivača proizvoda odred jeijppmodu Stanko-s lojne hromatografij© je 1-2%.The precipitate was filtered off, washed with 2x600 ml of diisopropyl ether and dried in a vacuum desiccator above Ρ 2 ο ς 1 paraffin flakes. In this way 5g (76%) of the desired product is obtained. The total content of the contaminant of the product is determined by the Stanko-sebaceous Chromatography © is 1-2%.

Rf= 0,55 -0,65 (etil acetat) (Rf vrednost L-D-L laktama je 0,45-0,50 u etil acetatu).Rf = 0.55-0.65 (ethyl acetate) (Rf value of L-D-L lactams is 0.45-0.50 in ethyl acetate).

/0Č/ - -55,8° (c=l,tetrahidrofuran).(0H) - -55.8 ° (c = 1, tetrahydrofuran).

DD

Stpanj 2Level 2

GMr

Benziloksikarbonil-D-fenilalanil-L-propil-N -benziloksikarbonilL-arginin aldehid .Benzyloxycarbonyl-D-phenylalanyl-L-propyl-N-benzyloxycarbonyl-L-arginine aldehyde.

300mg (0,45 mola) zaštičenog tripeptid laktama (Primer 1,stupanj 1) se rastvori u 2,5 litra anhidrovanog tetrahidrofurana ohladjenog do temperature od -5°C. Rastvor se ohladi do temperature od -20°C do -25°C u kupatilu suvi led/aceton, i i uz jako mešanje tokom 20-25 minu+a doda se rastvor litijum aluminijum hidrida i tetrahidrofurana, koji ima koncentraciju od oko 0,7 mola/litar,što odgovara 0,375 mola litijum aluminijum hidrida. Napredovanje reakcije se prati pomoču tanko-slojne hromatografije koriščenjem 240:20:6:11 smeše etil acetat/piridn/airčetna kiselina/voda kao eluenta. U slučaju potrebe,dalja količina litijum aluminijum hidrid* nog rastvora se doda dok ne nestane mrlja koja ima Rf vrednost od 0,75-0,80,koja odgovara laktamu.300 mg (0.45 mol) of protected tripeptide lactam (Example 1, step 1) was dissolved in 2.5 liters of anhydrous tetrahydrofuran cooled to -5 ° C. The solution was cooled to -20 ° C to -25 ° C in a dry ice / acetone bath, and stirred vigorously for 20-25 min + and a solution of lithium aluminum hydride and tetrahydrofuran was added, having a concentration of about 0.7 moles / liter, equivalent to 0.375 moles of lithium aluminum hydride. The progress of the reaction was monitored by thin layer chromatography using 240: 20: 6: 11 ethyl acetate / pyridine / acetic acid / water mixture as eluent. If necessary, a further amount of lithium aluminum hydride solution is added until a stain having an R f value of 0.75-0.80 corresponding to the lactam disappears.

Kada se reakcija zvrši,reakciona smeša se postepeno sipa u 3 litra IN H2S°4 rastvora na temperaturi od 2-3°C uz mešanje. Krajnja pH vrednost se podesi dcdavaa.4era.p0 izboru dalje količine i^SO^.When the reaction is complete, the reaction mixture is gradually poured into 3 liters of IN H2 S ° 4 solution at 2-3 ° C with stirring. The final pH value is adjusted to dcdavaa.4era.p0 to select a further amount and ^ SO ^.

Voda se dodaje u rastvor dok ovaj ne psotane mutan,tada se ekstrahuj sa 3x0,9 litara n-heksana. Izmedju dve ekstrakcije materijal se razdvaja kao uljana faza,stoga se homogenizuje ka tetrahidrofuranom, zatim zatim dobije izgled mleka dodatkom nešto vode. Vodena faza se ekstrahuje sa 2x21itara dihlorometana. Sjedinjeni dihlorometanski rastvori se isperu £ia 2x0, b litra 5% NaHCO^ rastvora na 4-8°C, zatim sa 2x0,5 litra destilovane vode na temperaturi od 4-8°C, osuši se iznad anhidrovanog natrijum sulfata i upari pod vakumom na temperaturi od najviše 40°C (oko 300g uljane supstance se dobiva)The water is added to the solution until it is cloudy, then extracted with 3x0.9 liters of n-hexane. Between the two extractions, the material is separated as an oily phase and is therefore homogenized to tetrahydrofuran, then obtained as milk by the addition of some water. The aqueous phase is extracted with 2x21 liters of dichloromethane. The combined dichloromethane solutions were washed with 2x0, b liters of 5% NaHCO4 solution at 4-8 ° C, then with 2x0.5 liters of distilled water at 4-8 ° C, dried over anhydrous sodium sulfate and evaporated in vacuo at a temperature of not more than 40 ° C (about 300g of oily substance is obtained)

Uljani ostatak se rastvori u 7:3 smeši dihlorometana i acetona, protokom kroz filterski sloj (prečnik:višini =5:1) dobiven iz 900g Kieselgel G adsorbensa koriščenjem 7:3 smeše dihlorimetana i acetona kao eluenta bez isisavanja, zatim se filterski sloj ispere sa 6 litara iste eluentske smeše. Postupak može da netraje duže od 20 minuta. Sjedinjeni filtrati se upare na oko 600ml na temperaturi od najviše 40°C, zatim se doda 1 litar benzena i rastvor se ponovo upari, zatim se proizvod staloži dodatkom 1,6 litara z LkJLoheksana uz mešanje. Talog se odfiltrira, ispere sa 2x0,3 litra cikloheksana i osuši u vakumskom eksikatoru na sobnoj temperaturi iznad parafinskih ljuspi. Tako se dobiva 240g (79,7%) jedinjenja iz naslova.The oily residue was dissolved in a 7: 3 mixture of dichloromethane and acetone, filtered through a filter layer (diameter: height = 5: 1) obtained from 900g of Kieselgel G adsorbent using a 7: 3 mixture of dichloromethane and acetone as eluent without suction, then the filter layer was washed with 6 liters of the same eluent mixture. The process may take more than 20 minutes. The combined filtrates were evaporated to about 600 ml at a temperature of up to 40 ° C, then 1 liter of benzene was added and the solution was re-evaporated, then the product was precipitated by adding 1.6 liters of LkJLhexane with stirring. The precipitate was filtered off, washed with 2x0.3 liters of cyclohexane and dried in a vacuum desiccator at room temperature above paraffin flakes. This gives 240g (79.7%) of the title compound.

14.14.

Rf =0,52-0,62 (etil acetat/piridin/sirčetna kiselina/voda =R f = 0.52-0.62 (ethyl acetate / pyridine / acetic acid / water =

240:20:6:11,.240: 20: 6: 11,.

Sadržaj nečistoče prema tanko-siojnoj hromatografskoj analizi je 0,5—% .The impurity content by thin-layer chromatographic analysis is 0.5%.

/= -0,8° (c=l,tetrahidrofuran).Δ = -0.8 ° (c = 1, tetrahydrofuran).

DD

PRIMER 2 kEXAMPLE 2 k

Dobivanje D-fenilalanin-L-prolil-L-arginin-aldehida sulfataPreparation of D-phenylalanine-L-prolyl-L-arginine aldehyde sulfate

QQ

20. Ig (0,03mola) benziloksikarbonil-D-fenilalaniirL-prolil-N benziloksikarbonil-L-arginin aldehida se rastvori u 214ml tetrahidrofurana i rastvor se ohladi do temperature—od 0°C. 4,3g paladijum na uglju katalizatora se suspenduje u 70ml dejonizovane vode i doda se 102ml IN I^SO^. Suspenzija katalizatora se ohladi do temperature od 2-5°C, vazduh se eliminiše pomoču gasovitog azota. Zatim se gornji tetrahidrofuranski rastvor doda u suspenziju uz mešanje i fino izdeljen vodonični gas se vodi u sistem. Temperatura se drži izmedju 6 i 8°c hladjenjem sa ledom. Napredovanje reakcije se kontroliše tanko-slojnom hromataografijom i sita eluenstka smeša se korosti kao što je opisano u primeru 1. Na kraju reakcije (oko 3 časa), reakciona smeša tako dobivena se obradjuje prema primeru 1. Prinos: 12,5g (83,2%) .20. The Ig (0.03 mol) benzyloxycarbonyl-D-phenylalanyl-1-prolyl-N benzyloxycarbonyl-L-arginine aldehyde is dissolved in 214 ml of tetrahydrofuran and the solution is cooled to a temperature of 0 ° C. 4.3g of palladium on coal catalyst is suspended in 70ml of deionized water and 102ml IN I ^ SO ^ is added. The catalyst suspension was cooled to 2-5 ° C, the air was eliminated with the help of gaseous nitrogen. The top tetrahydrofuran solution is then added to the suspension with stirring and fine hydrogen gas is introduced into the system. The temperature is kept between 6 and 8 ° C by cooling with ice. The progress of the reaction was monitored by thin layer chromatography and the eluent sieve mixture was crucible as described in Example 1. At the end of the reaction (about 3 hours), the reaction mixture thus obtained was treated according to Example 1. Yield: 12.5 g (83.2 %).

R^ =0,52-0,57(etilacetat/piridin/sirčetna kiselina/voda=25:20:6:11)Rf = 0.52-0.57 (ethyl acetate / pyridine / acetic acid / water = 25: 20: 6: 11)

- , /20 =-117°C (c=l,voda)-, / 20 = -117 ° C (c = 1, water)

Sadržaj nečistoča na bazi tanko-slojne hromatografske analizeje 3,5%. Sadržaj D-L-D izomera na bazi HPLC analize je 1,5%.The impurity content of thin-layer chromatographic analysis is 3.5%. The content of D-L-D isomers based on HPLC analysis is 1.5%.

PRIMER 3EXAMPLE 3

Dobivanje D-fenilalanil-L-prolil-L-arginin aldehid sulfataPreparation of D-Phenylalanil-L-prolyl-L-arginine aldehyde sulfate

15.15.

GMr

201g (0,3 mola) benziloksikarbonil-D-fenilalanil-L-prolil-N benziloksikarbonil-L-arginin aldehida se rastvori u 2 litra etandla na sobnoj temperaturi. 60g katalizatora koji obuhvata 10% paladijuma na barijum sulfatu kao nosaču se suspenduje u 0,6 litara dejonizovane vode i doda se 600m IN H SO (0,3 mola). Suspenzija se ohladi do temperature od 2-5°C i etanolni rastvor zaštičenog tripeptid aldehida se doda. Zatim se doda dejonizovana voda u količini koja odgovara 6:4 odnosu rastvarača prema vodenoj fazi.201g (0.3 mol) of benzyloxycarbonyl-D-phenylalanyl-L-prolyl-N benzyloxycarbonyl-L-arginine aldehyde was dissolved in 2 liters of ethanol at room temperature. 60g of catalyst comprising 10% palladium on barium sulphate as a carrier was suspended in 0.6 liters of deionized water and 600m INH SO (0.3 mol) was added. The suspension was cooled to 2-5 ° C and ethanolic solution of the protected tripeptide aldehyde was added. Deionized water is then added in an amount corresponding to a 6: 4 ratio of solvent to aqueous phase.

Zatim se barbotira vodonični gas kroz smešu uz mešanje i hladjenje na temperaturi od 6-8° C. Napredovanje hidrogenizacije se prati tanko-slojno, hromatografijom prema primeru 1. Pri kraju reakcije (oko 3-4 časa) katalizator se odfiltrira i ispere sa dejonizovanom vodom više puta. Filtrai se sjedine i alkohol se upari na rotirajučem isparivaču na temperaturi od 25-30°C. Vodeni rastvor koji ima pH od oko 3-4,se direktno suvo zamrzne. Tako se dobiva 10lg (65%) željenog proizvoda u obliku monohidrata,koji ima isti kvalietfet kao i proizvod dobiven u primeru 1.Hydrogen gas is then bubbled through the mixture with stirring and cooling at 6-8 ° C. The progress of hydrogenation is followed by thin-layer chromatography according to Example 1. At the end of the reaction (about 3-4 hours), the catalyst is filtered off and washed with deionized. water several times. The filters were combined and the alcohol was evaporated on a rotary evaporator at a temperature of 25-30 ° C. An aqueous solution having a pH of about 3-4 is directly freeze-dried. 10g (65%) of the desired product is obtained in the form of monohydrate, which has the same qualietfet as the product obtained in example 1.

ss

PRIMER 4EXAMPLE 4

Dobivanje D-fenilalanil-L-prolil-L-arginin aldehid sulfataPreparation of D-Phenylalanil-L-prolyl-L-arginine aldehyde sulfate

Prčen je postupak iz primera 3 izuzev što je 43cj 10% paladijum na uglju katalizatora,prethodno ispirano do neutralizacije i zatim koriščeno kao katalizator.The procedure of Example 3 was followed except that 43cj was 10% palladium on coal catalyst, previously rinsed to neutralization and then used as catalyst.

Tako se dobiva 125,lg (83,2%) željenog proizvoda koji ima isti kvalitet kao proizvod iz primera 1.This gives 125, lg (83.2%) of the desired product having the same quality as the product of Example 1.

PRIMER 5EXAMPLE 5

Dobivanje N-metil-D-fenilalanil-L-prolil-L-arginin aldehid sulfataPreparation of N-methyl-D-phenylalanyl-L-prolyl-L-arginine aldehyde sulfate

2u,5g (0,03 mola) N-benziloksikarbonil-N-metil-D-fenilalanil-LG prolil-N -bnnziloksikarbonil-L-arginin aldehida se rastvori u 214ml etanola, tada se doda HOml dejonizovane vode, 60ml IN υ4 .2u, 5g (0.03 mol) of N-benzyloxycarbonyl-N-methyl-D-phenylalanyl-LG prolyl-N-benzyloxycarbonyl-L-arginine aldehyde was dissolved in 214ml of ethanol, then HOml of deionized water was added, 60ml of IN υ 4.

(0,03 mola) i 3g 10% paladijuma na uglju kao katalizatora. Zatim se fino izdeljen gas uvodi u smešu uz hladjenje na temperaturi od 6-8°C. Napredovanje reakcije se prati tanko-slojnom hromatografijom koriščenjem smeše 25:20:6:1 etilacetat/piridin/sirčetne kiselina/vod< kao eluenta. Na hromatogramu vrednosti polaznerg materijala, intermedijera i krajnjeg proizvoda su oko 0,9, 0,7 i 0,4,repsektivno Reakcija se završava za oko 2 časa. Na kraju reakcije katalizator se odfiltrira i sipere sa 3x30ml dejonizovane vode. Filtrat i tečnost od sipiranja se sjedine,zatim se upare na rotirajučem isparivaču do oko lOOml na temperaturi od najviše 25°C,ostatak se zatim ekstrahuje sa 2x50ml dihlorometana.(0.03 mol) and 3g of 10% palladium on coal as catalyst. Subsequently, the finely made gas is introduced into the mixture with cooling at 6-8 ° C. The progress of the reaction was monitored by thin layer chromatography using a mixture of 25: 20: 6: 1 ethyl acetate / pyridine / acetic acid / water <RTI ID = 0.0> eluent. On the chromatogram, the values of the starting material, intermediate and end product are about 0.9, 0.7 and 0.4, respectively. The reaction is completed in about 2 hours. At the end of the reaction, the catalyst was filtered off and washed with 3x30ml deionized water. The filtrate and the pouring liquid are combined, then evaporated on a rotary evaporator to about 100 ml at a temperature of not more than 25 ° C, the residue is then extracted with 2x50 ml of dichloromethane.

Tragovi organskog rastvarača se uklone iz vodenog rastvora destilacijom i sotatak je razblažen sa dejonizovanom vodom do zapremine od oko 200ml.Provereno jeidalic.je pH 4. U slučaju potrebe pH je podešeno dodavanjem 0,1 N H2SO4 ili jonoizmenjivačke smole OH faze (npr. AG 1ΧΒ), zatim je rastvor smrznut~i_smrznut sušen. Prinos 12,5g (75%)Traces of the organic solvent are removed from the aqueous solution by distillation and the dilute is diluted with deionized water to a volume of about 200ml.Checked jeidalic.is pH 4. If necessary, the pH is adjusted by adding 0.1 NH 2 SO 4 or ion exchange resin OH phase (e.g. . AG 1ΧΒ), then the solution is frozen ~ and_frozen is dried. Yield 12.5g (75%)

Rf=0,35-0,45 letilacetat/piridin/sirčetna kiselina/voda=25:20:6:1) /(//2°=-126,0+5° (c=l,voda)Rf = 0.35-0.45 lethal acetate / pyridine / acetic acid / water = 25: 20: 6: 1) / (// 2 ° = -126.0 + 5 ° (c = l, water)

DD

Ukupni sadržaj nečistoče na bazi tanko-siojno hromatografske analize je 2-3% .The total impurity content based on thin-chromatographic analysis is 2-3%.

Sadržaj nečistoče na bazi HPLC analize je 3-5%.The impurity content based on HPLC analysis is 3-5%.

N-benziloksikarbonil-N-metil-D-fenilalanil-L-prolll-N -benziloksikarbonil-L-arginin aldehid je koriščen kao polazni materijal i može se dobiti kao što sledi:N-Benzyloxycarbonyl-N-methyl-D-phenylalanyl-L-prolll-N-benzyloxycarbonyl-L-arginine aldehyde was used as starting material and can be obtained as follows:

Stupanj 1Level 1

GMr

N-benziloksikarbonil-N-metil-D-fenilalani1-L-prolil-N benziloksikarbonil-L-arginin laktamN-benzyloxycarbonyl-N-methyl-D-phenylalanyl-L-prolyl-N benzyloxycarbonyl-L-arginine lactam

GMr

42,95g (0,llmola) t-butoksikarbonil-N -benziioksikarboni1-L-aroinin laktama je suspendovano u HOml suvog hloroforma i 275ml hidrohlorid etil acetata, je dodato uz konstantno mešanje. Reakciona smeša je42.95 g (0, 10 mol) of t-butoxycarbonyl-N-benzyloxycarbonyl-L-aroinine lactam was suspended in HOml of dry chloroform and 275ml of ethyl acetate hydrochloride, was added with constant stirring. The reaction mixture is

17.17.

mešana oko 3 časa na sobnoj temperaturi,krajnja tačka reakcije je odredjena tanko-slojnom hromatografijom koriščenjem smeše 60:20:6:11 etil acetat/piridin/sirčekna kiselina/voda kao eluent.stirred for about 3 hours at room temperature, the reaction end point was determined by thin layer chromatography using a mixture of 60: 20: 6: 11 ethyl acetate / pyridine / acetic acid / water as eluent.

(Rf vrednosti polaznog materijala i krajnjeg proizvoda su oko 0,9 i 0,3 respektivno). Na kraju reakcije,smeša se razblaži sa 400ml dietil etra, staložena kristalna supstanca se odfiltrira,Ispere sa 2xl00ml dietil etra i 2x50ml acetona,zatim se osuši na vakumskom eskikatoru iznad fosfor pentoksida i kalijum hidroksida. Posle l-2časa sušenj-a^tako dobivena-laktamska so (oko 0,1 mol) se rastvori u lOOml anhidrovanog dimetil formamida i magacionira na -15°C do svog koriščen-j^dodavanjenrmešanog anhidrida /.dobivenog kao što sledi:(The Rf values of the starting material and the end product are about 0.9 and 0.3 respectively). At the end of the reaction, the mixture was diluted with 400 ml of diethyl ether, the crystalline solid filtered off, washed with 2x100 ml of diethyl ether and 2x50 ml of acetone, then dried on a vacuum ejector over phosphorus pentoxide and potassium hydroxide. After 1-2 hours of drying, the lactam salt thus obtained (about 0.1 mol) was dissolved in 100 ml of anhydrous dimethyl formamide and magnified at -15 [deg.] C. to its used anhydrous anhydride / obtained as follows:

Oslobadjanje N-benziloksikarbonil-N-metil-D-fenilalanil-L-prolina:Release of N-benzyloxycarbonyl-N-methyl-D-phenylalanyl-L-proline:

50,9g (0,1 mola) N-benziloksikarbonil-N-metil-D-fenilalanil-Lproiin cikloheksil amonijumova so je rastvoreno u-2U0ml dietil etra i l20ml IN H2SO4· Etil etarska fa-z-a-je isprana sa 2x50ml vode, osušena iznad anhidrovanog natrijum alfafca i uparena pod sniženim pritsikom na temperaturi od najviše 35°C do dobivanja gustog ulja.50.9g (0.1 mol) of N-benzyloxycarbonyl-N-methyl-D-phenylalanyl-Lproin cyclohexyl ammonium salt was dissolved in-2U0ml diethyl ether and l20ml IN H 2 SO 4 · Ethyl ether fa-3 was washed with 2x50ml of water, dried over anhydrous sodium alfafac and evaporated under reduced pressure at a temperature of not more than 35 ° C to give a thick oil.

Ostatak (oko 0,lmola) je rastvoren.-:i 170ml anhidrovanog dimetil formamida,ohladjen do temperature od -15°C i uz mešanje je dodato ll,2ml(0,l mola) N-metil-morfolina. Zatim je 13,2ml i-butoksikarbonil hlorida dodato ukapavanjem za 3-5 minuta uz održavanje iste temperature. Posle daljih 5-10 minuta mešanja gornja dimetil formamidna suspenzija amino kw.ngS3Mente je* dodata mešanom anhidridu tako dobivenom, zatim se doda 35ml trietil amina reakcionoj smeši uz jako mešanje na temperaturi od -20 do -25°C. pH parnog prostora je proveravan (pH mora biti iznad 8) i slučaju potrebe dodaje se dalja količina trietil amina. Reakcuona smeša se meša 1 čas na temperaturi od -15°C,lčas na 0°C i zatim se razblažuje sa 200ml benzena i 150ml vode se doda.The residue (about 0, 1 mol) was dissolved in .-: and 170 ml of anhydrous dimethyl formamide, cooled to -15 [deg.] C. and 1, 2 ml (0, 1 mol) of N-methyl-morpholine were added with stirring. Then, 13.2ml of i-butoxycarbonyl chloride was added dropwise over 3-5 minutes while maintaining the same temperature. After further 5-10 minutes of stirring, the above dimethyl formamide suspension of amino kw.ngS3Mente was * added to the mixed anhydride thus obtained, then 35 ml of triethyl amine was added to the reaction mixture with vigorous stirring at -20 to -25 ° C. The pH of the vapor space was checked (the pH should be above 8) and a further amount of triethyl amine was added if necessary. The reaction mixture was stirred for 1 hour at -15 ° C, then at 0 ° C and then diluted with 200ml benzene and 150ml water was added.

Faze se razdvoje i vodena faza se ekstrahuje sa 3x30ml benzena.The phases were separated and the aqueous phase was extracted with 3x30ml benzene.

Sjedinjeni benzenski rastvori se isperu sa 2x50ml vode,osušeiznad anhidrovanog natrijum sulfata i upare pod sniženim pritiskom na temperaturi od najviše 40°C -do dobivanja gustog ulja. Uljani ostatak se rastvori u 75ml 2:1 smeše etra i tetrahidrofuranaThe combined benzene solutions were washed with 2x50ml of water, dried over anhydrous sodium sulfate and evaporated under reduced pressure at a temperature of up to 40 ° C to obtain a thick oil. The oily residue was dissolved in 75 ml of a 2: 1 mixture of ether and tetrahydrofuran

18.18.

i filtrira kroz filterski sloj kao što sledi:and filter through a filter layer as follows:

300g (5-struka količina, Kieselgel-60 adsorbensa se supsnduge u etar i filterski sloj se pripremi sa odnosom prečnik:višina od 3:1. Kontaminirajuča gornja mrlja je eluirana sa smešom 95:5 etra i tetrahidrofurana,dok je željeni proizvod eluiran sa čistim tetrahidrofurana.Substanciški sadržaj frakcija je kontrolisan tankoslojnom hromatografijom koriščenjem smeše 480:20:6:11 etil acetat/ piridin/sirčetna kiselina/voda kao eluebta. vrednost željenog proizvoda je 0,71-0,75. Sjedinjene frakcije su uparene pod 1 vakumom na temperaturi od 35°C do dobivanja gustog ostatka i proizvod je koriščen odjednom ili je m&gacionirana u suvom ledu. Prinos: 58,8g (85%).300g (5-fold amount, Kieselgel-60 adsorbents are sundried in ether and the filter layer is prepared with a diameter: 3: 1 ratio. The contaminating top spot is eluted with a mixture of 95: 5 ether and tetrahydrofuran, while the desired product is eluted with The content of the fractions was controlled by thin layer chromatography using a mixture of 480: 20: 6: 11 ethyl acetate / pyridine / acetic acid / water as eluebt. The desired product was 0.71-0.75. The combined fractions were evaporated under 1 vacuum. at 35 [deg.] C. to give a thick residue and the product was used at one time or m &apos; s in dry ice Yield: 58.8g (85%).

Rf=0,7l-0,75 (etil acetat/piridin/sirčetna kiselina/voda=480:20: 6:11.Rf = 0.7l-0.75 (ethyl acetate / pyridine / acetic acid / water = 480: 20: 6:11.

=+13,5° (c=l,tetrahidrofuran)= + 13.5 ° (c = l, tetrahydrofuran)

DD

Stupanj 2Level 2

GMr

N-benziloksikarbonil-N-metil-D-fenilalanil-L-prolil-N benziloksikarbonil-L-arginin aldehidN-benzyloxycarbonyl-N-methyl-D-phenylalanyl-L-prolyl-N benzyloxycarbonyl-L-arginine aldehyde

34,14g (0,05 mola) N-benziloksikarbonil-N-metil-D-fenilalanil-LG propil-N -benziloksikarbonil-L-argin laktama (primer 5,stupanj 1) se rastvori u 150ml suvog tetrahidrofurana ohladjenog do temperature od 0°C. Rastvor je ohladjen do -20°C i 0,0375 mola litijum aluminijum hidrida je rastvoreno u tetrahidrofuranu i dodato uz mešanje za 5-10 minuta. Napredovanje redukcije je pračeno tankoslojnom hromatografijom koristeči smešu 240:20:6:11 etil acetat/ piridin/sirčetna kiselina i voda. (R^ vrednosti laktama koriščenih kao polazni materijal i aldehida su 0,8 i 0,5 respektivno).34.14g (0.05 mol) of N-benzyloxycarbonyl-N-methyl-D-phenylalanyl-LG propyl-N-benzyloxycarbonyl-L-argin lactam (example 5, step 1) was dissolved in 150 ml of dry tetrahydrofuran cooled to 0 ° C. The solution was cooled to -20 ° C and 0.0375 mol of lithium aluminum hydride was dissolved in tetrahydrofuran and added with stirring for 5-10 minutes. The progress of the reduction was followed by thin layer chromatography using a mixture of 240: 20: 6: 11 ethyl acetate / pyridine / acetic acid and water. (The R ^ values of the elbows used as starting material and aldehydes are 0.8 and 0.5 respectively).

U slučaju potrebe,dalja količina litijum aluminijum hidrida se doda, i pri kraju reakcije smeša se postepeno uz neprekidno mešanje sipaIf necessary, a further amount of lithium aluminum hydride is added, and at the end of the reaction, the mixture is gradually mixed with continuous stirring.

320ml IN H„SO prethodno ohladjene do temperature od 2-4°C. Krajnje z 4 pH treba da je izmedju 2 i 3,ovo pH se podešava dodavanjem dalje320ml IN H 'SO pre-cooled to 2-4 ° C. The final z 4 pH should be between 2 and 3, this pH is adjusted by adding further

19.19.

količine I^SO^.ako je potrebno. Ako se gradi talog,ovaj se odfiltrira, rastvor se razblaži sa vodom do zamučenja i zatim se esktrahuje sa 3xl00ml n-heksana.quantities I ^ SO ^ .if necessary. If a precipitate is formed, this is filtered off, the solution is diluted with water until turbid and then extracted with 3xl00ml n-hexane.

Vodena tetrahidrofuranska faza je ekstrahovana sa 250ml dihlorometana 2 ili 3 puta i sjedinjeni dihlorometanski rastvori su isprani sa 2x50ml vode, 2x50ml hladnog 5% rastvora NaHCO^, zatim sa 2x50ml vode. Zatim je rastvor osušen iznad anhidrovanog natrijum sulfata i uparen na vakumu na temperatruii od najviše 40°C.The aqueous tetrahydrofuran phase was extracted with 250 ml of dichloromethane 2 or 3 times and the combined dichloromethane solutions were washed with 2x50ml of water, 2x50ml of cold 5% NaHCO 3 solution, then with 2x50ml of water. The solution was then dried over anhydrous sodium sulfate and evaporated in vacuo to a temperature of not more than 40 ° C.

Ostatk uparavanja je rastvoren u 7:3 smeši dihlorometana i acetona (120ml) i propušhena bez isisavanja kroz filterski sloj dobiven od 180g Kieselgel-60 adsorbensa pomoču 200ml 7:3 smeše dihlorometana i acetona,zatim je filterski sloj ispran sa 600ml iste eluenntske smeše. Postupak ne traje duŽe od 20 minuta.The evaporation residue was dissolved in a 7: 3 mixture of dichloromethane and acetone (120ml) and passed without suction through a filter layer obtained from 180g of Kieselgel-60 adsorbent using 200ml 7: 3 mixture of dichloromethane and acetone, then the filter layer was washed with 600ml of the same eluent mixture. The procedure does not take more than 20 minutes.

Sjedinjeni filtrati se upare do 50-60ml pod sniženim pritiskom na temperaturi najviše od 40°C,zatim se ova operacija ponovi posle dodavanja lOOml benzena ostatku. Proizvod se staloži iz rastvora od Oko 50-60ml dodavanjem lOOml cikloheksana.The combined filtrates were evaporated to 50-60ml under reduced pressure at a temperature of more than 40 ° C, then this operation was repeated after the addition of 100ml of benzene to the residue. The product was precipitated from a solution of about 50-60ml by the addition of 100ml of cyclohexane.

Tako dobiven talog je ispran sa 2x30ml cikloheksana i osušen iznad parafinskih jluspi u vakumskom eksikatoru. Prinos je 18g (53%) .The precipitate thus obtained was washed with 2x30ml cyclohexane and dried over paraffin flakes in a vacuum desiccator. Yield is 18g (53%).

Rf=0,55-0,59 (etil acetat/piridin/sirčetna kiselina/voda=Rf = 0.55-0.59 (ethyl acetate / pyridine / acetic acid / water =

240:20:6:11).240: 20: 6: 11).

/<λ./2θ =+14,1°(c=l,tetrahidrofuran) ./<λ./ 2 θ = + 14.1 ° (c = l, tetrahydrofuran).

DD

Ukupan sadržaj nečistoča proizvoda maskimalno je 2-3%.The total impurity content of the product is 2-3% by weight.

Claims (5)

Patentni zahtevkiPatent claims 1. Izboljšan postopek za pridobivanje tripeptidnih aldehidov s formulo IAn improved process for the preparation of tripeptide aldehydes of formula I R-D-Phe-Pro-Arg-H.H2SO4 I kjerRD-Phe-Pro-Arg-HH 2 SO 4 I where R predstavlja vodik ali metil, je Phe fenilalaninska skupina, je Pro L-prolinska skupina in Arg označuje L-argininsko skupino v farmacevtsko čisti obliki, s kondenzacijo NG-zaščitenega-L-arginin laktama s formulo IV,R represents hydrogen or methyl, Phe is a phenylalanine group, is a Pro L-proline group, and Arg denotes the L-arginine group in pharmaceutically pure form, by condensation of the N G -protected-L-arginine lactam of formula IV, H-Arg (Z)-laktam.HCl IV kjer ima Arg enak pomen, kot predhodno in Z označuje benziloksikarbonil, z dipeptidom s formulo V,H-Arg (Z) -lactam.HCl IV where Arg has the same meaning as above and Z denotes benzyloxycarbonyl with a dipeptide of formula V, ZR (D-Phe)-Pro-OH V kjer so R, Z, Phe in Pro enaki, kot je definirano predhodno, preko mešanega anhidrida, redukcijo tripeptidnega laktama s formulo III,ZR (D-Phe) -Pro-OH V where R, Z, Phe and Pro are the same as defined previously, via mixed anhydride, reduction of the tripeptide lactam of formula III, ZR (D-Phe)-Pro-Arg (Z)-laktam III kjer so R, Z, Phe, Pro in Arg enaki, kot je definirano predhodno, z litijevim aluminijevim hidridom in hidrogenolizo tako dobljenega zaščitenega tripeptidnega aldehida s formulo IIZR (D-Phe) -Pro-Arg (Z) -lactam III wherein R, Z, Phe, Pro and Arg are the same as previously defined with lithium aluminum hydride and hydrogenolysis of the protected tripeptide aldehyde of formula II thus obtained ZR-(D-Phe)-Pro-Arg(Z)-H II kjer so R, Z, Phe in Arg enaki, kot je definirano predhodno, v prisotnosti H2SO4, označen s tem, da obsega af sprostitev Nezaščitenega L-arginin laktama in situ med kondenzacijo NGzaščitenega -L-arginin laktam hidroklorida s formulo IV,ZR- (D-Phe) -Pro-Arg (Z) -H II wherein R, Z, Phe and Arg are the same as defined previously in the presence of H 2 SO 4 , characterized in that af comprises the release of Unprotected L -arginin lactam in situ during the condensation of N G protected L-arginine lactam hydrochloride of the formula IV, H-Arg (Z)-laktam.HClH-Arg (Z) -lactam.HCl IV kjer je Z enak, kot je definiran predhodno, in dipeptida s formulo VIV wherein Z is the same as previously defined and a dipeptide of formula V ZR(D-Phe)-Pro-OH V kjer so R, Z, Phe in Pro enaki, kot je definirano predhodno, v mešani anihdrid, v reakcijski zmesi in nato dodajanje baze k zmesi omenjenih reakcijskih komponent, nato, po redukciji tako dobljenega zaščitenega tripeptidnega laktama s formulo III,ZR (D-Phe) -Pro-OH V wherein R, Z, Phe and Pro are the same as previously defined in the mixed anhydride, in the reaction mixture and then adding the base to the mixture of said reaction components, then, after reduction of the thus obtained protected tripeptide lactam of formula III, ZR (D-Phe)-Pro-Arg(Z)-laktam III kjer so R, Z, Phe, Pro in Arg enaki, kot je definirano predhodno, razgradnjo tako dobljenega kompleksa z dodajanjem reakcijske zmesi v prebitek IN H2SO4 pri temperaturi od 0 do 5°C in nato izvedbo hidrogenolize zaščitenega tripeptida s formulo II,ZR (D-Phe) -Pro-Arg (Z) -lactam III where R, Z, Phe, Pro and Arg are the same as defined previously, decomposing the complex thus obtained by adding the reaction mixture to excess AND H 2 SO 4 at temperature from 0 to 5 ° C and then carrying out the hydrogenolysis of the protected tripeptide of formula II, ZR-(D-Phe)-Pro-Arg(Z)-H II kjer so R, Z, Phe, Pro in Arg enaki, kot je definirano predhodno, pri temperaturi pod 10°C, v prisotnosti 1-2 molskih ekvivalentov H2SO4 ali a2) po redukciji tako dobljenega zaščitenega tripeptidnega laktama s formulo III,ZR- (D-Phe) -Pro-Arg (Z) -H II where R, Z, Phe, Pro and Arg are the same as previously defined at a temperature below 10 ° C in the presence of 1-2 molar equivalents of H 2 SO 4 or a 2 ) after reduction of the protected tripeptide lactam of formula III thus obtained, ZR (D-Phe)-Pro-Arg (Z)-laktam III kjer so R, Z, Phe, Pro in Arg enaki, kot je definirano predhodno, razgradnjo tako tvorjenega kompleksa z dodajanjem reakcijske zmesi v prebitek IN H2SO4 pri temperaturi od 0°C do 5°C, nato izvedbo hidrogenolize tako dobljenega zaščitenega tripeptida s formulo II,ZR (D-Phe) -Pro-Arg (Z) -lactam III wherein R, Z, Phe, Pro and Arg are the same as defined previously, decomposing the complex thus formed by adding the reaction mixture to excess AND H 2 SO 4 at a temperature from 0 ° C to 5 ° C, followed by the hydrogenolysis of the protected tripeptide of formula II thus obtained, ZR-(D-Phe)-Pro-Arg(Z)-H II kjer so R, Z, Phe, Pro in Arg enaki, kot je definirano predhodno, pri temperaturi pod 10°C v prisotnosti 1-2 molskih ekvivalentov H2SO4, ali a3) izvedbo hidrogenolize zaščitenega tripeptida s formulo II,ZR- (D-Phe) -Pro-Arg (Z) -H II where R, Z, Phe, Pro and Arg are the same as previously defined at a temperature below 10 ° C in the presence of 1-2 molar equivalents of H 2 SO 4 , or a 3 ) performing a hydrogenolysis of a protected tripeptide of formula II, ZR-(D-Phe)-Pro-Arg-(Z)-HZR- (D-Phe) -Pro-Arg- (Z) -H IIII 22kjer so R, Z, Phe, Pro in Arg enaki, kot je definirano predhodno, pri temperaturi pod 10°C, v prisotnosti 1-2 molskih ekvivalentov H2SO4.22 where R, Z, Phe, Pro and Arg are the same as previously defined at a temperature below 10 ° C in the presence of 1-2 molar equivalents of H 2 SO 4 . 2. Postopek po zahtevku 1, označen s tem, da obsega sprostitev Νθ-zaščitenega-Larginin laktama iz laktam hidroklorida s formulo IV s trietilaminom.The process of claim 1, wherein the release comprises Νθ-protected-Larginine lactam from lactam hydrochloride of formula IV with triethylamine. 3. Postopek po zahtevku 1, označen s tem, da obsega izvedbo hidrogenolize pri temperaturi od 6 - 8°C.Process according to claim 1, characterized in that it comprises carrying out hydrogenolysis at a temperature of 6 - 8 ° C. 4. Postopek po enem od zahtevkov 1-3, označen s tem, da obsega izvedbo hidrogenolize s prepihavanjem plina vodika skozi sistem.Process according to one of Claims 1-3, characterized in that it comprises performing hydrogenolysis by blowing hydrogen gas through the system. 5. Postopek po enem od zahtevkov 1-3, označen s tem, da hidrogenolizo izvedemo v etanolu ali tetrahidrofuranu.Process according to one of Claims 1-3, characterized in that the hydrogenolysis is carried out in ethanol or tetrahydrofuran.
SI9011225A 1990-06-22 1990-06-22 Improved production procedure of tripeptide aldehydes SI9011225A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
YU122590A YU49020B (en) 1990-06-22 1990-06-22 Improved process for the preparation of tripeptide aldehydes

Publications (1)

Publication Number Publication Date
SI9011225A true SI9011225A (en) 1997-10-31

Family

ID=25553295

Family Applications (1)

Application Number Title Priority Date Filing Date
SI9011225A SI9011225A (en) 1990-06-22 1990-06-22 Improved production procedure of tripeptide aldehydes

Country Status (2)

Country Link
SI (1) SI9011225A (en)
YU (1) YU49020B (en)

Also Published As

Publication number Publication date
YU49020B (en) 2003-07-07
YU122590A (en) 1992-07-20

Similar Documents

Publication Publication Date Title
CA1258749A (en) METHOD OF PREPARING .alpha.-L-ASPARTYL-L-PHENYLALANINE METHYL ESTER AND ITS HYDROCHLORIDE
RO111191B1 (en) Preparation and/or purification process for the clavulanic acid and intermediary for its preparation thereof
JP3792777B2 (en) Method for producing 1-alkoxycarbonyl-3-phenylpropyl derivative
CN112739683B (en) Preparation method of brivaracetam and intermediate thereof
KR20020002476A (en) Formation and anion-exchange of crystalline echinocandin ammonium salts
CN102993270A (en) Preparation process of glycyl-L-tyrosine
EP3162810B1 (en) Method for producing synthetic pentapeptide
AU677654B2 (en) New phosphonic acid compounds, process for preparing them and pharmaceutical compositions containing them
JPH09501697A (en) 1- [N ▲ 22-((S) -ethoxycarbonyl) -3-phenylpropyl) -N ▲ 66-trifluoroacetyl] -L-lysyl-L-proline (lisinopril (Tfa) ethyl ester Purification method
SE452318B (en) AMINO ACIDS FOR USE AS INTERMEDIATES IN THE PRODUCTION OF BESTATIN
SU648082A3 (en) Metho of obtaining amino acid deriva]ves, their salts, racemates or optically active antipodes
SI9011225A (en) Improved production procedure of tripeptide aldehydes
JP2002524569A (en) Neotame manufacturing method
Knowlton et al. Acyl substituent effects on ester aminolysis
KR100336139B1 (en) Novel peptide active materials and methods for their preparation
CN106045883B (en) A kind of preparation method of aspartic acid -1- tert-butyl ester derivatives
HRP920779A2 (en) IMPROVED PROCEDURE FOR THE PREPARATION OF TRIPEPTIDE ALDEHYDS
GB2244994A (en) Preparation of tripeptide aldehydes
KR0147817B1 (en) Method for producing tripeptide aldehydes
IE61522B1 (en) Improved process for the prepartion of tripeptide aldehydes
CH651015A5 (en) CARNITINAMIDES OF OPTICALLY ACTIVE AMINO ACIDS AND PROCEDURES FOR THEIR PREPARATION.
SU1095588A1 (en) Cyclic analog of enkephalin displaying analgetic effect
EP0050856B1 (en) New peptide, process for its preparation and pharmaceutical composition containing it
US5149812A (en) Industrial process for the preparation of (1S)-1-[N-(4-O-deacetyl-23-vinblastinoyl)amino]-2-methylpropyl diethyl phosphonate and its salts
SU1051062A1 (en) Process for preparing arylamides of n-substituted amino acids and peptides