Abstract: The present invention provides Crystalline 5-Azacytidine (I) designated as Form-SA-1 and process for preparing thereof. The present application also provides lyophilized formulation comprising crystalline 5-Azacytidine Form-SA-1 useful in the treatment of cancer, and methods of preparing said lyophilized formulation.
CRYSTALLINE 5-AZACYTIDINE AND ITS FORMULATION
The following specification particularly describes the invention and the manner in which it is to be performed.
FIELD OF THE INVENTION
The present invention provides Crystalline 5-Azacytidine designated as Form-SA-1 and process for preparing thereof.
Also provided in the present application, the lyophilized formulation comprising crystalline 5-Azacytidine designated as Form-SA-1, and methods of preparing said lyophilized formulation.
BACK GROUND OF THE INVENTION
5-azacytidine (also known as 4-amino-l-p-D-ribofuranosyl-l, 3, 5-triazin-2(lH)-one) has the structure (I) as mentioned below -OH OH (I)
It is reported to be insoluble in acetone, ethanol, and methyl ethyl ketone, slightly soluble in ethanol and water (50:50), propylene glycol, and polyethylene glycol, sparingly soluble in water, water saturated octanol, 5% dextrose in water, N-methylpyrrolidone, normal saline, and 5% Tween™ 80 in water, and soluble in dimethylsulfoxide (DMSO). Azacitidine is used in the treatment of myelodysplastic syndrome.
5-azacytidine is believed to exert its antineoplastic effects by causing hypomethylation of DNA and direct cytotoxicity on abnormal hematopoietic cells in the bone marrow. Hypomethylation may restore normal functions to genes that are critical for differentiation and proliferation. The cytotoxic effects of azacitidine cause the death of rapidly dividing cells, including cancer cells that are no longer responsive to normal growth control mechanism. Non-proliferating cells are relatively insensitive to azacitidine.
5-Azacitidine (or Azacitidine) underwent NCI-sponsored clinical trials for the treatment of myelodysplastic syndromes (MDS). See Komblith et al., J. Clin. Oncol. 20(10): 2441-2452 (2002) and Silverman et al., J. Clin. Oncol. 20(10): 2429-2440 (2002).
Now, it is commercially available as product containing Azacitidine and is sold as VIDAZA®, 5-azacytidine for injection, by Celgene. The VIDAZA® product received marketing approval in the USA in 2004 and is supplied in sterile lyophilized form for reconstitution as a suspension for subcutaneous injection, or reconstitution as a solution with further dilution for intravenous infusion. Vials of the VIDAZA® product contain 100 mg of azacitidine and 100 mg of mannitol, as a sterile lyophilized powder.
5-Azacytidine is approved for subcutaneous (SC) or intravenous (IV) administration to treat various proliferative disorders. It has been also reported that s-triazine ring of 5-azacytidine has a particular sensitivity towards water as Azacitidine rapidly degrades in aqueous solution via hydrolysis. See, e.g., Beisler, J. Med. Chem., 1978, 21(2), 204-08; Chan, et al., J. Pharm. Sci., 1979, 68(7), 807-12. In an aqueous environment both in vivo and in vitro, 5-azacytidine underwent a spontaneous hydrolysis and resulted in an equilibration with a labile product, n-formylguanyl-ribosylurea, and finally the irreversible formation of guanyl-ribosylurea. Due to this instability, an aqueous formulation was not a viable option to be explored as formulation. Hence, a lyophilized dosage form was developed to minimize water activity in the medicinal product. To minimize azacitidine degradation during product manufacturing, the manufacturing process was developed such that compounding, filtration and filling operations are performed as a continuous process at reduced temperatures.
Dumitru et al in US6,887,855 disclosed that 5-azacytidine exists in at least eight different polymorphic and pseudopolymorphic crystalline forms (Forms I-VIII), in addition to an amorphous form. Form I is a polymorph found in prior art retained samples of 5-azacytidine drug substance. Form II is a polymorph found in some prior art retained samples of the 5-azacytidine drug substance; in those samples, Form II is always found in mixed phase with Form I. Form III is a hydrate, and is formed when prior art retained and current samples of the drug product are reconstituted with water to form a "slurry" prior to administration to the patient. Form VI is found in prior art retained samples of the 5-azacytidine drug product, either substantially free of other polymorphs, or in mixed phase with Form I. The invention provides novel crystalline forms referred to as Form IV, Form V, Form VII and Form VIII. Forms I-VIII each have characteristic X-ray power diffraction (XRPD) patterns and are easily distinguished from one another using XRPD.
Dumitru et al in US7,772,199 disclosed amorphous nature of 5-azacytidine, prepared by a method comprising adding solid 5-azacytidine to a solvent selected from propylene glycol. polyethylene glycol, and DMSO; allowing equilibration to occur; and recovering 5-azacytidine therefrom.
Dumitru et al in US 6,943,249 disclosed methods for isolating crystalline Form I of 5-azacytidine substantially free of other forms, and also pharmaceutical compositions comprising Form I of 5-azacytidine. The method includes isolating crystalline Form I of 5-azacytidine substantially free of other forms, the method comprising: recrystallizing 5-azacytidine from a solvent mixture comprising at least one primary solvent and at least one co-solvent selected from the group consisting of C2 - C5 alcohols, aliphatic ketones, and alkyl cyanides, by cooling said solvent mixture from a temperature selected to allow said 5-azacytidine to dissolve completely to about ambient temperature; and isolating the recrystallized 5-azacytidine.
Arnold et al in US 4,684,630 discloses a method of intravenously injecting an aqueous unstable anticancer agent into a warm-blooded mammal, the agent being selected from the group consisting of 5-azacytosine arabinoside and 5-azacytidine, comprising in combination the following steps:
(a) aqueously diluting a stable, anhydrous organic solution to form an organic-aqueous solution, the organic solution consisting of the agent and a highly water soluble organic solvent selected from the group consisting of dimethylsulfoxide and dimethylacetamide, the organic-aqueous solution having the organic solvent present in a concentration of less than about 5% based on the total weight of the organic-aqueous solution, the organic-aqueous solution being physiologically suitable for intravenous injection into the warm-blooded mammal, the agent being present in the organic-aqueous solution in an effective dosage concentration per unit volume of approximately 1 mg./ml.; and
(b) intravenously injecting the organic-aqueous solution into the warm-blooded mammal; the dilution step occuring immediately prior to the intravenous injection step. U.S. Publication No.2011/0042247 disclose a pharmaceutical formulation of azacitidine, prepared by a process comprising preparing an aqueous solution containing azacitidine at about -3°C to about -1°C; and lyophilizing the solution.
Anthony et al in U.S. Publication No. 2012/0196823 disclose a liquid pharmaceutical composition comprising a cytidine analog selected from 5-azacytidine and Decitabine, and cold sterile water, which is substantially free of impurities.
Kim, Je Hak et al in WO2013/012135 disclose a pre-freeze dried azacitidine preparation, in which azacitidine is dissolved in an aqueous solution comprising 40 to 60 (v/v) % of tertiary butanol, and a method of manufacturing the freeze dried azacitidine preparation. The pre-freeze dried azacitidine preparation of the present invention has improved stability in an aqueous solution. When the pre-freeze dried azacitidine preparation is frozen and dried under predetermined process conditions including a freeze drying cycle, a stability-improved freeze dried azacitidine preparation can be usefully produced.
Despite various disclosures, there still need remains for newer crystalline forms of 5-azacytidine and their lyophilized formulations, to potentially permit, inter alia, convenient administration to patients, limited amount of impurities upon storage, with suitable impurity profile to minimize potential toxicity, and accurate delivery of intended dose of cytidine analogs for treating new diseases or disorders or new patient populations; and/or other potential advantageous benefits.
SUMMARY OF THE INVENTION
Aspects of the present invention relate to a Crystalline 5-Azacytidine designated as Form-SA-1, characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60, 13.90, 15.15 and 31.4 ±0.2 29°.
Aspects of the present invention relate to a Crystalline 5-Azacytidine Form-SA-1 having water content less than 1% w/w.
Aspects of the present invention relate to a process for preparing Crystalline 5-Azacytidine Form SA-1, comprising the steps of-
i) dissolving 5-azacytidine in a solvent vehicle comprising acetonitrile and refrigerated water in the ratio of 20:80 to 60:40.
ii) freeze-drying the solution,
iii) isolating the Crystalline 5-Azacytidine Form SA-1.
Aspects of the present invention relates to a lyophilized formulation of crystalline 5-Azacytidine and an optional bulking agent; wherein the said lyophilized formulation comprising crystalline 5-Azacytidine is Form-SA-1, characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60,13.90,15.15 and 31.4 ±0.2 20°.
Aspects of the present invention relate to a lyophilized formulation of crystalline 5-Azacytidine and a bulking agent selected from mannitol, sorbitol, lactose, sucrose, or any mixtures of two or more thereof; wherein the said lyophilized formulation comprising crystalline 5-Azacytidine is Form-SA-1, characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60, 13.90, 15.15 and 31.4 ±0.2 26°.
Aspects of the present invention relate to a process for preparing lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1, characterized by the steps:
i) dissolving bulking agent and 5-azacytidine, in a stabilizing amount of solvent vehicle comprising acetonitrile and refrigerated water; in the ratio of 20:80 to 60:40.
ii) lyophilizing the solution obtained from step (i); wherein the said lyophilized formulation having l-P-D-ribofuranosyl-3-guanylurea (RGU) impurity not more than 0.2%w/w and total impurities not more than 2%w/w.
Aspects of the present invention relate to a lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1, having water content not more than 2% w/w.
Aspects of the present invention, relates to a lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1 for parenteral administration, in a sterile vessel is provided, comprising 5-azacytidine for administration to a subject in need thereof. The sterile vessel comprising a pharmaceutical formulation according to the present invention; for example, may be a vial, syringe, or ampoule.
Aspects of the present invention, herein relates to methods of using the lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1 for parenteral administration, provided herein to treat diseases or disorders including, e.g., cancer, disorders related to abnormal cell proliferation, hematologic disorders, or immune disorders, among others. In certain embodiments, the pharmaceutical compositions of 5-azacytidine which are parenterally administered to subjects in need thereof to treat a cancer or a hematological disorder, such as, for example, Myelodysplastic syndromes (MDS), acute myelogenous leukemia (AML).
BRIEF DESCRIPTION OF THE DRAWING
Fig.1 is Illustration of X-ray powder diffraction (XRPD) pattern of Crystalline 5-Azacytydine Form I.
X-Ray powder diffraction angle of Form-I provided under the table below:
Fig.2 is Illustration of X-ray powder diffraction (XRPD) pattern of Crystalline 5-Azacytidine Form SA-1 prepared in example 1.
X-Ray powder diffraction pattern of Crystalline 5-Azacytidine Form SA-1 provided under the table below:
Fig.3 is Illustration of X-ray powder diffraction (XRPD) pattern of lyophilized formulation prepared in example 2 comprising Crystalline 5-Azacytidine Form SA-1. Fig.4 is Illustration of X-ray powder diffraction (XRPD) pattern of placebo lyophilized formulation of example 2.
Comparative X-Ray powder diffraction pattern of lyophilized formulation of example 2 containing crystalline Form-SA-1 and its corresponding placebo lyophilized formulation of example 2; provided under the table below:
XRPD peaks (20°) values of (Fig 3) XRPD peaks (20°) values of (Fig 4)
12.582 16.874
13.099 17.310
13.445 18.780
13.936 19.488
14.466 19.867
15.164 20.428
16.537 21.203
17.345 22.118
17.991 22.064
18.763 23.445
19.490 24.687
19.886 25.343
20.435 27.060
21.327 27.608
21.689 27.924
22.133 29.420
22.797 32.231
23.118 33.203
24.215 34.019
24.720 35.069
25.359 36.180
26.384 39.547
26.883 40.452
27.239 44.011
27.936 44.977
28.674 -
29.411 -
29.687 -
30.639 -
31.513 -
32.174 -
33.223 -
34.039 -
35.321 -
36.188 -
37.459 -
39.557 -
40.474 -
43.987 -
44.990 -
DETAILED DESCRIPTION OF THE INVENTION
In an embodiment of the present invention, it provides a Crystalline 5-Azacytidine designated as Form-SA-1, characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60, 13.90, 15.15 and 31.4 ±0.2 26°. Said Crystalline 5-Azacytidine Form-SA-1 is further characterized by having water content upto less than 1% w/w.
In another embodiment of the present invention, it provides a process for preparing Crystalline 5-Azacytidine Form SA-1, comprising the steps of-
i) dissolving 5-azacytidine in a solvent vehicle comprising acetonitrile and refrigerated water in the ratio of 20:80 to 60:40.
ii) freeze-drying the solution,
iii) isolating the Crystalline 5-Azacytidine Form SA-1.
In a particular embodiment of the present invention, said process for preparing Crystalline 5-Azacytidine Form SA-1, comprising the steps of-
i) dissolving 5-azacytidine in a solvent vehicle comprising acetonitrile and refrigerated water in the ratio of 20:80 to 60:40; wherein refrigerated water is a precooled water having temperature of less than 5°C and dissolving of 5-azacytidine is carried out under nitrogen purging, ii) freeze-drying the solution,
iii) isolating the Crystalline 5-Azacytidine Form SA-1. During said process of preparing Crystalline 5-Azacytidine Form SA-1, it is preferable that before subjecting to freeze drying step, the step i) solution is stirred until to get clear solution.
In yet another embodiment of the present invention, it provides a lyophilized formulation of crystalline 5-Azacytidine and an optional bulking agent; wherein the said lyophilized formulation comprising crystalline 5-Azacytidine is Form-SA-1, characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60, 13.90, 15.15 and 31.4 ±0.2 20°.
The optional bulking agent can be selected from mannitol, sorbitol, lactose, sucrose, or any mixtures of two or more thereof
In a particular embodiment of the present invention, it provides a lyophilized formulation of Crystalline 5-Azacytidine Form SA-1; wherein the said lyophilized formulation is prepared by using a stabilizing amount of solvent vehicle comprising acetonitrile and refrigerated water.
In a further particular embodiment of the present invention, it encompasses a lyophilized formulation of crystalline 5-Azacytidine and a bulking agent selected from mannitol, sorbitol, lactose, sucrose, or any mixtures of two or more thereof; wherein the said lyophilized formulation comprising crystalline 5-Azacytidine is Form-SA-1, characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60, 13.90, 15.15 and 31.4 ±0.2 26°.
In yet another embodiment of the present invention, provides a process for preparing lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1, characterized by the steps:
i) dissolving an optional bulking agent and 5-azacytidine, in a stabilizing amount of solvent vehicle comprising acetonitrile and refrigerated water; in the ratio of 20:80 to 60:40. ii) lyophilizing the solution obtained from step (i); wherein the said lyophilized formulation having l-p-D-ribofuranosyl-3-guanylurea (RGU) impurity not more than 0.2%w/w and total impurities not more than 2%w/w.
Said lyophilized formulation according to present invention comprising Crystalline 5-Azacytidine Form SA-1, possess water content not more than 2% w/w. In a particular embodiment, said water content may range between 0.5% to 1.5% w/w.
In a further embodiment according to the present invention, it also provides a lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1 for parenteral administration, in a sterile vessel, comprising 5-azacytidine for administration to a subject in need thereof. The sterile vessel comprising a pharmaceutical formulation according to the present invention; for example, may be a vial, syringe, or ampoule.
In a further embodiment of the present invention, provides methods of using the lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1 for parenteral administration, provided herein to treat diseases or disorders including, e.g., cancer, disorders related to abnormal cell proliferation, hematologic disorders, or immune disorders, among others. In certain embodiments, the pharmaceutical compositions of 5-azacytidine which are parenterally administered to subjects in need thereof to treat a cancer or a hematological disorder, such as, for example, Myelodysplastic syndromes (MDS), acute myelogenous leukemia (AML).
In another embodiment of the present invention, lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1, wherein the assay value of 5-Azacytidine is NLT 90%w/w and NMT 110%w/w.
"Stable" as referred to in the context of the present invention refers to both physical stability and chemical stability.
The term "formulation" as used in the context of the present invention refers to any of various dosage forms suitable for administration of a drug, such as parenterally, intraperitoneally, intravenously, intraarterially, intramuscularly, subcutaneously, etc.
The term "physical stability" as used in the specification refers to retaining an original physical form in a formulation, even after storage under any of various stability testing conditions.
The term "chemical stability" as referred in the specification relates to maintaining an original drug purity of the formulation, in terms of drug-related impurities or drug-related substances. 5-azacytidine hydrolyzes quickly in water, and this is dependent on pH and temperature. It has been observed that, due to hydrolysis, around nine solid state forms have been identified: five polymorphic forms, three psueodpolymorphic forms and an amorphous form. Polymorphism could be of importance since speed of dissolution of azacitidine could affect its degradation. Azacitidine rapidly degrades in aqueous solutions via hydrolysis, and due to this instability a lyophilized dosage form was developed to minimize water activity in the dosage form. Hence, the water content of a formulation may impact the stability of the product.
Two major degradants have been observed due to hydrolysis. The hydrolytic pathway leads to the formation of an initial N-formyl compound hydrolysis product "RGU-CHO," which is a reversible reaction and the compounds are in equilibrium with each other. This is followed by ring opening and loss of formic acid which results in formation of an amine compound "RGU," which is an irreversible reaction. RGU-CHO is N-(formylamidino) N'-P-D-ribofuranosylurea ("N-formyl compound" below) and RGU is l-p-D-ribofuranosyl-3-guanylurea ("amine compound" below). Azacitidine N-formyl compound-RGU-CHO Amine compound-RGU
The term "Impurity-1" as referred in the specification relates to 4-amino-l, 3,5-triazine-2-(lH)-one or also known as 5-Azacytosine.
The term "Impurity-2" as referred in the specification relates to l-O-Acetyl-2, 3, 5-Tri-O-benzoyl- p -D-ribofuranose.
The term "Impurity-3" as referred in the specification relates to l-(2, 3, 5-Tri-O-benzoyl-p-D-ribifuranosyl)-4-amino-l,2-dihydro-l,3,5-triazin-2-one.
The term "Total impurity" as referred in the specification relates to sum of all known impurities like "Impurity-1", "Impurity-2", "Impurity-3" and RGU; but excluding RGU-CHO.
As used herein "stabilizing amount of solvent vehicle" means the ratio of organic solvent and water which would reduce the level of degradation products of 5-azacytidine in the invention compositions. The ratio is 20:80 to 60:40 of stabilizing amount of solvent vehicle which would limit the levels of l-P-D-ribofuranosyl-3-guanylurea (RGU) is NMT 0.2%w/w of 5-AZT.
The term "water for injections or WFI" as referred in the specification relates to distilled or sterile water for injection or saline or physiological saline or 0.9% Sodium Chloride Injection or Lactated Ringer's Injection.
The term "refrigerated water or refrigerated water for injection" referred in the specification relates to having a temperature of less than about 8°C, or a temperature of between about 2°C to 8°C or a temperature of about 5°C.
Injectable formulations can be prepared in conventional forms, either as liquid solutions or suspensions, solid forms suitable for solubilization or suspending in liquid prior to injection, or as emulsions. Sterile injectable formulations can be prepared according to techniques known in the art using suitable carriers, dispersing or wetting agents, and/or suspending agents. The injectable formulations may be sterile injectable solutions or suspensions in a nontoxic, parenterally acceptable diluent or solvent. Among the acceptable vehicles and solvents that may be employed are water, Ringer's solution and isotonic sodium chloride solution. In addition, fixed oils, fatty esters or polyols are conventionally employed as solvents or suspending media.
The technique known as lyophilization is sometimes employed to process injectable pharmaceuticals that exhibit poor active ingredient stability in aqueous solutions. Lyophilization processing is suitable for injectables because it can be conducted under sterile conditions, which is a primary requirement for parenteral dosage forms. Cryoprotectants are excipients whose primary function is to protect the active constituent during a freezing process. Cryoprotectants in the present invention include bulking agents that may be used in the invention.
Lyophilization or freeze-drying is a process in which water is removed from a product after it is frozen and placed under a vacuum, allowing the ice to change directly from a solid to a vapor, without passing through a liquid phase. The process consists of three separate, unique, and interdependent processes; a freezing phase, a primary drying phase (sublimation), and a secondary drying phase (desorption). These processes may be optimized to enhance the product stability as well as decrease the manufacturing costs.
Freezing Phase:
A primary function of the freezing phase is to ensure that the entire container having the complex solution is completely frozen, prior to proceeding to a subsequent phase. Additionally, it is usually desired that these containers freeze in a uniform manner. While there are different ways that this can be accomplished, one option is to chill the containers after they are loaded onto the lyophilizer shelves and holding for 30-60 minutes prior to initiation of the freezing cycle. It is generally not practical to equilibrate the shelves to a freezing temperature, because of frost accumulation during the filling and loading of the containers.
Primary Drying Phase:
Once the formulation is brought to the desired frozen state, primary drying via sublimation can proceed. The primary drying phase involves the removal of bulk water at a product temperature below the ice transition temperature under a vacuum (pressures typically between 50-300 mTorr). This phase can be a critical one for stabilizing an active. The goal is to identify the glass transition temperature (Tg') for the formulation. The Tg' is the temperature at which there is a reversible change of state between a viscous liquid and a rigid, amorphous glassy state. One can measure the Tg' of candidate formulations using a differential scanning calorimeter (DSC), in particular with modulated DSC. Generally, the collapse temperature is observed to be about 2-5°C greater than the Tg'. Hence, the shelf temperature is set such that the target product temperature is maintained near or below the Tg' of the formulation throughout the removal of solvent during the primary dry phase.
As the solvent is progressively removed from the formulation containers, the product temperature will approach and reach the shelf temperature since it is no longer cooled by water sublimation. To optimize the duration of the primary dry phase, the removal of solvent vapor can be tracked using a moisture detector, or by monitoring the decrease in pressure difference between a capacitance manometer and a thermocouple pressure gauge or by a pressure drop measurement. The optimization of the primary dry cycle involves a removal of solvent as quickly as possible without causing cake collapse and subsequent product instability.
Secondary Drying Phase:
The secondary drying phase is the final segment of the lyophilization cycle, where residual moisture is removed from a formulation's interstitial matrix by desorption with elevated temperatures and/or reduced pressures. The final moisture content of a lyophilized formulation, which can be measured by Karl Fischer or other methods, is important because if the solid cake contains too much residual moisture, the stability of the active can be compromised. Hence, it is imperative that one achieves a moisture level as low as possible.
To accomplish a low residual moisture, the shelf temperature is typically elevated to accelerate desorption of water molecules. The duration of the secondary drying phase is usually short. When microstructure collapse occurs, the residual moisture is generally significantly greater than desired. One alternative is to purge the sample chamber of the lyophilizer with alternating cycles of an inert gas such as nitrogen, to facilitate displacement of bound water. However, another solution is to properly formulate the drug product and run an optimal lyophilization cycle.
The advantages of lyophilization include: ease of processing a liquid, which simplifies aseptic handling; enhanced stability of a dry powder; removal of water without excessive heating of the product; enhanced product stability in a dry state; and rapid and easy dissolution of reconstituted product. The product is dried without elevated temperatures, thereby eliminating adverse thermal effects, and then stored in the dry state in which there are relatively few stability problems.
Additionally, freeze dried products are often more soluble, dispersions are stabilized, and products subject to degradation by oxidation or hydrolysis are protected.
Pharmaceuticals to be freeze dried are frequently in aqueous solutions, ranging from about 0.01 to 40% by weight concentrations of total solids. Usually, an improvement in stability of the lyophilizate, compared to a solution, is due to the absence of water in the lyophilizate.
A pharmacologically active constituent of many pharmaceutical products is present in such small quantities that, if freeze dried alone, it may not give a composition of suitable mass, and in some cases its presence would be hard to detect visually. Therefore, exoipients are often added to increase the amount of solids present. In most applications it is desirable for a dried product cake to occupy essentially the same volume as that of the original solution. To achieve this, the total solids content of the original solution is frequently about 10 to 25% by weight.
Bulking substances that are useful for this purpose, often in combination, include, but are not limited to, sodium or potassium phosphates (monobasic potassium phosphate, potassium dihydrogen phosphate, etc.), citric acid, tartaric acid, gelatin, lactose and other carbohydrates such as dextrose, mannitol and dextran, and occasionally preservatives. Various excipients contribute appearance characteristics to the cake, such as dull and spongy, sparkling and crystalline, firm or friable, expanded or shrunken, and uniform or striated. Therefore formulations of a composition to be freeze dried should be a result of consideration not only of the nature and stability characteristics required during the liquid state, both freshly prepared and when reconstituted before use, but also the characteristics desired in the final lyophilized cake.
The injectable pharmaceutical formulations may optionally include one or more other pharmaceutically acceptable excipients. The pharmaceutically acceptable excipients may include any one or more of: antibacterial preservatives, such as one or more of phenylmercuric nitrate, thiomersal, benzalkonium chloride, benzethonium chloride, phenol, cresol, and chlorobutanol; antioxidants including one or more of ascorbic acid, sodium sulfite, sodium bisulfite and sodium metabisulfite; chelating agents such as ethylenediamine tetraacetic acid (EDTA); buffers including one or more of acetate, citrate, tartarate, phosphate, benzoate and bicarbonate buffers; tonicity contributors including one or more of sodium chloride, potassium chloride, dextrose, mannitol, sorbitol and lactose; and alkaline substances including one or more of sodium hydroxide, potassium hydroxide, sodium carbonate and meglumine.
In aspects the invention includes kits provided for delivery of the azacitidine or its salts. A kit according to the present invention comprises a container holding the drug composition, a sterile reconstitution vehicle, and a sterile syringe.
Certain specific aspects and embodiments of the invention will be further described in the following examples, which are provided only for purposes of illustration and are not intended to limit the scope of the invention in any manner.
Example 1:
Preparation of Crystalline 5-Azacytidine Form-SA-1 by Freeze-drying.
Brief method of preparation:
1. 30% of precooled Milli-Q water (5°C) of required batch Size was collected in cleaned Duran bottle and the temperature was maintained at 5°C throughout the manufacturing process.
2. Dispensed quantity of acetonitrile was added to the above step and stirred for 5minutes and the solution was cooled to 5°C.
3. Weighed quantity of 5-azacytidine Form I was added to the above step and stirred to get the clear solution.
4. Volume was made up to 100% with cool Milli-Q water and stirred for 5minutes.
5. The solution of step 4 was filtered through 0.2(i PES Filter and filtrate was filled into 30ml/20mm flint moulded Vial with a fill volume of 20.0mL, half stoppered with dark grey Bromobutyl rubber stopper and loaded into precooled Lyophilizer.
6. The Lyophilization was carried out as per below recipe.
7. After completion of the cycle, vacuum was breakdown through Nitrogen then the vials were fully stoppered and unloaded from Lyophilizer. The unloaded vials were sealed using aluminum seals.
Water content of Crystalline 5-Azacytidine Form-SA-1 obtained is 0.6% w/w.
Example 2 :
Azacitidine for injection 100mg/Vial.
Brief method of preparation:
1. 30% of precooled Milli-Q water (5°C) of required batch Size was collected in cleaned Duran bottle and the temperature was maintained at 5°C throughout the manufacturing process.
2. Dispensed quantity of acetonitrile was added to the above step and stirred for 5minutes and the solution was cooled to 5°C.
3. Weighed quantity of Mannitol was added to the above step and stirred to get a clear solution.
4. Weighed quantity of 5-azacytidine was added to the above step and stirred to get the clear solution.
5. Volume was made up to 100% with cool Milli-Q water and stirred for 5minutes.
6. The solution of step 5 was filtered through 0.2u PES Filter and filtrate was filled into 30ml/20mm flint moulded Vial with a fill volume of 20.0mL, half stoppered with dark grey Bromobutyl rubber stopper and loaded into precooled Lyophilizer.
7. The Lyophilization was carried out as per below recipe.
8. After completion of the cycle, vacuum was breakdown through Nitrogen then the vials were fully stoppered and unloaded from Lyophilizer. The unloaded vials were sealed using aluminum seals.
A placebo formulation of example 2 is prepared with the same formula and manufacturing process excluding 5-azacytidine Form I.
Further, example 2 & its corresponding placebo formulations were subjected to X-ray powder diffraction (XRPD) and as illustrated in Fig 3&4; it was observed that 5-azacytidine SA-1 formed in the example 1 formulation.
Chemical stability is tested for example 2 at initial stage as well as storing the lyophilized vials under 40°C and 75% relative humidity and 60 °C 1 week. Assay, water content & impurity analyses are performed before storage ("Initial") and after storage, and are expressed as percentages of the label 5-azacytidine content.
While the foregoing provides a detailed description of the preferred embodiments of the invention, it is to be understood that the descriptions are illustrative only of the principles of the invention and not limiting. Furthermore, as many changes can be made to the invention without departing from the scope of the invention, it is intended that all material contained herein be interpreted as illustrative of the invention and not in a limiting sense.
Claims:
1. Crystalline 5-Azacytidine designated as Form-SA-1 characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60, 13.90, 15.15 and 31.4 ±0.2 26°.
2. Crystalline 5-Azacytidine Form-SA-1 according to claim 1; wherein the water content is less than 1% w/w.
3. A process for preparing Crystalline 5-Azacytidine Form SA-1, comprising the steps of-
i) dissolving 5-azacytidine in a solvent vehicle comprising acetonitrile and refrigerated water in the ratio of 20:80 to 60:40. ii) freeze-drying the solution, iii) isolating the Crystalline 5-Azacytidine Form SA-1.
4. A process for preparing Crystalline 5-Azacytidine Form SA-1 according to claim-3, wherein refrigerated water used in step i) is a precooled water having temperature of less than 5°C and dissolving of 5-azacytidine is carried out under nitrogen purging.
5. A process for preparing Crystalline 5-Azacytidine Form SA-1 according to claim-3, wherein before freeze drying step, the step i) solution is stirred to get clear solution.
6. A lyophilized formulation of crystalline 5-Azacytidine and optionally a bulking agent; wherein the said lyophilized formulation comprising crystalline 5-Azacytidine is Form-SA-1, characterized by an X-Ray powder diffraction pattern having at least four characteristic diffraction angle peaks at about 12.00, 12.60, 13.90, 15.15 and 31.4 ±0.2 26°.
7. A lyophilized formulation according to claim-6; wherein the bulking agent is selected from mannitol, sorbitol, lactose, sucrose, or any mixtures of two or more thereof.
8. A process for preparing lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1, characterized by the steps:
i) dissolving optional bulking agent and 5-azacytidine, in a stabilizing amount of solvent vehicle comprising acetonitrile and refrigerated water; in the ratio of 20:80 to 60:40.
ii) lyophilizing the solution obtained from step (i); wherein the said lyophilized formulation having l-p-D-ribofuranosyl-3-guanylurea (RGU) impurity not more than 0.2%w/w and total impurities not more than 2%w/w.
9. A process for preparing lyophilized formulation according to claim-8, wherein 5-azacytidine used in the step i) is Form I.
10. A lyophilized formulation comprising Crystalline 5-Azacytidine Form SA-1 according to claims 6-9, having water content not more than 1% w/w.
| # | Name | Date |
|---|---|---|
| 1 | 2148-CHE-2013 CORRESPONDENCE OTHERS 31-07-2013.pdf | 2013-07-31 |
| 1 | 2148-CHE-2013 FORM-5 15-05-2013.pdf | 2013-05-15 |
| 2 | 2148-CHE-2013 FORM-1 31-07-2013.pdf | 2013-07-31 |
| 2 | 2148-CHE-2013 FORM-3 15-05-2013.pdf | 2013-05-15 |
| 3 | 2148-CHE-2013 FORM-2 15-05-2013.pdf | 2013-05-15 |
| 3 | 2148-CHE-2013 DRAWINGS 15-05-2013.pdf | 2013-05-15 |
| 4 | 2148-CHE-2013 FORM-1 15-05-2013.pdf | 2013-05-15 |
| 4 | 2148-CHE-2013 ABSTRACT 15-05-2013.pdf | 2013-05-15 |
| 5 | 2148-CHE-2013 CLAIMS 15-05-2013.pdf | 2013-05-15 |
| 5 | 2148-CHE-2013 DESCRIPTION (COMPLETE) 15-05-2013.pdf | 2013-05-15 |
| 6 | 2148-CHE-2013 CORRESPONDENCE OTHERS 15-05-2013.pdf | 2013-05-15 |
| 7 | 2148-CHE-2013 CLAIMS 15-05-2013.pdf | 2013-05-15 |
| 7 | 2148-CHE-2013 DESCRIPTION (COMPLETE) 15-05-2013.pdf | 2013-05-15 |
| 8 | 2148-CHE-2013 ABSTRACT 15-05-2013.pdf | 2013-05-15 |
| 8 | 2148-CHE-2013 FORM-1 15-05-2013.pdf | 2013-05-15 |
| 9 | 2148-CHE-2013 DRAWINGS 15-05-2013.pdf | 2013-05-15 |
| 9 | 2148-CHE-2013 FORM-2 15-05-2013.pdf | 2013-05-15 |
| 10 | 2148-CHE-2013 FORM-3 15-05-2013.pdf | 2013-05-15 |
| 10 | 2148-CHE-2013 FORM-1 31-07-2013.pdf | 2013-07-31 |
| 11 | 2148-CHE-2013 FORM-5 15-05-2013.pdf | 2013-05-15 |
| 11 | 2148-CHE-2013 CORRESPONDENCE OTHERS 31-07-2013.pdf | 2013-07-31 |