SI9400087A - Novel process for the preparation of cetrorelix lyophilisate - Google Patents
Novel process for the preparation of cetrorelix lyophilisate Download PDFInfo
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- SI9400087A SI9400087A SI9400087A SI9400087A SI9400087A SI 9400087 A SI9400087 A SI 9400087A SI 9400087 A SI9400087 A SI 9400087A SI 9400087 A SI9400087 A SI 9400087A SI 9400087 A SI9400087 A SI 9400087A
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- SI
- Slovenia
- Prior art keywords
- lyophilisate
- cetrorelix
- weight
- mannitol
- preparation
- Prior art date
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- 108700008462 cetrorelix Proteins 0.000 title claims description 17
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Abstract
Description
-1NOV POSTOPEK IZDELAVE CETRORELIX LIOFILIZATA-1New Procedure for Manufacturing CETRORELIX Lyophilizates
Cetrorelix je dekapeptid s končno kislinsko amidno skupino, ki se ga uporablja kot acetatno sol. Sinteza in nekateri farmakološki učinki so opisani v EP - prijavi 299 402.Cetrorelix is a decapeptide with the final acid amide group used as the acetate salt. The synthesis and certain pharmacological effects are described in EP application 299 402.
Učinkovino naj bi bilo mogoče aplicirati subkutano v dozi 0,1 do 20 mg. Vodne raztopine dekapeptida so nestabilne, avtoklaviranje v končni posodi ni mogoče. Dekapeptid nagiba pri običajni sterilizaciji po farmakopeji k razpadanju. Da bi dobili raztopino, ki jo je mogoče injiciraii, je bil torej nujen razvoj liofilizata. Vsekakor je količina učinkovine v raztopini, ki naj bi se jo liofiliziralo tako majhna, da po sušenju raztopin z nizkimi koncentracijami učinkovin brez pomožnih sredstev rezultirajo na stekleni steni ampule samo rahla fina vlakna, ki jih tok vodne pare, uporabljene za sterilizacijo, iznese iz posodice. Uporabiti je tudi potrebno tvorec ogrodja, ki tvori stabilno pogačo. Pri visokih koncentracijah učinkovin se je mogoče tem pomožnim snovem odpovedati. Kot tvorci ogrodja pridejo v poštev naslednje pomožne snovi: heksiti (heksitoli), posebno manit, glucit, sorbit, kot D-sorbit, dulcit, allit, altrit (na primer D- in L-altrit), idit (na primer D- in L-idit), njihove optično aktivne oblike (D-oziroma L-oblike) kot tudi odgovarjajoči racemati. Zlasti se uporabljajo manit, kot D-manit, L-manit, DL-manit, sorbit in/ali dulcit in sicer od teh predvsem D-manit. Kot heksit se lahko uporabijo tudi zmesi omenjenih heksitov, na primer zmesi manita in sorbita in/ali dulcita. Ker je dulcit v vodi manj topen kot na primer manit, naj koncentracija dulcita v vodni raztopini na primer ne preseže 3 masnih %. Manit in sorbit pa sta lahko na primer zmešana v vseh razmerjih.The active substance should be administered subcutaneously at a dose of 0.1 to 20 mg. Aqueous decapeptide solutions are unstable; autoclaving in the final vessel is not possible. Decapeptide tends to decompose in normal post-pharmacopoeial sterilization. Therefore, the development of a lyophilisate was necessary in order to obtain an injectable solution. In any case, the amount of the active substance in the solution to be lyophilized is so small that, after drying the solutions with low concentrations of the active substances without auxiliary agents, only the fine fibers are removed from the ampoule glass wall by the steam stream used for sterilization from the container. . It is also necessary to use a frame creator to form a stable cake. At high concentrations of the active substances, these excipients can be waived. The following excipients are considered as framework makers: hexites (hexitols), especially mannitol, glucit, sorbitol, such as D-sorbitol, dulcite, allit, altrit (for example D- and L-altrit), idite (for example D- and L-idite), their optically active forms (D- or L-forms) as well as the corresponding racemates. In particular, mannitol is used, such as D-mannitol, L-mannitol, DL-mannitol, sorbitol and / or dulcite, of which mainly D-mannitol. Hexite may also be used as mixtures of said hexites, for example mixtures of mannitol and sorbitol and / or dulcite. Since dulcite is less soluble in water than for example mannitol, for example, the concentration of dulcite in an aqueous solution should not exceed 3% by weight. For example, mannitol and sorbitol can be confused in all proportions.
Poleg heksita se lahko doda tudi še druge običajne farmacevtske pomožne snovi, kot na primer amino kisline, kot na primer alanin, glicin, lizin, fenilalanin, asparaginsko kislino, glutaminsko kislino, levcin, laktozo, polivinilpirolidon, glukozo, fruktozo, albumin in ekvivalentne tvorce ogrodja. Nadalje se lahko kot tvorce ogrodja uporabi sečnino in natrijev klorid. Skupna množina takih snovi v raztopini, ki se uporabi za liofilizacijo, je na primero -16,9 masnih deležev, na primer 0,1 - 7 masnih deležev, glede na 1 masni delež cetrorelixa. V gotovem liofilizatu je lahko skupna množina takih pomožnih snovi do 16,9 masnih deležev, glede na en masni delež heksita. V podrobnostih se množina takih pomožnih snovi ravna po obstajajoči množini heksita in sicer tako, da skupna množina heksita in drugih takih pomožnih snovi v gotovem liofilizatu maksimalno ne znaša več kot 17 masnih deležev, glede na 1 masni delež cetrorelixa. V primeru, da je v liofilizatu samo 0,1 masni delež heksita, je lahko tudi do 16,9 masnih deležev drugih pomožnih snovi; če obstaja na primer 8,5In addition to hexite, other conventional pharmaceutical auxiliaries, such as amino acids such as alanine, glycine, lysine, phenylalanine, aspartic acid, glutamic acid, leucine, lactose, polyvinylpyrrolidone, glucose, fructose, albumin and equivalents, may be added frames. Furthermore, urea and sodium chloride may be used as the framework's creators. The total amount of such substances in the solution used for lyophilization is, for example, -16.9% by weight, for example 0.1 - 7% by weight, relative to 1% by weight of cetrorelix. In the finished lyophilisate, the total amount of such excipients may be up to 16.9% by weight, based on one weight fraction of hexite. In detail, the amount of such excipients shall be guided by the existing amount of hexite, such that the total amount of hexite and other such excipients in the finished lyophilisate does not exceed a maximum of 17 parts by weight based on 1 weight fraction of cetrorelix. If there is only 0.1% by weight of hexite in the lyophilisate, up to 16.9% by weight of other excipients may be present; if for example 8.5
-2masnih deležev heksita, je lahko na primer množina drugih pomožnih snovi do 8,5 masnih deležev, glede na 1 masni delež cetrorelixa.For example, by weight of 2% by weight of hexite, the amount of other excipients may be up to 8.5% by weight, relative to 1% by weight of cetrorelix.
Med razvojnimi deli do liofilizata pa smo morali ugotoviti, da se učinkovina vede pri predelavi zelo različno in nepredvidljivo. Prvi poskusi so vodili do dobrih rezultatov, kmalu pa se je izkazalo, da nastopijo težave pri sterilizaciji s filtriranjem in sledijo izjalovljene šarže.However, from development to lyophilisate, we had to find out that the active substance behaves very differently and unpredictably during processing. The first experiments led to good results, and problems with filtering sterilization soon followed and failed batches followed.
Iz literature na primer iz Povvell, M.F.: Pharmaceutical Research, 1258-1263 (8)1991; Dathe, M.: Int. J. Peptide Protein Res. 344-349 (36) 1990; Szejtli, J.: Pharmaceutical Technology International 1622, 1991 je poznano, da oligopeptidi posebno taki s končno kislinsko amidno funkcijo, nagibajo k tvorbi gela. Pri sterilizaciji s filtriranjem je to vidno pri hitrosti filtracije, često se celo ugotovi povišano viskoznost takšnih raztopin že organoleptično. Na filtru za sterilizacijo preostane galerti podobna plast. S tem ni več mogoče pripraviti zdravila s točno definirano koncentracijo učinkovine.From the literature, for example, Povvell, M. F.: Pharmaceutical Research, 1258-1263 (8) 1991; Dathe, M.: Int. J. Peptide Protein Res. 344-349 (36) 1990; Szeitli, J.: Pharmaceutical Technology International 1622, 1991 It is known that oligopeptides, especially those with a terminal acid amide function, tend to form a gel. In sterilization by filtration, this is evident at the filtration rate, and often the increased viscosity of such solutions is already organoleptic. There is a layer-like layer remaining on the sterilization filter. Thus, it is no longer possible to prepare a drug with a well-defined active substance concentration.
V tabeli 1 so našteti različni izsledki prvih 11 poskusov.Table 1 lists the different outcomes of the first 11 experiments.
Koncentracije učinkovin nihajo med 100 % in 36 %.Active substance concentrations fluctuate between 100% and 36%.
Tabela 1: cetrorelix-acetatTable 1: Cetrorelix acetate
Šarža DoziranjeBatch Dosage
Koncentracija učinkovine %Concentration of the active substance%
-3V literaturi so navedeni naslednji dodatki za preprečitev te tvorbe gela, ki so bili uporabljeni poskusno:-3 The following supplements have been reported in the literature to prevent this gel formation that have been used experimentally:
V poštev pridejo organska topila, na primer acetonitril, n-butanol, terciarni butanol, etanol, izopropanol, oktanol in benzilalkohol. Dalje se lahko uporabi soli in pufrske raztopine, kot na primer acetatni pufer, citratni pufer, natrijev klorid, natrijev fosfat, natrijev EDTA, natrijev bikarbonat, fosfatni pufer, gvanidinacetat, sečnino.Organic solvents such as acetonitrile, n-butanol, tertiary butanol, ethanol, isopropanol, octanol and benzyl alcohol may be considered. Further, salts and buffer solutions such as acetate buffer, citrate buffer, sodium chloride, sodium phosphate, sodium EDTA, sodium bicarbonate, phosphate buffer, guanidine acetate, urea may be used.
Nadalje se lahko uporabi polimere kot na primer želatino, polietilenglikol 600, hidroksietil škrob, polivilpirolidon, polivilalkohol. Tudi dodatek amino kislin, na primer alanina, glicina, lizina, fenilalanina, asparaginske kisline, glutaminske kisline in levcina je bil že opisan.Further polymers such as gelatin, polyethylene glycol 600, hydroxyethyl starch, polyvinylpyrrolidone, polyvalyl alcohol may be used. The addition of amino acids, for example alanine, glycine, lysine, phenylalanine, aspartic acid, glutamic acid and leucine, has already been described.
Od kislin so bile uporabljene citronska kislina, kaprilska kislina, oktanojska kislina, klorovodikova kislina, žveplova(VI) kislina in ocetna kislina. Od fiziološko neoporečnih tenzidov so na voljo benzalkonijev klorid, cetil alkohol, žolčne kisline, lecitin, polisorbati, Spans(R) in Pluronics(R).Citric acid, caprylic acid, octanoic acid, hydrochloric acid, sulfuric (VI) acid, and acetic acid were used. Of the physiologically acceptable surfactants, benzalkonium chloride, cetyl alcohol, bile acids, lecithin, polysorbates, Spans (R) and Pluronics (R) are available .
Tudi ogljikovi hidrati in ciklodekstrini kot na primer glukoza, laktoza, manitol, saharoza, alfa-, betain gama ciklodekstrini, hidroksipropil-alfa- in beta-ciklodekstrini, hidroksietil ciklodekstrini in metil ciklodekstrini so že bili uporabljeni. Te pomožne snovi so bile preskušene kot pomožna sredstva za filtriranje za preprečitev nastajanja gela.Carbohydrates and cyclodextrins such as glucose, lactose, mannitol, sucrose, alpha-, betaine gamma cyclodextrins, hydroxypropyl-alpha- and beta-cyclodextrins, hydroxyethyl cyclodextrins and methyl cyclodextrins have also been used. These excipients have been tested as filtering aids to prevent gel formation.
Zadovoljive rešitve problema pa ni bilo mogoče ugotoviti. Samo nakisanje z ocetno kislino je pokazalo delne uspehe. Toda tudi tu smo se morali vedno znova sprijazniti z velikimi izgubami pri filtriranju. Presenetljivo pa seje izkazalo, da je mogoče cetrorelix dobro raztopiti v 30 % v./v. ocetni kislini. Tej raztopini smo nato dolili vodo za injekcijske namene do končne koncentracije 3 % cetrorelixa in dodali manit. Čeprav je v literaturi opisano, da v kislem mediju končna amidna skupina zlahka hidrolizira, tega pri cetrorelixu nismo mogli ugotoviti. Raztopine, pripravljene po tej metodi, niso delale pri filtraciji nobenih težav. Vedno smo našli korektne koncentracije učinkovine.However, a satisfactory solution to the problem could not be determined. Acetic acid acidification alone has shown partial success. But even here, we always had to face the huge filtering losses. Surprisingly, cetrorelix has been shown to be able to dissolve well in 30% v./v. acetic acid. This solution was then filled with water for injection to a final concentration of 3% cetrorelix and mannitol added. Although it has been reported in the literature that the terminal amide group is readily hydrolyzed in an acidic medium, this has not been established with cetrorelix. The solutions prepared by this method did not work for filtration problems. We have always found the right concentrations of the active substance.
Hitrost filtracije doseže vrednosti, ki zagotavljajo zadovoljive poteke proizvodnje. Splošen proces sterilne liofilizacije je opisan v Sucker, Fuchs und Speiser (Herausgeber) Pharmazeutische Technologie 2. izdaja 1991, Thieme-Verlag, Stuttgart-New York, na straneh 557-559. Nadaljnji opis uporabljenega liofilizacijskega procesa se nahaja v DE-OS 37 35 614.The filtration rate reaches values that ensure satisfactory production runs. The general process of sterile lyophilization is described in Sucker, Fuchs und Speiser (Herausgeber) Pharmazeutische Technologie 2nd Edition 1991, Thieme-Verlag, Stuttgart-New York, pages 557-559. A further description of the lyophilization process used is found in DE-OS 37 35 614.
Liofilizat se uporablja pri terapiji sterilnosti žensk. Terapevtski postopek obstoji do sedaj v tem, daLyophilisate is used in the treatment of women's sterility. The therapeutic procedure exists so far in that
-4se zorenje foliklov stimulira s humanim menopavzalnim gonadotropinom in nato sproži ovulacijo z odmerkom humanega horionskega gonadotropina. Do tako sprožene ovulacije je prišlo 32 ur kasneje. Tako pridobljene jajčne celice so na razpolago za oploditev zunaj telesa.-4 All follicular maturation is stimulated by human menopausal gonadotropin and then triggered by ovulation with a dose of human chorionic gonadotropin. Such ovulation was triggered 32 hours later. The eggs thus obtained are available for fertilization outside the body.
Slaba stran te terapije z agonisti je dejstvo, da v stimulacijski fazi dozori do 10 foliklov. Zaradi tega povečanega zorenja foliklov pride do vrhov hormonskega nivoja LH. Posledica teh vrhov je zgodnji stadij zorenja foliklov in ovulacija v nepredvidenem času. Do te motnje ovulacije pride pri približno 25% obravnavanih primerov in predstavlja slabo stran, ker je ciklus, ki kaže takšno motnjo ovulacije izgubljen za pridobivanje jajčnih celic in se mora ves postopek približno 1 mesec kasneje ponoviti.The downside of this agonist therapy is the fact that up to 10 follicles mature in the stimulation phase. This increased follicle maturation leads to peaks in the hormonal level of LH. These peaks result in early follicular maturation and ovulation at an unanticipated time. This ovulation disorder occurs in about 25% of the cases considered and is a disadvantage because the cycle showing such ovulation disorder is lost to egg production and must be repeated about 1 month later.
Nadaljnja slaba stran konvencionalnega postopka stimulacije je 4 tedne dolgo trajanje terapije, ki je potrebno, da se doseže zadostno supresijo. Nadalje kažejo agonisti v 1-2 % primerov sindrom hiperstimulacije, pri kateri celice folikla hipertrofirajo. Rizik hiperstimulacije je posebno velik pri policističnih ovarijih. Sindrom hiperstimulacije je hud stranski učinek, ki lahko vodi do smrtnih primerov.A further disadvantage of the conventional stimulation process is the 4-week duration of therapy required to achieve sufficient suppression. In 1-2% of cases, agonists also show hyperstimulation syndrome in which the follicle cells hypertrophy. The risk of hyperstimulation is particularly high in polycystic ovaries. Hyperstimulation syndrome is a severe side effect that can lead to death.
Izkazalo pa se je, da ima antagonist cetrorelix ravno pri tem postopku naslednje prednosti:In this process, however, the cetrorelix antagonist has been shown to have the following advantages:
Da bi dosegli totalno supresijo, zadošča pri postopku s cetrorelixom 5 dni trajajoča terapija. Do sindroma hiperstimulacije ne more priti. Vrh tega je mogoče v 2. fazi terapije, v fazi sproženja ovulacije, prihraniti HMG. To predstavlja ne nepomebno stroškovno prednost tega postopka zunaj telesne oploditve. Oploditev zunaj telesa se uporablja na primer pri okvari jajcevodov. Za to terapijo je potrebno ciklus točno nadzorovati in čas ovulacije čim bolj točno določiti. Do zdaj je bilo to doseženo le omejeno, ker se je zaradi stimulacije s HMG/HCG pojavil predovulatorni porast LH često prezgodaj ali se ni ohranil dovolj dolgo. Vendar je za uspeh postopka odločilnega pomena, da se ta prezgodnji porast prepreči, da bi lahko točno določili čas oploditve. S tem se zmanjša telesno in psihično obremenitev pacientke in optimalno uporabi klinično logistiko. Da bi dosegli ta cilj z visoko zanesljivostjo, je potrebno čim bolj popolnoma suprimirati endogeno produkcijo hormonov (LH-FSH, estradiol), da bi hkrati z odmerkom eksogenih gonadotropinov (HMG/HCG) stimulirali zorenje foliklov in ves čas nadzorovali hormonski status. Šele ko je doseženo dovolj visoko število foliklov (4-6), ki imajo približno enako stopnjo zrelosti, se sproži ovulacijo z odmerkom HCG-bolus injekcije.In order to achieve total suppression, 5 days of therapy is sufficient in the cetrorelix procedure. Hyperstimulation syndrome cannot occur. In addition, HMG can be saved in phase 2 of therapy, during the ovulation initiation phase. This represents a not insignificant cost advantage of this procedure beyond bodily fertilization. Out-of-body fertilization is used for example in fallopian tubes. For this therapy, the cycle should be closely monitored and the time of ovulation determined as accurately as possible. To date, this has been achieved only to a limited extent because pre-ovulatory LH rise often occurs prematurely or does not persist for long enough due to HMG / HCG stimulation. However, it is crucial for the success of the procedure to prevent this premature rise so that the timing of fertilization can be accurately determined. This reduces the physical and mental burden of the patient and optimally utilizes clinical logistics. In order to achieve this goal with high reliability, endogenous hormone production (LH-FSH, estradiol) must be suppressed as completely as possible in order to stimulate follicular maturation and control hormonal status at the same time as the dose of exogenous gonadotropins (HMG / HCG). Only when a sufficiently high number of follicles (4-6) having approximately the same degree of maturity is reached, ovulation is initiated with a dose of HCG bolus injection.
Z uporabo antagonista je mogoče izvesti postopek bistveno uspešneje in varneje za pacientko.Using the antagonist can make the procedure significantly more successful and safer for the patient.
Nadaljnje področje uporabe cetrorelix-liofilizata v skladu s predloženin izumom je uporaba pri zaščiti gonad pacientov moškega spola. Paciente predhodno zdravijo s cetrorelix liofilizatom in s temA further scope of cetrorelix-lyophilisate according to the present invention is the use in the protection of gonads of male patients. Patients are pre-treated with cetrorelix lyophilisate and therefore
-5podkrepijo aktivnost gonad. Zaradi tega nimajo drugi škodljivi vplivi, kot na primer terapija z obsevanjem ali terapija s citostatiki nobenih možnosti ali samo še majhne, da bi učinkovali na občutljivo tkivo gonad.-5Support gonad activity. As a result, no other adverse effects, such as radiation therapy or cytostatic therapy, have any potential, or only minor, to affect the sensitive tissue of the gonads.
Primer izdelavnega postopka:Example of manufacturing process:
V primerno stekleno posodo pripravimo približno 1,5 litra vode za injekcijske namene. V drugo stekleno posodo pripravimo 210 g vode za injekcijske namene in dodamo 91,17 g ocetne kisline. Izračunano količino cetrorelix acetata (1,62 - 1,695 g, glede na koncentracijo uporabljene šarže) raztopimo med mešanjem v pripravljeni 30 % -ni ocetni kislini. To raztopino prenesemo v stekleno posodo z 1,5 litra vode za injekcijske namene, dodamo 82,2 g manitola, raztopimo in z vodo za injekcijske namene dopolnimo na 3039 g.Prepare approximately 1.5 liters of water for injection in a suitable glass container. Prepare 210 g of water for injection for the second glass vessel and add 91.17 g of acetic acid. The calculated amount of cetrorelix acetate (1.62-1.695 g, depending on the concentration of the batch used) was dissolved while stirring in the prepared 30% acetic acid. Transfer this solution to a glass jar with 1.5 liters of water for injection, add 82.2 g of mannitol, dissolve and make up to 3039 g with water for injection.
Kontrola med postopkom:Control during the process:
vrednost pH: 2,5 - 3,0 gostota: 1,009 - 1,017 g/cm2 3 pri 20° C lomni količniki: 1,227 - 1,340 pri 440 nm in 20° C.pH value: 2.5 - 3.0 density: 1.009 - 1.017 g / cm 2 3 at 20 ° C refractive index: 1.227 - 1.340 at 440 nm and 20 ° C.
Sterilizacija raztopine poteka s filtriranjem preko primernega membranskega filtra (širina por 0,2 pm) pri aseptičnih pogojih. 100 ml predtoka je potrebno zavreči. Filtre je potrebno sterilizirati z vodno paro pod tlakom. Raztopino cetrorelixa za liofilizacijo hranimo zaščiteno pred rekontaminacijo.Sterilization of the solution is carried out by filtration through a suitable membrane filter (pore width 0.2 pm) under aseptic conditions. 100 ml of flow must be discarded. The filters must be sterilized with pressurized steam. Keep the cetrorelix solution for lyophilization protected from recontamination.
Raztopino takoj doziramo v injekcijske stekleničke DIN 2R brezbarvne, hidrolitski razred I, pri aseptičnih pogojih in opremimo s sterilnimi liofilizacijskimi zamaški. Teoretična polnilna količina je 2,0 ml = 2,026 g.The solution is immediately dispensed into colorless DIN 2R vials, hydrolytic class I, under aseptic conditions and equipped with sterile lyophilization stoppers. The theoretical fill amount is 2.0 ml = 2.026 g.
ml injekcijske stekleničke so bile oprane na stroju za pranje injekcijskih stekleničk in osušene z vročim zrakom ter sterilizirane. Očiščeni liofilizacijski zamaški so bili avtoklavirani. Predzaprte injekcijske stekleničke smo prenesli v napravo za liofilizacijo in zamrznili pri ploščni temperaturi 40°C. Sušenje poteka s pomočjo sušilnega programa pri ploščni temperaturi, ki narašča od -40°C na +20° C. Nato napravo napolnimo s sterilnim dušikom, stekleničke v napravi zapremo in zamaške zavarujemo z zarobljenemi pokrovi.ml of the injection bottles were washed on the bottle washer and dried with hot air and sterilized. The cleaned lyophilization stoppers were autoclaved. The pre-closed vials were transferred to a lyophilizer and frozen at a plate temperature of 40 ° C. Drying is carried out by means of a drying program at a plate temperature rising from -40 ° C to + 20 ° C. Then the device is filled with sterile nitrogen, the bottles in the device are closed and the caps are sealed with the covers closed.
-6Injekcijske stekleničke vizualno kontroliramo na napake pri zapiranju in zunanje napake. Injekcijske stekleničke z napakami izsortiramo in uničimo.-6Injection bottles are visually controlled for sealing errors and external faults. Defective injection bottles are sorted and destroyed.
Liofilizat cetrorelix 1 mg je bela, trdna liofilizirana pogača v brezbarvni 2 ml injekcijski steklenički, ki je zaprta s sivim liofilizacijskim zamaškom in rumenim flipp-off zarobljenim pokrovom.Cetrorelix 1 mg lyophilisate is a white, solid lyophilized cake in a colorless 2 ml bottle closed with a gray lyophilization stopper and a yellow flipp-off trapped lid.
Claims (4)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4305225A DE4305225A1 (en) | 1993-02-19 | 1993-02-19 | New manufacturing process for Cetrorelix lyophilisate |
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| Publication Number | Publication Date |
|---|---|
| SI9400087A true SI9400087A (en) | 1994-12-31 |
| SI9400087B SI9400087B (en) | 2002-02-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| SI9400087A SI9400087B (en) | 1993-02-19 | 1994-02-18 | Novel process for the preparation of cetrorelix lyophilisate |
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| EP (2) | EP0947200B1 (en) |
| JP (1) | JP4033919B2 (en) |
| KR (2) | KR100355686B1 (en) |
| CN (1) | CN1109557C (en) |
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| AU (1) | AU671881C (en) |
| BR (1) | BR9400617A (en) |
| CA (1) | CA2115943C (en) |
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| ES (1) | ES2148247T3 (en) |
| FI (1) | FI110059B (en) |
| GR (1) | GR3034237T3 (en) |
| HR (1) | HRP940117B1 (en) |
| HU (1) | HU218281B (en) |
| IL (1) | IL108704A (en) |
| MX (1) | MX9401312A (en) |
| NO (1) | NO316601B1 (en) |
| NZ (2) | NZ250906A (en) |
| PL (1) | PL177177B1 (en) |
| PT (1) | PT611572E (en) |
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| SI (1) | SI9400087B (en) |
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| TW (1) | TW387812B (en) |
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| DK1082129T3 (en) * | 1998-04-23 | 2004-01-26 | Zentaris Gmbh | Method for treating fertility defects |
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| DE10040700A1 (en) * | 2000-08-17 | 2002-02-28 | Asta Medica Ag | Salts of biologically active peptides, their production and use |
| DE10157628A1 (en) * | 2001-11-26 | 2003-06-12 | Zentaris Ag | Solution for injection of an LHRH antagonist |
| US20030186892A1 (en) * | 2002-03-28 | 2003-10-02 | Rajneesh Taneja | Enhancement of endogenous gonadotropin production |
| PL208073B1 (en) | 2002-09-27 | 2011-03-31 | Aeterna Zentaris Gmbh | Administration form for pharmaceutically active peptides with sustained release and method for the production thereof |
| DE602005004014T2 (en) | 2004-03-12 | 2008-12-11 | Intercell Ag | PROCESS FOR SOLUBILIZING PEPTIDE MIXTURES |
| EP1674082A1 (en) | 2004-12-22 | 2006-06-28 | Zentaris GmbH | Process for the manufacture of sterile suspensions or lyophilisates of low-soluble basic peptide complexes, pharmaceutical formulations comprising these complexes and their use as medicament |
| JOP20090061B1 (en) * | 2008-02-11 | 2021-08-17 | Ferring Int Center Sa | METHODS OF TREATING PROSTATE CANCER WITH GnRH ANTAGONIST |
| CN101630607B (en) * | 2008-07-19 | 2012-04-25 | 浙江家泰电器制造有限公司 | Liquid heating ware overheating protection controller assembly |
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| RU2454221C2 (en) * | 2010-07-06 | 2012-06-27 | Общество с ограниченной ответственностью "Завод Медсинтез" | Method for preparing lyophilised antiviral agent |
| BR112013013903A2 (en) | 2010-12-06 | 2016-09-13 | Astron Res Ltd | ready-to-use stable aqueous pharmaceutical preparation of cetrorelix for parenteral administration, process for manufacturing a ready-to-use aqueous stable pharmaceutical preparation of cetrorelix for use of cetrorelix for parenteral administration |
| GB201022147D0 (en) * | 2010-12-31 | 2011-02-16 | Immune Targeting Systems Its Ltd | Formulation |
| CN102423484B (en) * | 2011-11-23 | 2014-01-15 | 深圳翰宇药业股份有限公司 | Stable cetrorelix medicinal composition and preparation method thereof |
| EP3015553A1 (en) | 2014-10-30 | 2016-05-04 | Biotecon Diagnostics GmbH | Stabilised reaction mixture |
| RU2667128C2 (en) * | 2016-12-29 | 2018-09-14 | Герман Петрович Беккер | Composition for preparation of anti-tumor medication and method for preparation of anti-tumor medication based on it |
| CN114096266A (en) | 2019-06-17 | 2022-02-25 | 印塔斯制药有限公司 | Stable formulations of cetrorelix |
| CN112717119B (en) * | 2021-01-27 | 2024-04-30 | 南京羚诺生物医药技术研究院有限公司 | Cetrorelix pharmaceutical composition and preparation method thereof |
| US20240123021A1 (en) | 2021-06-25 | 2024-04-18 | Extrovis Ag | Pharmaceutical compositions |
| CN114159544A (en) * | 2022-01-24 | 2022-03-11 | 福州华为医药技术开发有限公司 | Cetrorelix acetate for injection and preparation method thereof |
| CN115969954A (en) * | 2023-01-09 | 2023-04-18 | 开封明仁药业有限公司 | A kind of cetrorelix freeze-dried pharmaceutical composition for injection and preparation method thereof |
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-
1993
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1994
- 1994-01-31 TW TW083100769A patent/TW387812B/en not_active IP Right Cessation
- 1994-02-04 EP EP99102340.9A patent/EP0947200B1/en not_active Expired - Lifetime
- 1994-02-04 DE DE59409389T patent/DE59409389D1/en not_active Expired - Lifetime
- 1994-02-04 EP EP94101672A patent/EP0611572B1/en not_active Expired - Lifetime
- 1994-02-04 AT AT94101672T patent/ATE193653T1/en active
- 1994-02-04 PT PT94101672T patent/PT611572E/en unknown
- 1994-02-04 ES ES94101672T patent/ES2148247T3/en not_active Expired - Lifetime
- 1994-02-04 SG SG1996006874A patent/SG46632A1/en unknown
- 1994-02-04 DK DK94101672T patent/DK0611572T3/en active
- 1994-02-14 CZ CZ94312A patent/CZ284314B6/en not_active IP Right Cessation
- 1994-02-14 CZ CZ98974A patent/CZ285768B6/en not_active IP Right Cessation
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- 1994-02-18 SK SK810-2001A patent/SK283022B6/en not_active IP Right Cessation
- 1994-02-18 UA UA94005526A patent/UA43829C2/en unknown
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| SP73 | Change of data on owner |
Owner name: ZENTARIS GMBH; DE Effective date: 20060526 |
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| SP73 | Change of data on owner |
Owner name: ZENTARIS IVF GMBH; DE Effective date: 20090424 |