WO2017163170A1 - Pharmaceutical composition comprising apixaban - Google Patents

Pharmaceutical composition comprising apixaban Download PDF

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Publication number
WO2017163170A1
WO2017163170A1 PCT/IB2017/051605 IB2017051605W WO2017163170A1 WO 2017163170 A1 WO2017163170 A1 WO 2017163170A1 IB 2017051605 W IB2017051605 W IB 2017051605W WO 2017163170 A1 WO2017163170 A1 WO 2017163170A1
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WIPO (PCT)
Prior art keywords
apixaban
pharmaceutical composition
composition according
organic solvent
granulated
Prior art date
Application number
PCT/IB2017/051605
Other languages
French (fr)
Inventor
Mukesh Kumar Garg
Swati Aggrawal
Abhishek Srivastava
Original Assignee
Sun Pharmaceutical Industries Limited
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Filing date
Publication date
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Publication of WO2017163170A1 publication Critical patent/WO2017163170A1/en

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/435Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with one nitrogen as the only ring hetero atom
    • A61K31/44Non condensed pyridines; Hydrogenated derivatives thereof
    • A61K31/445Non condensed piperidines, e.g. piperocaine
    • A61K31/4523Non condensed piperidines, e.g. piperocaine containing further heterocyclic ring systems
    • A61K31/4545Non condensed piperidines, e.g. piperocaine containing further heterocyclic ring systems containing a six-membered ring with nitrogen as a ring hetero atom, e.g. pipamperone, anabasine
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2013Organic compounds, e.g. phospholipids, fats
    • A61K9/2018Sugars, or sugar alcohols, e.g. lactose, mannitol; Derivatives thereof, e.g. polysorbates
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1629Organic macromolecular compounds
    • A61K9/1635Organic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyvinyl pyrrolidone, poly(meth)acrylates

Definitions

  • the present invention relates to a pharmaceutical composition
  • a pharmaceutical composition comprising apixaban prepared by a non-aqueous wet granulation process wherein the composition releases at least 80% of apixaban in 30 minutes, when measured in United States
  • Apixaban is a factor Xa inhibitor used for the treatment or prevention of a thromboembolic disorder, and is disclosed in U.S. Patent No. 6,967,208.
  • apixaban tablets are marketed by Bristol Myer Squibb under the trade name Eliquis ® .
  • PCT application No. WO 2011/106478 discloses that the formulations of apixaban that were made using a wet granulation process as well as those using larger particle size of the drug substance resulted in less than optimal exposures, which can present quality control challenges. It further discloses a dry granulation process for preparing a composition comprising crystalline apixaban particles having a D90 equal to or less than about 89 ⁇ as measured by laser light scattering.
  • Apixaban has an Occupational Exposure Limit (OEL) of around 8.3 ⁇ g/m 3 . Drugs having an OEL value of less than 10 ⁇ g/m 3 are considered potent and require special containment area.
  • OEL Occupational Exposure Limit
  • the choice of which granulation process to use is limited for potent drugs. Since the drug content in the compositions comprising potent drugs is low, such compositions are generally not well suited for dry methods such as roller compaction, which may lead to problems in achieving an even drug distribution in the composition of the drug. Further, the machines as well as operations used in dry granulation are difficult to build in a contained way and pose a risk of airborne contamination. Hence, wet granulation is considered a preferable process over dry granulation for potent drugs such as apixaban.
  • a pharmaceutical composition comprising wet granulated apixaban and at least one pharmaceutical excipient, wherein the wet granulated apixaban is granulated using an organic solvent and the composition releases at least 80% of apixaban in 30 minutes, when measured in United States Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a temperature of 37°C ⁇ 0.5°C in 900 mL of pH 6.8 phosphate buffer containing sodium lauryl sulphate (SLS).
  • USP United States Pharmacopeia
  • SLS sodium lauryl sulphate
  • a first aspect of the present invention provides a pharmaceutical composition comprising wet granulated apixaban and at least one pharmaceutical excipient, wherein the wet granulated apixaban is granulated using an organic solvent and the composition releases at least 80% of apixaban in 30 minutes, when measured in United States
  • a second aspect of the present invention provides a wet granulated apixaban composition prepared by non-aqueous granulation process wherein the ratio of organic solvent to intra-granular mass during the granulation process is from about 1 :0.2 to about 1 :0.6.
  • a third aspect of the present invention provides a wet granulated apixaban composition prepared by non-aqueous granulation process wherein the ratio of organic solvent to intra-granular mass during the granulation process is from about 1 :0.2 to about 1 :0.6 and the composition releases at least 80% of apixaban in 30 minutes, when measured in United States Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a temperature of 37°C ⁇ 0.5°C in 900 mL of pH 6.8 phosphate buffer containing sodium lauryl sulphate.
  • USP United States Pharmacopeia
  • At least 85% of apixaban is released in 30 minutes.
  • apixaban is in crystalline form. According to another embodiment, apixaban has a particle size D90 of not less than 100 ⁇ , in particular from about 100 ⁇ to about 200 ⁇ , e.g., 120 ⁇ - 150 ⁇ .
  • the apixaban composition is stable at a temperature of 40°C and 75% relative humidity (RH) for a period of 3 months.
  • intra-granular mass means an intra-granular component of the composition comprising apixaban and one or more pharmaceutically acceptable excipients along with the organic solvents used during the granulation phase.
  • non-aqueous wet granulation means that apixaban is granulated using organic solvents selected from the group consisting of ethanol, isopropyl alcohol, dichloromethane, dimethylsulphoxide, dimethylformamide, N-methyl-2- pyrrolidone, dimethylacetamide, acetic acid or mixtures thereof.
  • the organic solvent is dichloromethane.
  • the non-aqueous granulation is high shear wet granulation.
  • the non-aqueous granulation may be carried out in a rapid mixer granulator.
  • D90 value means at least 90% of the apixaban particles have a volume diameter in the specified range when measured by a light scattering method such as by a Malvern Mastersizer.
  • a fourth aspect of the present invention provides a non-aqueous wet granulation process for the preparation of a pharmaceutical composition wherein the process comprises:
  • step b) blending and granulating the pharmaceutically acceptable excipients with the solution/dispersion of step a);
  • step b) compressing/filling the granules of step b) into suitable size tablets/capsules.
  • the solution or dispersion of step a) further comprises one or more pharmaceutically acceptable excipients.
  • a fifth aspect of the present invention provides a non-aqueous wet granulation process for the preparation of a pharmaceutical composition wherein the process comprises:
  • step b) blending the granules of step a) with one or more pharmaceutically acceptable excipients;
  • step b) compressing/filling the granules of step b) into suitable size tablets/capsules.
  • apixaban may be partly added to the granulating liquid of step a).
  • the granulating liquid of step a) further comprises one or more pharmaceutically acceptable excipients.
  • Examples of pharmaceutically acceptable excipients include binders, diluents, lubricants/glidants, surfactants, disintegrants or mixtures thereof.
  • binders include carbomer (e.g. carbopol), carboxymethylcellulose sodium, dextrin, ethyl cellulose, gelatin, guar gum, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropyl methylcellulose, liquid glucose, maltodextrin, methylcellulose, polymethacrylates, povidone, pregelatinized starch, sodium alginate, starch or mixtures thereof.
  • carbomer e.g. carbopol
  • carboxymethylcellulose sodium, dextrin ethyl cellulose
  • gelatin guar gum
  • hydroxyethyl cellulose hydroxypropyl cellulose
  • hydroxypropyl methylcellulose hydroxypropyl methylcellulose
  • polymethacrylates povidone
  • pregelatinized starch sodium alginate, starch or mixtures thereof.
  • diluents include microcrystalline cellulose, lactose, starch, pregelatinized starch, calcium carbonate, calcium sulfate, sugar, dextrates, dextrin, dextrose, dibasic calcium phosphate dihydrate, tribasic calcium phosphate, kaolin, magnesium carbonate, magnesium oxide, maltodextrin, mannitol, potassium chloride, powdered cellulose, sodium chloride, sorbitol or mixtures thereof.
  • disintegrants examples include low substituted hydroxypropyl-cellulose, croscarmellose sodium (e.g. Ac Di Sole, Primellose®), crospovidone (e.g. Kollidon®, Polyplasdone®), microcrystalline cellulose, polacrilin potassium, powdered cellulose, pregelatinized starch, sodium starch glycolate (e.g. Explotab®, Primoljel®) and starch, or mixtures thereof.
  • croscarmellose sodium e.g. Ac Di Sole, Primellose®
  • crospovidone e.g. Kollidon®, Polyplasdone®
  • microcrystalline cellulose e.g. Kollidon®, Polyplasdone®
  • polacrilin potassium e.g. Kollidon®, Polyplasdone®
  • powdered cellulose e.g. Explotab®, Primoljel®
  • starch e.g. Explotab®, Primoljel®
  • lubricants or glidants examples include colloidal silicon dioxide, stearic acid, magnesium stearate, calcium stearate, talc, hydrogenated castor oil, sucrose esters of fatty acid, microcrystalline wax, yellow beeswax, white beeswax, or mixtures thereof.
  • surfactants include sodium lauryl sulfate, sodium dodecyl sulfate, ammonium lauryl sulfate, benzalkonium chloride, alkyl poly(ethylene oxide), copolymers of poly(ethylene oxide) and poly(propylene oxide) commercially known as poloxamers or poloxamines, polyvinyl alcohol (PVA), fatty alcohols, polyoxyethylene alkyl ether, polyoxyethylene alkyl aryl ether, polyethylene glycol fatty acid ester, alkylene glycol fatty acid mono ester, sucrose fatty acid ester, sorbitol monolaurate (Span ® 20 or Span ® 80), polyoxyethylene sorbitan fatty acid ester (polysorbates), or mixtures thereof.
  • PVA polyvinyl alcohol
  • fatty alcohols polyoxyethylene alkyl ether
  • polyoxyethylene alkyl aryl ether polyethylene glycol fatty acid ester
  • alkylene glycol fatty acid mono ester suc
  • the composition may be further coated with a functional or non-functional coating.
  • the coating of the present invention may further comprise excipients selected from the group comprising plasticizers, binders, opacifiers, anti-tacking agents, anti- foaming agents, colors, film-forming polymers, or mixtures thereof.
  • Organic or aqueous solvents may be used during the coating process. Solvents may be selected from the group comprising water, acetone, isopropyl alcohol, ethanol, isopropyl acetate, dichloromethane, or mixtures thereof.
  • plasticizers include propylene glycol, triethyl citrate, tributyl citrate, dibutyl sebacate, acetyl tributyl citrate, glyceryl monostearate, triacetin, polyethylene glycol, diethyl phthalate, acetylated monoglycerides, diacetylated monoglyceride, cetyl alcohol, or mixtures thereof.
  • opacifiers examples include titanium dioxide, silicon dioxide, talc, calcium carbonate, behenic acid, or mixtures thereof.
  • anti-tacking agents examples include talc, colloidal silicon dioxide, or mixtures thereof.
  • anti -foaming agents examples include silicon based surfactants, e.g., simethicone; vegetable oils; waxes; hydrophobic silica; polyethylene glycol; or mixtures thereof.
  • Coloring agents may be selected from FDA approved colorants such as iron oxide, lake of tartrazine, allura red, titanium dioxide, or mixtures thereof.
  • film-forming polymers examples include hydroxypropyl methylcellulose, methyl cellulose, carboxymethyl cellulose, hydroxyethyl cellulose, polyethylene glycol, polyvinyl alcohol, or mixtures thereof.
  • commercially available coating compositions comprising film-forming polymers marketed under various trade names, such as Opadry ® , may also be used for coating.
  • Coating may be carried out by using any conventional coating techniques known in the art, such as spray coating in a conventional coating pan, fluidized bed processor, or dry powder coating.
  • step 1) was granulated with solution of step 2) to obtain granules.
  • Lubricated granules of step 4) were compressed into a suitable size tablet.
  • step 5 Tablets obtained in step 5 were coated with OpadryTM Pink dispersion. Dissolution studies
  • the dissolution was carried out in United States Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a temperature of 37 ⁇ 0.5°C, in 900 mL of pH 6.8 phosphate buffer containing 0.05% SLS.
  • USP United States Pharmacopeia
  • Table 1 Dissolution profile of Example 1 and Eliquis ® tablet.

Abstract

The present invention relates to a pharmaceutical composition comprising apixaban prepared by a non-aqueous wet granulation process wherein the composition releases at least 80% of apixaban in 30 minutes, when measured in United States Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a 5 temperature of 37°C ± 0.5°C in 900 mL of pH 6.8 phosphate buffer containing sodium lauryl sulphate.

Description

PHARMACEUTICAL COMPOSITION COMPRISING APIXABAN
The present invention relates to a pharmaceutical composition comprising apixaban prepared by a non-aqueous wet granulation process wherein the composition releases at least 80% of apixaban in 30 minutes, when measured in United States
Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm and temperature of 37°C ± 0.5°C in 900 mL of pH 6.8 phosphate buffer containing sodium lauryl sulphate.
Background of the Invention
Apixaban is a factor Xa inhibitor used for the treatment or prevention of a thromboembolic disorder, and is disclosed in U.S. Patent No. 6,967,208. Commercially, apixaban tablets are marketed by Bristol Myer Squibb under the trade name Eliquis®.
PCT application No. WO 2011/106478 discloses that the formulations of apixaban that were made using a wet granulation process as well as those using larger particle size of the drug substance resulted in less than optimal exposures, which can present quality control challenges. It further discloses a dry granulation process for preparing a composition comprising crystalline apixaban particles having a D90 equal to or less than about 89 μιη as measured by laser light scattering.
Apixaban has an Occupational Exposure Limit (OEL) of around 8.3 μg/m3. Drugs having an OEL value of less than 10 μg/m3 are considered potent and require special containment area. Although there are several granulation processes that can be used in formulating dosage forms, the choice of which granulation process to use is limited for potent drugs. Since the drug content in the compositions comprising potent drugs is low, such compositions are generally not well suited for dry methods such as roller compaction, which may lead to problems in achieving an even drug distribution in the composition of the drug. Further, the machines as well as operations used in dry granulation are difficult to build in a contained way and pose a risk of airborne contamination. Hence, wet granulation is considered a preferable process over dry granulation for potent drugs such as apixaban.
Therefore, the present inventors have now developed an apixaban composition which is prepared by non-aqueous wet granulation method, but still provides the desired dissolution characteristics. Summary of the Invention
There is provided a pharmaceutical composition comprising wet granulated apixaban and at least one pharmaceutical excipient, wherein the wet granulated apixaban is granulated using an organic solvent and the composition releases at least 80% of apixaban in 30 minutes, when measured in United States Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a temperature of 37°C ± 0.5°C in 900 mL of pH 6.8 phosphate buffer containing sodium lauryl sulphate (SLS).
Detailed Description of the Invention
A first aspect of the present invention provides a pharmaceutical composition comprising wet granulated apixaban and at least one pharmaceutical excipient, wherein the wet granulated apixaban is granulated using an organic solvent and the composition releases at least 80% of apixaban in 30 minutes, when measured in United States
Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a temperature of 37°C ± 0.5°C in 900 mL of pH 6.8 phosphate buffer containing sodium lauryl sulphate.
A second aspect of the present invention provides a wet granulated apixaban composition prepared by non-aqueous granulation process wherein the ratio of organic solvent to intra-granular mass during the granulation process is from about 1 :0.2 to about 1 :0.6.
A third aspect of the present invention provides a wet granulated apixaban composition prepared by non-aqueous granulation process wherein the ratio of organic solvent to intra-granular mass during the granulation process is from about 1 :0.2 to about 1 :0.6 and the composition releases at least 80% of apixaban in 30 minutes, when measured in United States Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a temperature of 37°C ± 0.5°C in 900 mL of pH 6.8 phosphate buffer containing sodium lauryl sulphate.
According to one embodiment of the present invention, at least 85% of apixaban is released in 30 minutes.
According to one embodiment of the present invention, apixaban is in crystalline form. According to another embodiment, apixaban has a particle size D90 of not less than 100 μιη, in particular from about 100 μιη to about 200 μιη, e.g., 120 μιη - 150 μιη.
According to another embodiment, the apixaban composition is stable at a temperature of 40°C and 75% relative humidity (RH) for a period of 3 months.
The term "intra-granular mass" as used herein means an intra-granular component of the composition comprising apixaban and one or more pharmaceutically acceptable excipients along with the organic solvents used during the granulation phase.
The term "non-aqueous wet granulation" as used herein means that apixaban is granulated using organic solvents selected from the group consisting of ethanol, isopropyl alcohol, dichloromethane, dimethylsulphoxide, dimethylformamide, N-methyl-2- pyrrolidone, dimethylacetamide, acetic acid or mixtures thereof.
According to another embodiment, the organic solvent is dichloromethane.
According to another embodiment, the non-aqueous granulation is high shear wet granulation.
According to another embodiment, the non-aqueous granulation may be carried out in a rapid mixer granulator.
The term "D90 value" means at least 90% of the apixaban particles have a volume diameter in the specified range when measured by a light scattering method such as by a Malvern Mastersizer.
A fourth aspect of the present invention provides a non-aqueous wet granulation process for the preparation of a pharmaceutical composition wherein the process comprises:
a) dissolving/dispersing apixaban in an organic solvent;
b) blending and granulating the pharmaceutically acceptable excipients with the solution/dispersion of step a); and
c) compressing/filling the granules of step b) into suitable size tablets/capsules.
According to another embodiment, the solution or dispersion of step a) further comprises one or more pharmaceutically acceptable excipients.
According to another embodiment, a portion of apixaban is added to the pharmaceutically acceptable excipients of step b). A fifth aspect of the present invention provides a non-aqueous wet granulation process for the preparation of a pharmaceutical composition wherein the process comprises:
a) granulating apixaban with a granulating liquid prepared using an organic solvent;
b) blending the granules of step a) with one or more pharmaceutically acceptable excipients; and
c) compressing/filling the granules of step b) into suitable size tablets/capsules.
According to another embodiment, apixaban may be partly added to the granulating liquid of step a).
According to another embodiment, the granulating liquid of step a) further comprises one or more pharmaceutically acceptable excipients.
Examples of pharmaceutically acceptable excipients include binders, diluents, lubricants/glidants, surfactants, disintegrants or mixtures thereof.
Examples of binders include carbomer (e.g. carbopol), carboxymethylcellulose sodium, dextrin, ethyl cellulose, gelatin, guar gum, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropyl methylcellulose, liquid glucose, maltodextrin, methylcellulose, polymethacrylates, povidone, pregelatinized starch, sodium alginate, starch or mixtures thereof.
Examples of diluents include microcrystalline cellulose, lactose, starch, pregelatinized starch, calcium carbonate, calcium sulfate, sugar, dextrates, dextrin, dextrose, dibasic calcium phosphate dihydrate, tribasic calcium phosphate, kaolin, magnesium carbonate, magnesium oxide, maltodextrin, mannitol, potassium chloride, powdered cellulose, sodium chloride, sorbitol or mixtures thereof.
Examples of disintegrants include low substituted hydroxypropyl-cellulose, croscarmellose sodium (e.g. Ac Di Sole, Primellose®), crospovidone (e.g. Kollidon®, Polyplasdone®), microcrystalline cellulose, polacrilin potassium, powdered cellulose, pregelatinized starch, sodium starch glycolate (e.g. Explotab®, Primoljel®) and starch, or mixtures thereof.
Examples of lubricants or glidants include colloidal silicon dioxide, stearic acid, magnesium stearate, calcium stearate, talc, hydrogenated castor oil, sucrose esters of fatty acid, microcrystalline wax, yellow beeswax, white beeswax, or mixtures thereof.
Examples of surfactants include sodium lauryl sulfate, sodium dodecyl sulfate, ammonium lauryl sulfate, benzalkonium chloride, alkyl poly(ethylene oxide), copolymers of poly(ethylene oxide) and poly(propylene oxide) commercially known as poloxamers or poloxamines, polyvinyl alcohol (PVA), fatty alcohols, polyoxyethylene alkyl ether, polyoxyethylene alkyl aryl ether, polyethylene glycol fatty acid ester, alkylene glycol fatty acid mono ester, sucrose fatty acid ester, sorbitol monolaurate (Span® 20 or Span® 80), polyoxyethylene sorbitan fatty acid ester (polysorbates), or mixtures thereof.
The composition may be further coated with a functional or non-functional coating. The coating of the present invention may further comprise excipients selected from the group comprising plasticizers, binders, opacifiers, anti-tacking agents, anti- foaming agents, colors, film-forming polymers, or mixtures thereof. Organic or aqueous solvents may be used during the coating process. Solvents may be selected from the group comprising water, acetone, isopropyl alcohol, ethanol, isopropyl acetate, dichloromethane, or mixtures thereof.
Examples of plasticizers include propylene glycol, triethyl citrate, tributyl citrate, dibutyl sebacate, acetyl tributyl citrate, glyceryl monostearate, triacetin, polyethylene glycol, diethyl phthalate, acetylated monoglycerides, diacetylated monoglyceride, cetyl alcohol, or mixtures thereof.
Examples of opacifiers include titanium dioxide, silicon dioxide, talc, calcium carbonate, behenic acid, or mixtures thereof.
Examples of anti-tacking agents include talc, colloidal silicon dioxide, or mixtures thereof.
Examples of anti -foaming agents include silicon based surfactants, e.g., simethicone; vegetable oils; waxes; hydrophobic silica; polyethylene glycol; or mixtures thereof.
Coloring agents may be selected from FDA approved colorants such as iron oxide, lake of tartrazine, allura red, titanium dioxide, or mixtures thereof.
Examples of film-forming polymers include hydroxypropyl methylcellulose, methyl cellulose, carboxymethyl cellulose, hydroxyethyl cellulose, polyethylene glycol, polyvinyl alcohol, or mixtures thereof. Alternatively, commercially available coating compositions comprising film-forming polymers marketed under various trade names, such as Opadry®, may also be used for coating.
Coating may be carried out by using any conventional coating techniques known in the art, such as spray coating in a conventional coating pan, fluidized bed processor, or dry powder coating.
EXAMPLES
Example 1
Figure imgf000007_0001
Manufacturing process:
1. Apixaban, lactose monohydrate, microcrystalline cellulose, sodium lauryl sulphate and croscarmellose sodium were sifted together.
2. Povidone was dissolved in dichloromethane to obtain a solution.
3. Blend of step 1) was granulated with solution of step 2) to obtain granules.
4. Granules of step 3) were lubricated with magnesium stearate.
5. Lubricated granules of step 4) were compressed into a suitable size tablet.
6. Tablets obtained in step 5) were coated with Opadry™ Pink dispersion. Dissolution studies
The dissolution tests were carried out using tablets prepared in Example 1 and Eliquis® tablet.
The dissolution was carried out in United States Pharmacopeia (USP) type 2 dissolution apparatus, at a stirring speed of 75 rpm, at a temperature of 37±0.5°C, in 900 mL of pH 6.8 phosphate buffer containing 0.05% SLS.
Table 1: Dissolution profile of Example 1 and Eliquis® tablet.
Figure imgf000008_0001
The results of the dissolution tests are shown in Table 1. It is evident that tablets prepared according to Example 1 provide a release profile which is comparable to Eliquis® tablet.

Claims

We claim:
1. A pharmaceutical composition comprising wet granulated apixaban and at least one pharmaceutical excipient, wherein the wet granulated apixaban is granulated using an organic solvent and the composition releases at least 80% of apixaban in 30 minutes, when measured in United States Pharmacopeia (USP) type 2 dissolution apparatus, paddle at a stirring speed of 75 rpm and at a temperature of 37°C ± 0.5°C in 900 mL of pH 6.8 phosphate buffer with sodium lauryl sulphate.
2. The pharmaceutical composition according to claim 1, wherein at least 85% of the apixaban is released in 30 minutes.
3. The pharmaceutical composition according to claim 1, wherein the apixaban is in crystalline form.
4. The pharmaceutical composition according to claim 1, wherein the apixaban has a particle size D90 of not less than 100 μιη.
5. The pharmaceutical composition according to claim 1, wherein the composition is stable at a temperature of 40°C and a relative humidity of 75% for a period of 3 months.
6. The pharmaceutical composition according to claim 1, wherein the wet granulated apixaban is prepared by non-aqueous granulation.
7. The pharmaceutical composition according to claim 1, wherein the ratio of organic solvent to intra-granular mass during the granulation process ranges from about 1 :0.2 to about 1 :0.6.
8. The pharmaceutical composition according to claim 1, wherein organic solvent is selected from the group consisting of ethanol, isopropyl alcohol, dichloromethane, dimethylsulphoxide, dimethylformamide, N-methyl-2-pyrrolidone, dimethylacetamide, acetic acid or mixtures thereof.
9. The pharmaceutical composition according to claim 1, wherein the organic solvent is dichloromethane.
10. The pharmaceutical composition according to claim 1, wherein the apixaban is granulated using high shear wet granulation.
11. The pharmaceutical composition according to claim 10, wherein the apixaban is granulated in a rapid mixer granulator.
12. The pharmaceutical composition according to claim 1, wherein the process of preparation comprises:
a) dissolving/dispersing apixaban in an organic solvent;
b) blending and granulating the pharmaceutically acceptable excipients with the solution/dispersion of step a); and
c) compressing/filling the granules of step b) into suitable size tablets/capsules.
13. The pharmaceutical composition according to claim 12, wherein the solution or dispersion further comprises one or more pharmaceutically acceptable excipients.
14. The pharmaceutical composition according to claim 12, wherein the apixaban may be partly added to the pharmaceutically acceptable excipients of step b).
15. The pharmaceutical composition according to claim 1, wherein the process of preparation comprises:
a) Granulating the apixaban with a granulating liquid prepared using an organic solvent to form granules;
b) blending the granules of step a) with one or more pharmaceutically acceptable excipients; and
c) compressing/filling the granules of step b) into suitable size tablets/capsules.
16. The pharmaceutical composition according to claim 15, wherein a portion of the apixaban is added to the granulating liquid of step a).
PCT/IB2017/051605 2016-03-21 2017-03-20 Pharmaceutical composition comprising apixaban WO2017163170A1 (en)

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Cited By (9)

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CN108553441A (en) * 2018-06-08 2018-09-21 北京阳光诺和药物研究有限公司 A kind of Apixaban tablet and preparation method thereof
CN108645933A (en) * 2018-05-24 2018-10-12 河北常山生化药业股份有限公司 The gas-chromatography detection method of residual solvent in Eliquis bulk pharmaceutical chemicals
WO2019177318A1 (en) * 2018-03-13 2019-09-19 Chong Kun Dang Pharmaceutical Corp. Pharmaceutical formulation for solubilization comprising apixaban and its preparation method
CN110772490A (en) * 2019-10-31 2020-02-11 宁波高新区美诺华医药创新研究院有限公司 Preparation method of apixaban tablets
EP3669866A1 (en) 2018-12-19 2020-06-24 KRKA, d.d., Novo mesto Pharmaceutical composition comprising apixaban
EP3582777A4 (en) * 2017-02-17 2020-12-23 Unichem Laboratories Ltd Pharmaceutical composition of apixaban
WO2022115051A1 (en) * 2020-11-27 2022-06-02 Santa Farma Ilac Sanayii A.S. Direct compression method for non-micronised apixaban formulations
WO2022150030A3 (en) * 2021-01-08 2022-08-25 Sanovel Ilac Sanayi Ve Ticaret Anonim Sirketi A film coated tablet of apixaban
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WO2022150030A3 (en) * 2021-01-08 2022-08-25 Sanovel Ilac Sanayi Ve Ticaret Anonim Sirketi A film coated tablet of apixaban
WO2023115593A1 (en) * 2021-12-26 2023-06-29 浙江海正药业股份有限公司 Apixaban tablet and preparation process therefor

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