CA2115943C - Novel process for the preparation of cetrorelix lyophilisate - Google Patents
Novel process for the preparation of cetrorelix lyophilisate Download PDFInfo
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- CA2115943C CA2115943C CA002115943A CA2115943A CA2115943C CA 2115943 C CA2115943 C CA 2115943C CA 002115943 A CA002115943 A CA 002115943A CA 2115943 A CA2115943 A CA 2115943A CA 2115943 C CA2115943 C CA 2115943C
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- cetrorelix
- lyophilisate
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- acetic acid
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/06—Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite
- A61K47/26—Carbohydrates, e.g. sugar alcohols, amino sugars, nucleic acids, mono-, di- or oligo-saccharides; Derivatives thereof, e.g. polysorbates, sorbitan fatty acid esters or glycyrrhizin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K38/00—Medicinal preparations containing peptides
- A61K38/04—Peptides having up to 20 amino acids in a fully defined sequence; Derivatives thereof
- A61K38/08—Peptides having 5 to 11 amino acids
- A61K38/09—Luteinising hormone-releasing hormone [LHRH], i.e. Gonadotropin-releasing hormone [GnRH]; Related peptides
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/0012—Galenical forms characterised by the site of application
- A61K9/0019—Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
- A61K9/19—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles lyophilised, i.e. freeze-dried, solutions or dispersions
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P13/00—Drugs for disorders of the urinary system
- A61P13/02—Drugs for disorders of the urinary system of urine or of the urinary tract, e.g. urine acidifiers
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P15/00—Drugs for genital or sexual disorders; Contraceptives
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P15/00—Drugs for genital or sexual disorders; Contraceptives
- A61P15/08—Drugs for genital or sexual disorders; Contraceptives for gonadal disorders or for enhancing fertility, e.g. inducers of ovulation or of spermatogenesis
Abstract
A novel lyophilisate and method of preparation as well as the use of the lyophilisate to treat female infertility and for gonad protection. A lyophilisate of a peptide with 3 - 15 amino acids and optionally one or several bulking agents is prepared by dissolving 1 part by weight of peptide in 100 - 10,000 parts by weight of acetic acid and then transferring to water, the solution so obtained being lyophilized. Cetrorelix is preferred as the peptide.
Description
2115~~~
Cetrorelix is a decapeptide with a terminal acid amide group that is used as an acetate salt. The synthesis and some pharmacological effects are described in published European Patent Application 299 402.
It should be possible to administer the active substance subcutaneously in a dose of 0.1 to 20 mg. Aqueous solutions of the decapeptide are unstable, autoclaving in the final container is not possible. With conventional sterilization according to the prescribed conditions the decapeptide tends to decompose. To obtain an injectable solution it was therefore necessary to develop a lyophilisate.
The amount of active substance in the solution to be lyophilized is, however, so small that, in low active substance concentrations, only a loose fluf:~ results on the glass wall of the ampoule after drying the solution free of auxiliary substances and this fluff is carried out of the vial with the stream of steam used for sterilization purposes. It is therefore necessary to use a bulking agent that forms a stable cake. In high concentrations this auxiliary substance can be dispensed with. The following auxiliary substances may be considered as bulking agentss hexitols, in particular mannitol, glucitol, sorbitol, such as D-sorbitol, dulcitol, allitol, altritol (for example D- and L-altritol), iditol (for example D- and L-iditol), their optically active forms (D- and L-foams) as well as the corresponding racemates. Mannitol is used in particular, such as D-mannitol, L-mannitol, DL-mannitol, sorbitol and/or dulcitol and of these preferably D-mannitol. The hexitol used may also be mixtures of the hexitols named, for example mixtures of mannitol and sorbitol and/or dulcitol. Since dulcitol is less water soluble than, for example, mannitol, the dulcitol content in the aqueous solution should not exceed for example 3 percent by weight. Mannitol and sorbitol, on the other hand, can for example be mixed in any ~5 ratio.
21~~943 _ 2 Apart from hexitol it is also possible to add other, conventional pharmaceutical auxiliary substances, such as amino acids, such as alanine, glycine, lysine, phenylalanine, asparaginic acid, glutaminic acid, leucine, lactose, polyvinylpyrrolidone, glucose, fructose, albumin and equivalent bulking agents. Urea and sodium chloride may also be used as bulking agents. The total amount of such substances in the solution which is used for freeze-drying, is for example 0 -16.9 parts by weight, for example 0.1 - 7 parts by weight, based on 1 part by weight of cetrorelix. In the finished lyophilisate the total amount of such auxiliary substances may be up to 16.9 parts by weight, based on one part by weight of hexitol. In detail, the amount of such auxiliary substances depends on the amount of hexitol present and to such an extent that the total amount of hexitol and such other auxiliary substances in the finished lyophilisate may not be more than a maximum of 17 parts by weight, based on 1 part by weight of cetrorelix. If only 0.1 part by weight of hexitol is present in the lyophilisate, it is thus possible to have up to 16.9 parts by weight of other auxiliary substances; if, for example, 8.5 parts by weight of hexitol are present, the amount of other auxiliary substances may for example be up to 8.5 parts by weight, based an 1 part by weight of cetrorelix.
It was, however, found during development work on the lyophilisate that the active substance behaves in a widely different and unpredictable, manner during processing. The first batches gave good results, but it soon transpired that difficulties occurred during sterile filtration and faulty batches resulted.
It is known from the literature, for example from powell, M.F.;
Pharmaceutical research, 1258-1263 (8)1991; Dathe, M: Int. J.
Peptide Protein Res. 3~4-3~9 (36) 1990; Szejtli, J.:
Pharmaceutical Technology International 16-22, 1991 that oligopeptides, particularly those with terminal acid amide function, tend to form gels. During sterile filtration this is apparent from the speed of filtration, indeed, the increased viscosity of such solutions can often already be detected organoleptically. ~ gelatinous layer remains on the sterile filter. Tt is then no longer possible to prepare a medicament pith an exactly defined active substance content.
Table 1 lists various results of the first 11 batches.
The active suLStance contents fluctuate between 100 and 36~.
Table 1: Cetrorelix acetate Batch Dosage active substance content 1 100 ug 100 2 500 ug 100 3 500 ug 90 4 500 ug $6 500 ug 100 6 500 ug 85 7 1 mg 80 8 1 mg 100 9 2 mg 100 2 mg 80 11 2 mg 100 21~ ~~~~~
To avoid this gel formation, the literature lists the following additives which may be tried out on an experimental basis:
Organic solvents may be considered, for example acetonitrile, n-butanol, tertiary butanol, ethanol, isopropanol, octanol and benzyl alcohol. It is also possible to use salts and buffer solutions, such as acetate buffer, citrate buffer, sodium chloride, sodium phosphate, sodium ~DTA, sodium bicarbonate, phosphate buffer, guanidine acetate, urea.
polymers may also be used, such as gelatin, polyethylene glycol X00, hydraxyethyl starch, polyvinylpyrxalidone, polyvinyl alcohol. The use of amino acids, for examp:Le alanine, glycine, lysine, phenylalanine, asparaginic acid, g:Lutaminic acid and leucine has also been described.
Acids that were used were citric acid, caprylic acid, octanic acid, hydrochloric acid, sulphuric acid and acetic acid.
physiologically acceptable tensides that may be used are benzalDsonium chloride, cetyl alcohol, bile acids, lecithins, polysorbates, Spans{R~ said pluronicscR).
Carbohydrates and cyclodextrines such as glucose, lactose, mannitol, saccharose, alpha-, beta- and gamma gyclodextrins, hydroxypropyl-alpha- and beta-cyclodextrins, hydroxyethyl cyclodextrins and methyl cycladextrins have already been used.
These auxiliary substances were tested as filtration supporting agents to prevent gel formation.
ri1a satisfactory solution of, the problem could, however, be found. Only acidification with acetic acid showed partial success, Mere, too, it was, however, always necessary to accept high filtration losses. It was then surprisingly found that cetrorelix can be easily dissolved in 30~ volume/valume acetic acid. The solution is then filled up to a final concentration of 3~ cetrare.lix with water for injection purposes and mannitol is added, Although it is stated in the literature that the terminal amide group hydrolyses easily in acid medium, this was not found in the case of cetrorelix. Solutions prepared according to this method caused no difficulties during filtration. The correct amounts of active substance were always found.
The filtration speed attains values that ensure satisfactory production sequences. A general process for sterile lyophilisation is describeo: in pages 557 - 559 of Sucker, Fuchs and Speiser (Publishers) "F~harmazeutisch~=_ Technologie" 2nd edition 1991, Thieme-Verlag, Stuttgart-New York. A further description of the lyophilisation process used is given in German published specification (DOS) 37 35 614.
The lyophilisate is used :ire the treatment of female sterility.
One therapeutic process hae; hitherto consisted in stimulating follicle maturation using human menopause gonadotrophin and then triggering ovulation by administering human chorion gonadotrophin.
The ovulation triggered thereby occurred 32 hours later. The ova collected thereby are available for in vitro fertilisation.
A disadvantage of this trea..tment with agonists is the fact that up to 10 follicles mature during the stimulation phase. This elevated follicle maturat:ic>n leads to hormone level peaks in the LH. These peaks result in an early stage of follicle maturation and ovulation at an unpredi.eted point in time. This impaired ovulation occurs in about ~5% of treated cases and is a disadvantage since the cycle that displays disturbed ovulation of this kind cannot be used for the collection of ova and the entire treatment has to be repeated about 1 month later.
Another disadvantage of the conventional simulation treatment is the long treatment duration of 4 weeks which is needed to achieve satisfactory suppression. The agonists continue to display a hyperstimulation syndrome in 1-2% of cases in which the follicle cells hypertrophy. The ri~~k of hyperstimulation is particularly great in the case of polyc~rstic ovaries. The hyperstimulat.ion syndrome is a severe side effect which can lead to fatalities.
- 5a -The present invention provides a lyophilisate of cetrorelix and optionally one or more bull~:ing agents. The lyophilisate is obtained by a process comprising dissolving 1 part per weight of cetrorelix in 100 to 10,000 parts by weight of acetic acid, diluting the cetrorelix/acetic acid solution with water, optionally, adding a bulking agent, and lyophilising the resulting solution.
The present invention also provides a process for the preparation of a sterile cetrorelix lyophilisate, in which cetrorelix is (Ac-D-Nal (2) 1, D-phe (4C1) z, D-PaL (3) 3, D-Cit6, D-Alal°) -LHRH, wherein cetrorelix is dissolved in aqueous acetic acid in the ratio 1:100-10,000 wt/wt, the solution 1S diluted with water, if required a wilder is added, and the :solution is sterile-filtered, filled into injection vials and :Lyophilised.
T'he cetrorelix being dissolved can be in the form of an acetate salt.
It has now been found that the antagonist cetrorelix displays the following advantages in this particular treatment:
_ 5 _ Treatment with cetrorelix over 5 days is sufficient to achieve total suppression. The hyperstimulation syndrome cannot arise.
In addition, less HMG is used in the 2nd phase of therapy, the ovulation triggering phase. This gives this in-vitro fertilisation treatment a not inconsiderable cost advantage.
In-vitro fertilisation is, for example, used when a tube anomaly is present. To perform this treatment it is necessary to precisely monitor the cycle and to establish the time of ovulation as precisely as possible. This has hitherto only been achieved to a limited extent since preovulatory LH increase often occurred too early due to simulation with HMG/HCG, or was not maintained for a sufficiently long period. Avoidance of this premature increase is, however, of critical importance for the success of the treatment in order to precisely determine the time of fertilisation. This reduces the physical and mental burden on the patient and makes optimum use of hospital logistics. To achieve this objective with great reliability it is necessary to suppress endogenous hormone production (LH-FSH, aestradiol) as completely as possible in order to simultaneously stimulate follicle maturation through administration of exogenous gonadotrophins (HMG/HCG) and to monitor the hormone status at any time. It is only when a sufficiently large number of follicles have been achieved (4-6), having approximately the same degree of maturation, that ovulation is triggered by administering an HCG bolus injection.
Use of an antagonist makes treatment substantially more successful and safer for the patient.
Another area of use of the cetrorelix lyophilisate according to the present invention is to protect the gonads in male patients.
Male patients are pre-treated with cetrorelix lyophilisate and the activity of the gonads is reinforced. As a result, other harmful noxious agents, such as radiation therapy or treatment with cytostatics, have no or only a small possibility of affecting the sensitive tissue of the gonads.
Example of the method of preparatian~
211~94~
Approx. 1.5 litres of water for injection purposes are prepared in a suitable glass vessel. 210 g water for injection purposes are prepared in another glass vessel and 91.17 g acetic acid are added. The amount of cetrorelix acetate calculated (1.62 - 1.695 g, depending on the content of the batch used) is dissolved in the prepared 30~ acetic acid with stirring. This salution is transferred to the glass vessel with 1.5 litres of water for injection purposes, 82.2 g mannitol are added, dissolved and made up to 3039 g with water for injection purposes.
In-process checks:
pFI value : 2 . 5 - 3 . 0 Density: 1.009 - 1.017 g/cm3 at 20°C
Refractive index: 1.227 - 1.340 at 440 nm and 20°C
The solution is sterilised by filtration through an appropriate membrane filter (pore size 0.2 um) under aseptic conditions. 100 ml first runnings should be discarded. The filters should be sterilised with superheated steam. Cetrorelix freeze-dried solution should be protected from recontamination during storage.
The solution is immediately filled into colourless injection bottles DIN 2R, hydrolytic class I under aseptic conditions and provided with sterile freeze-drying stoppers. The nominal filling amount is 2.0 ml = 2.026 g.
The 2 ml injection bottles were rinsed in an injection bottle washing machine, dried with hot air and sterilised. The cleaned freeze-drying stoppers were autoclaved. 'Phe closed injection bottles were transferred to a freeze-drying installation .and frozen at a plate temperature of -40°C. Drying was carried out using a drying programme with a plate temperature of -40°C
rising to +20°C. rfhe installation is then flooded with sterile nitrogen, the bottles are closed in the installation and 'the stoppers secured with crimped caps.
_ g _ The injection bottles are checked visually for faulty closures and outer faults. Faulty injection bottles are removed and destroyed.
Cetrorelix lyophilisate 1 mg is a white, solid, freeze-dried cake in a colourless 2 ml injection bottle which is closed with grey freeze-drying stoppers and yellow flip-off crimped caps.
Cetrorelix is a decapeptide with a terminal acid amide group that is used as an acetate salt. The synthesis and some pharmacological effects are described in published European Patent Application 299 402.
It should be possible to administer the active substance subcutaneously in a dose of 0.1 to 20 mg. Aqueous solutions of the decapeptide are unstable, autoclaving in the final container is not possible. With conventional sterilization according to the prescribed conditions the decapeptide tends to decompose. To obtain an injectable solution it was therefore necessary to develop a lyophilisate.
The amount of active substance in the solution to be lyophilized is, however, so small that, in low active substance concentrations, only a loose fluf:~ results on the glass wall of the ampoule after drying the solution free of auxiliary substances and this fluff is carried out of the vial with the stream of steam used for sterilization purposes. It is therefore necessary to use a bulking agent that forms a stable cake. In high concentrations this auxiliary substance can be dispensed with. The following auxiliary substances may be considered as bulking agentss hexitols, in particular mannitol, glucitol, sorbitol, such as D-sorbitol, dulcitol, allitol, altritol (for example D- and L-altritol), iditol (for example D- and L-iditol), their optically active forms (D- and L-foams) as well as the corresponding racemates. Mannitol is used in particular, such as D-mannitol, L-mannitol, DL-mannitol, sorbitol and/or dulcitol and of these preferably D-mannitol. The hexitol used may also be mixtures of the hexitols named, for example mixtures of mannitol and sorbitol and/or dulcitol. Since dulcitol is less water soluble than, for example, mannitol, the dulcitol content in the aqueous solution should not exceed for example 3 percent by weight. Mannitol and sorbitol, on the other hand, can for example be mixed in any ~5 ratio.
21~~943 _ 2 Apart from hexitol it is also possible to add other, conventional pharmaceutical auxiliary substances, such as amino acids, such as alanine, glycine, lysine, phenylalanine, asparaginic acid, glutaminic acid, leucine, lactose, polyvinylpyrrolidone, glucose, fructose, albumin and equivalent bulking agents. Urea and sodium chloride may also be used as bulking agents. The total amount of such substances in the solution which is used for freeze-drying, is for example 0 -16.9 parts by weight, for example 0.1 - 7 parts by weight, based on 1 part by weight of cetrorelix. In the finished lyophilisate the total amount of such auxiliary substances may be up to 16.9 parts by weight, based on one part by weight of hexitol. In detail, the amount of such auxiliary substances depends on the amount of hexitol present and to such an extent that the total amount of hexitol and such other auxiliary substances in the finished lyophilisate may not be more than a maximum of 17 parts by weight, based on 1 part by weight of cetrorelix. If only 0.1 part by weight of hexitol is present in the lyophilisate, it is thus possible to have up to 16.9 parts by weight of other auxiliary substances; if, for example, 8.5 parts by weight of hexitol are present, the amount of other auxiliary substances may for example be up to 8.5 parts by weight, based an 1 part by weight of cetrorelix.
It was, however, found during development work on the lyophilisate that the active substance behaves in a widely different and unpredictable, manner during processing. The first batches gave good results, but it soon transpired that difficulties occurred during sterile filtration and faulty batches resulted.
It is known from the literature, for example from powell, M.F.;
Pharmaceutical research, 1258-1263 (8)1991; Dathe, M: Int. J.
Peptide Protein Res. 3~4-3~9 (36) 1990; Szejtli, J.:
Pharmaceutical Technology International 16-22, 1991 that oligopeptides, particularly those with terminal acid amide function, tend to form gels. During sterile filtration this is apparent from the speed of filtration, indeed, the increased viscosity of such solutions can often already be detected organoleptically. ~ gelatinous layer remains on the sterile filter. Tt is then no longer possible to prepare a medicament pith an exactly defined active substance content.
Table 1 lists various results of the first 11 batches.
The active suLStance contents fluctuate between 100 and 36~.
Table 1: Cetrorelix acetate Batch Dosage active substance content 1 100 ug 100 2 500 ug 100 3 500 ug 90 4 500 ug $6 500 ug 100 6 500 ug 85 7 1 mg 80 8 1 mg 100 9 2 mg 100 2 mg 80 11 2 mg 100 21~ ~~~~~
To avoid this gel formation, the literature lists the following additives which may be tried out on an experimental basis:
Organic solvents may be considered, for example acetonitrile, n-butanol, tertiary butanol, ethanol, isopropanol, octanol and benzyl alcohol. It is also possible to use salts and buffer solutions, such as acetate buffer, citrate buffer, sodium chloride, sodium phosphate, sodium ~DTA, sodium bicarbonate, phosphate buffer, guanidine acetate, urea.
polymers may also be used, such as gelatin, polyethylene glycol X00, hydraxyethyl starch, polyvinylpyrxalidone, polyvinyl alcohol. The use of amino acids, for examp:Le alanine, glycine, lysine, phenylalanine, asparaginic acid, g:Lutaminic acid and leucine has also been described.
Acids that were used were citric acid, caprylic acid, octanic acid, hydrochloric acid, sulphuric acid and acetic acid.
physiologically acceptable tensides that may be used are benzalDsonium chloride, cetyl alcohol, bile acids, lecithins, polysorbates, Spans{R~ said pluronicscR).
Carbohydrates and cyclodextrines such as glucose, lactose, mannitol, saccharose, alpha-, beta- and gamma gyclodextrins, hydroxypropyl-alpha- and beta-cyclodextrins, hydroxyethyl cyclodextrins and methyl cycladextrins have already been used.
These auxiliary substances were tested as filtration supporting agents to prevent gel formation.
ri1a satisfactory solution of, the problem could, however, be found. Only acidification with acetic acid showed partial success, Mere, too, it was, however, always necessary to accept high filtration losses. It was then surprisingly found that cetrorelix can be easily dissolved in 30~ volume/valume acetic acid. The solution is then filled up to a final concentration of 3~ cetrare.lix with water for injection purposes and mannitol is added, Although it is stated in the literature that the terminal amide group hydrolyses easily in acid medium, this was not found in the case of cetrorelix. Solutions prepared according to this method caused no difficulties during filtration. The correct amounts of active substance were always found.
The filtration speed attains values that ensure satisfactory production sequences. A general process for sterile lyophilisation is describeo: in pages 557 - 559 of Sucker, Fuchs and Speiser (Publishers) "F~harmazeutisch~=_ Technologie" 2nd edition 1991, Thieme-Verlag, Stuttgart-New York. A further description of the lyophilisation process used is given in German published specification (DOS) 37 35 614.
The lyophilisate is used :ire the treatment of female sterility.
One therapeutic process hae; hitherto consisted in stimulating follicle maturation using human menopause gonadotrophin and then triggering ovulation by administering human chorion gonadotrophin.
The ovulation triggered thereby occurred 32 hours later. The ova collected thereby are available for in vitro fertilisation.
A disadvantage of this trea..tment with agonists is the fact that up to 10 follicles mature during the stimulation phase. This elevated follicle maturat:ic>n leads to hormone level peaks in the LH. These peaks result in an early stage of follicle maturation and ovulation at an unpredi.eted point in time. This impaired ovulation occurs in about ~5% of treated cases and is a disadvantage since the cycle that displays disturbed ovulation of this kind cannot be used for the collection of ova and the entire treatment has to be repeated about 1 month later.
Another disadvantage of the conventional simulation treatment is the long treatment duration of 4 weeks which is needed to achieve satisfactory suppression. The agonists continue to display a hyperstimulation syndrome in 1-2% of cases in which the follicle cells hypertrophy. The ri~~k of hyperstimulation is particularly great in the case of polyc~rstic ovaries. The hyperstimulat.ion syndrome is a severe side effect which can lead to fatalities.
- 5a -The present invention provides a lyophilisate of cetrorelix and optionally one or more bull~:ing agents. The lyophilisate is obtained by a process comprising dissolving 1 part per weight of cetrorelix in 100 to 10,000 parts by weight of acetic acid, diluting the cetrorelix/acetic acid solution with water, optionally, adding a bulking agent, and lyophilising the resulting solution.
The present invention also provides a process for the preparation of a sterile cetrorelix lyophilisate, in which cetrorelix is (Ac-D-Nal (2) 1, D-phe (4C1) z, D-PaL (3) 3, D-Cit6, D-Alal°) -LHRH, wherein cetrorelix is dissolved in aqueous acetic acid in the ratio 1:100-10,000 wt/wt, the solution 1S diluted with water, if required a wilder is added, and the :solution is sterile-filtered, filled into injection vials and :Lyophilised.
T'he cetrorelix being dissolved can be in the form of an acetate salt.
It has now been found that the antagonist cetrorelix displays the following advantages in this particular treatment:
_ 5 _ Treatment with cetrorelix over 5 days is sufficient to achieve total suppression. The hyperstimulation syndrome cannot arise.
In addition, less HMG is used in the 2nd phase of therapy, the ovulation triggering phase. This gives this in-vitro fertilisation treatment a not inconsiderable cost advantage.
In-vitro fertilisation is, for example, used when a tube anomaly is present. To perform this treatment it is necessary to precisely monitor the cycle and to establish the time of ovulation as precisely as possible. This has hitherto only been achieved to a limited extent since preovulatory LH increase often occurred too early due to simulation with HMG/HCG, or was not maintained for a sufficiently long period. Avoidance of this premature increase is, however, of critical importance for the success of the treatment in order to precisely determine the time of fertilisation. This reduces the physical and mental burden on the patient and makes optimum use of hospital logistics. To achieve this objective with great reliability it is necessary to suppress endogenous hormone production (LH-FSH, aestradiol) as completely as possible in order to simultaneously stimulate follicle maturation through administration of exogenous gonadotrophins (HMG/HCG) and to monitor the hormone status at any time. It is only when a sufficiently large number of follicles have been achieved (4-6), having approximately the same degree of maturation, that ovulation is triggered by administering an HCG bolus injection.
Use of an antagonist makes treatment substantially more successful and safer for the patient.
Another area of use of the cetrorelix lyophilisate according to the present invention is to protect the gonads in male patients.
Male patients are pre-treated with cetrorelix lyophilisate and the activity of the gonads is reinforced. As a result, other harmful noxious agents, such as radiation therapy or treatment with cytostatics, have no or only a small possibility of affecting the sensitive tissue of the gonads.
Example of the method of preparatian~
211~94~
Approx. 1.5 litres of water for injection purposes are prepared in a suitable glass vessel. 210 g water for injection purposes are prepared in another glass vessel and 91.17 g acetic acid are added. The amount of cetrorelix acetate calculated (1.62 - 1.695 g, depending on the content of the batch used) is dissolved in the prepared 30~ acetic acid with stirring. This salution is transferred to the glass vessel with 1.5 litres of water for injection purposes, 82.2 g mannitol are added, dissolved and made up to 3039 g with water for injection purposes.
In-process checks:
pFI value : 2 . 5 - 3 . 0 Density: 1.009 - 1.017 g/cm3 at 20°C
Refractive index: 1.227 - 1.340 at 440 nm and 20°C
The solution is sterilised by filtration through an appropriate membrane filter (pore size 0.2 um) under aseptic conditions. 100 ml first runnings should be discarded. The filters should be sterilised with superheated steam. Cetrorelix freeze-dried solution should be protected from recontamination during storage.
The solution is immediately filled into colourless injection bottles DIN 2R, hydrolytic class I under aseptic conditions and provided with sterile freeze-drying stoppers. The nominal filling amount is 2.0 ml = 2.026 g.
The 2 ml injection bottles were rinsed in an injection bottle washing machine, dried with hot air and sterilised. The cleaned freeze-drying stoppers were autoclaved. 'Phe closed injection bottles were transferred to a freeze-drying installation .and frozen at a plate temperature of -40°C. Drying was carried out using a drying programme with a plate temperature of -40°C
rising to +20°C. rfhe installation is then flooded with sterile nitrogen, the bottles are closed in the installation and 'the stoppers secured with crimped caps.
_ g _ The injection bottles are checked visually for faulty closures and outer faults. Faulty injection bottles are removed and destroyed.
Cetrorelix lyophilisate 1 mg is a white, solid, freeze-dried cake in a colourless 2 ml injection bottle which is closed with grey freeze-drying stoppers and yellow flip-off crimped caps.
Claims (10)
1. A lyophilisate of cetrorelix and optionally one or more bulking agents, wherein the lyophilisate is obtained by a process comprising:
dissolving 1 part per weight of cetrorelix in 100 to 10,000 parts by weight of acetic acid;
diluting the cetrorelix/acetic acid solution with water;
optionally, adding a bulking agent; and lyophilising the resulting solution.
dissolving 1 part per weight of cetrorelix in 100 to 10,000 parts by weight of acetic acid;
diluting the cetrorelix/acetic acid solution with water;
optionally, adding a bulking agent; and lyophilising the resulting solution.
2. A lyophilisate according to claim 1, wherein the cetrorelix being dissolved is in the form of an acetate salt.
3. A lyophilisate according to claim 1 or 2, wherein the bulking agent is mannitol.
4. A lyophilisate according to claim 1, 2 or 3, wherein the solution is sterile-filtered before lyophilisation.
5. Use of the lyophilisate according to any one of claims 1 to 4, for the treatment of female infertility.
6. Use of the lyophilisate according to any one of claims 1 to 4, for gonad protection.
7. Use of the lyophilisate according to any one of claims 1 to 4, to prepare a medicament for the treatment of female infertility.
8. Use of the lyophilisate according to any one of claims 1 to 4, to prepare a medicament for gonad protection.
9. Process for the preparation of a sterile cetrorelix lyophilisate, in which cetrorelix is (Ac-D-Nal(2)1, D-phe (4Cl)2, D-PaL(3)3, D-Cit6, D-Ala10) -LHRH, wherein cetrorelix is dissolved in aqueous acetic acid in the ratio 1:100-10,000 wt/wt, the solution is diluted with water, if required a builder is added, and the solution is sterile-filtered, filled into injection vials and lyophilised.
10. The process according to claim 9, wherein the cetrorelix being dissolved is in the form of an acetate salt.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4305225A DE4305225A1 (en) | 1993-02-19 | 1993-02-19 | New manufacturing process for Cetrorelix lyophilisate |
| DEP4305225.8 | 1993-02-19 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2115943A1 CA2115943A1 (en) | 1994-08-20 |
| CA2115943C true CA2115943C (en) | 2003-08-05 |
Family
ID=6480924
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002115943A Expired - Lifetime CA2115943C (en) | 1993-02-19 | 1994-02-18 | Novel process for the preparation of cetrorelix lyophilisate |
Country Status (29)
| Country | Link |
|---|---|
| EP (2) | EP0947200B1 (en) |
| JP (1) | JP4033919B2 (en) |
| KR (2) | KR100355686B1 (en) |
| CN (1) | CN1109557C (en) |
| AT (1) | ATE193653T1 (en) |
| AU (1) | AU671881C (en) |
| BR (1) | BR9400617A (en) |
| CA (1) | CA2115943C (en) |
| CZ (2) | CZ284314B6 (en) |
| DE (2) | DE4305225A1 (en) |
| DK (1) | DK0611572T3 (en) |
| 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) | NZ314707A (en) |
| PL (1) | PL177177B1 (en) |
| PT (1) | PT611572E (en) |
| RU (1) | RU2145234C1 (en) |
| SG (1) | SG46632A1 (en) |
| SI (1) | SI9400087B (en) |
| SK (2) | SK283021B6 (en) |
| TW (1) | TW387812B (en) |
| UA (1) | UA43829C2 (en) |
| ZA (1) | ZA941136B (en) |
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| US6828415B2 (en) * | 1993-02-19 | 2004-12-07 | Zentaris Gmbh | Oligopeptide lyophilisate, their preparation and use |
| AR006598A1 (en) * | 1996-04-19 | 1999-09-08 | Merck Sharp & Dohme | "ANTI-FUNGOUS COMPOSITIONS, ITS USE IN THE MANUFACTURE OF MEDICINES AND A PROCEDURE FOR THE PREPARATION" |
| DE19712718C2 (en) * | 1997-03-26 | 1999-09-23 | Asta Medica Ag | Immobilized and activity-stabilized complexes of LHRH antagonists and process for their preparation |
| SI1082129T1 (en) * | 1998-04-23 | 2004-02-29 | Zentaris Gmbh | Method for the treatment of fertility disorders |
| DE10024451A1 (en) * | 2000-05-18 | 2001-11-29 | Asta Medica Ag | Pharmaceutical dosage form for peptides, process for their preparation and use |
| DE10040700A1 (en) * | 2000-08-17 | 2002-02-28 | Asta Medica Ag | Salts of biologically active peptides, their production and use |
| US20030186892A1 (en) * | 2002-03-28 | 2003-10-02 | Rajneesh Taneja | Enhancement of endogenous gonadotropin production |
| DK1565160T3 (en) | 2002-09-27 | 2014-04-28 | Terna Zentaris Gmbh | Method of administration for sustained release pharmaceutically active peptides and a process for their preparation |
| EP1987843A3 (en) | 2004-03-12 | 2011-10-26 | Intercell AG | Method for solubilising 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 |
| CN101629758B (en) * | 2008-07-19 | 2012-09-26 | 浙江家泰电器制造有限公司 | Liquid heating ware overheating protection controller assembly |
| 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 |
| 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 |
| US20220233631A1 (en) | 2019-06-17 | 2022-07-28 | Intas Pharmaceuticals Ltd. | Stable formulation of cetrorelix |
| CN112717119A (en) * | 2021-01-27 | 2021-04-30 | 南京康舟医药科技有限公司 | Cetrorelix pharmaceutical composition and preparation method thereof |
| EP4164608A1 (en) | 2021-06-25 | 2023-04-19 | 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 |
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| US3816386A (en) * | 1972-06-20 | 1974-06-11 | Abbott Lab | Purification process for gn-rh |
| DD141996A1 (en) * | 1979-02-21 | 1980-06-04 | Ingrid Wolf | METHOD FOR PRODUCING LYOPHILIZED LHRH PRAEPARATIONS |
| CS230614B1 (en) * | 1982-08-06 | 1984-08-13 | Martin Cs Flegel | Analogues of realising factor for luteining and folliculstimulated hormon |
| US4565804A (en) * | 1984-09-07 | 1986-01-21 | The Salk Institute For Biological Studies | GnRH Antagonists VI |
| EP0268066A3 (en) * | 1986-10-17 | 1990-07-11 | Syntex (U.S.A.) Inc. | Fertility control and uterine therapy in dogs with luteinizing hormone releasing hormone antagonists |
| DE3735614A1 (en) * | 1986-10-31 | 1988-07-28 | Asta Pharma Ag | Ifosfamide lyophilisate and process for its preparation |
| US4801577A (en) * | 1987-02-05 | 1989-01-31 | Syntex (U.S.A.) Inc. | Nonapeptide and decapeptide analogs of LHRH useful as LHRH antagonists |
| US4800191A (en) * | 1987-07-17 | 1989-01-24 | Schally Andrew Victor | LHRH antagonists |
| NZ226170A (en) * | 1987-09-18 | 1990-07-26 | Ethicon Inc | Stable freeze-dried pharmaceutical composition containing epidermal growth factor |
| US5180711A (en) * | 1990-06-14 | 1993-01-19 | Applied Research Systems Ars Holding N.V. | Combined treatment with gnrh antagonist and gnrh to control gonadotropin levels in mammals |
| CN1036343C (en) * | 1990-11-10 | 1997-11-05 | 天津市计划生育研究所 | Synthesis, products and its application for luleinizing hormone releasing hormone and antagonistic znalogue |
-
1993
- 1993-02-19 DE DE4305225A patent/DE4305225A1/en not_active Ceased
-
1994
- 1994-01-31 TW TW083100769A patent/TW387812B/en not_active IP Right Cessation
- 1994-02-04 SG SG1996006874A patent/SG46632A1/en unknown
- 1994-02-04 DE DE59409389T patent/DE59409389D1/en not_active Expired - Lifetime
- 1994-02-04 EP EP99102340.9A patent/EP0947200B1/en not_active Expired - Lifetime
- 1994-02-04 PT PT94101672T patent/PT611572E/en unknown
- 1994-02-04 AT AT94101672T patent/ATE193653T1/en active
- 1994-02-04 ES ES94101672T patent/ES2148247T3/en not_active Expired - Lifetime
- 1994-02-04 EP EP94101672A patent/EP0611572B1/en not_active Expired - Lifetime
- 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
- 1994-02-17 AU AU55235/94A patent/AU671881C/en not_active Expired
- 1994-02-17 NZ NZ314707A patent/NZ314707A/en not_active IP Right Cessation
- 1994-02-17 JP JP02053294A patent/JP4033919B2/en not_active Expired - Lifetime
- 1994-02-17 PL PL94302266A patent/PL177177B1/en unknown
- 1994-02-17 NZ NZ250906A patent/NZ250906A/en not_active IP Right Cessation
- 1994-02-17 KR KR1019940002771A patent/KR100355686B1/en not_active IP Right Cessation
- 1994-02-18 HU HU9400481A patent/HU218281B/en unknown
- 1994-02-18 CA CA002115943A patent/CA2115943C/en not_active Expired - Lifetime
- 1994-02-18 BR BR9400617A patent/BR9400617A/en not_active Application Discontinuation
- 1994-02-18 NO NO940564A patent/NO316601B1/en not_active IP Right Cessation
- 1994-02-18 FI FI940779A patent/FI110059B/en not_active IP Right Cessation
- 1994-02-18 SK SK195-94A patent/SK283021B6/en not_active IP Right Cessation
- 1994-02-18 ZA ZA941136A patent/ZA941136B/en unknown
- 1994-02-18 HR HRP4305225.8 patent/HRP940117B1/en not_active IP Right Cessation
- 1994-02-18 UA UA94005526A patent/UA43829C2/en unknown
- 1994-02-18 SI SI9400087A patent/SI9400087B/en unknown
- 1994-02-18 IL IL10870494A patent/IL108704A/en not_active IP Right Cessation
- 1994-02-18 CN CN94101378A patent/CN1109557C/en not_active Expired - Lifetime
- 1994-02-18 SK SK810-2001A patent/SK283022B6/en not_active IP Right Cessation
- 1994-02-18 RU RU94005001A patent/RU2145234C1/en active
- 1994-02-21 MX MX9401312A patent/MX9401312A/en unknown
-
2000
- 2000-08-23 GR GR20000401924T patent/GR3034237T3/en unknown
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2001
- 2001-02-27 KR KR1020010009932A patent/KR100372187B1/en not_active IP Right Cessation
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