The invention relates to novel crystalline forms of Apremilast and pharmaceutical compositions/dosage forms containing same. It also refers to processes for preparing said dosage forms and the use thereof for treating patients. Finally, the invention pertains to the use of said novel crystalline forms for the preparation of a pharmaceutical composition or dosage form.
Apremilast, i.e. N-[2-[(1S)-1-(3-ethoxy-4-methoxyphenyl)-2-(methylsulfonyl)ethyl]-1,3-dioxo-2,3-dihydro-1H-isoindol-4-yl]acetamide), also referred to herein as “APM”, has the following chemical formula, wherein “S”, if not connected via a chemical bond in the formula, denotes the S-form of the chiral center.
Apremilast is a phosphodiesterase 4 inhibitor and blocks the action of an enzyme inside cells called phosphodiesterase 4 (PDE4). This enzyme plays a role in triggering the production of messenger molecules in the immune system called cytokines, which are involved in inflammation and other processes that cause psoriasis and psoriatic arthritis. By blocking PDE4, Apremilast reduces the level of these cytokines in the body, and so reduces the inflammation and other symptoms of psoriasis and psoriatic arthritis. Apremilast is the active ingredient of the medicament Otezla®, distributed by Celgene, Ltd, for the treatment of adults with psoriatic arthritis (inflammation of the joints associated with psoriasis) and moderate to severe plaque psoriasis (a disease causing red, scaly patches on the skin).
EP2276483 B1 discloses various polymorphic forms of Apremilast, i.e. Forms A, B, C, D, E, F and G. Regarding the characterization of these Forms A, B, C, D, E, F and G, in particular their XRPD peak locations and intensity, reference is made to EP2276483 B1. The stability, interconversion and equilibration studies in EP2276483 B1 show that most of these crystalline forms have a high tendency of interconversion, i.e. one polymorphic form converts into another polymorphic form in the presence of solvents.
The invention particularly relates to crystalline (solid) forms of N-[2-[(1S)-1-(3-ethoxy-4-methoxyphenyl)-2-(methylsulfonyl)ethyl]-1,3-dioxo-2,3-dihydro-1H-isoindol-4-yl]acetamide), i.e. Form N, Form M, Form O and Form P. It also refers to pharmaceutical compositions and dosage forms comprising said crystalline forms. The invention also concerns said pharmaceutical compositions or dosage forms for use in a method of treating a disease or disorder defined in the claims. Finally, the invention pertains to the use of said novel crystalline forms for the preparation of pharmaceutical compositions and dosage forms.
Although Form B is the commercially available form of Apremilast (Otezla®) and has quite good properties, there is a constant need for improvement of existing dosage forms.
Accordingly, one objective underlying the present invention was to improve the existing dosage forms.
It has unexpectedly been found that it is possible to provide new valuable polymorphic forms of Apremilast, designated Forms N, M, O and P herein. The crystalline forms described herein may have various benefits over the known crystalline forms.
In particular, it has been found that tablets comprising Form N show an improved dissolution profile as compared with tablets comprising Form B, wherein Form B is the commercially available form of Apremilast (Otezla®), see Experiment 9 and
Since EP2276483 B1 already discloses various polymorphic forms of Apremilast, it was not foreseeable, whether further polymorphic forms exist and can be prepared at all. In view of the high interconversion tendency of the known polymorphic forms, it was particularly unexpected that a new, substantially non-hygroscopic and stable (with respect to humidity) polymorph can be prepared (e.g. Form N). It is worth noting that EP2276483 B1 already describes 3 unsolvated or anhydrous crystalline forms, i.e. Forms A, B and F. Therefore, one could not have expected that a further unsolvated, anhydrous form can be prepared, let alone a stable form. Accordingly, there was no reasonable expectation of success that the problems underlying the present invention can indeed be solved by investigating the possible existence of further stable polymorphs. Rather, a skilled person seeking to improve the existing dosage forms would have modified the composition (type and amounts of excipients) of the marketed dosage form or would have improved the structure/type of said final drug dosage forms.
Furthermore, unexpectedly, crystalline Form M of Apremilast has been found, which is also substantially non-hygroscopic. In particular, Form M of Apremilast has superior solubility, particularly compared to prior art Form B. Water solubility of prior art Form B according to literature findings and experimental data is about 7-12 μg/ml, while water solubility of Form M is almost 3 times greater at the same conditions, i.e. is 29 μg/ml. Form B crystallizes as needle-like crystals. Needle-like crystal morphology can cause problems with filterability and flow characteristic. Form M crystallizes as prismatic crystals that have good flow characteristics and filterability and do not form aggregates.
Accordingly, the objective underlying the present invention has been solved.
The invention is further described with respect to the following items:
The solvent molecules, i.e. ethyl acetate, are contained in the crystal lattice.
The solvent molecules, i.e. dimethylacetamide, are contained in the crystal lattice.
The solvent molecules, i.e. dimethylformamide, are contained in the crystal lattice.
By way of example, the dosage form can be prepared by using a process comprising or consisting of the following steps:
By way of example, the dosage form can be prepared by using a process comprising or consisting of the following steps:
Within the meaning of the present invention, the term “solvent” refers to any solvent such as water and organic or inorganic solvents.
The term “room temperature” as used herein is understood to mean temperatures of about 15° C. to about 25° C.
Herein, the X-ray powder diffraction peaks of the crystalline Apremilast forms are described by their 2theta angles with a tolerance of “±0.2”. In the context of the present invention, it is also possible to use a smaller tolerance of “±0.1” or even “±0.0”.
Herein, Forms M and N are preferred, wherein Form N is most preferred.
Regarding the synthesis of Apremilast, reference is made to Example 1 herein, as well as to EP2276483 B1 and U.S. Pat. No. 6,962,940. Apremilast as the starting material for crystallizing any of Forms N, M, O and P of the present invention can be prepared by using any method.
Purity and assay analysis were carried out using Ultra Performance Liquid Chromatograph Waters Acquity I-Class equipped with PDA detector. The analysis were conducted using Waters Acquity UPLC BEH C18 1.7 μm, 2.1×100 mm column, at a temperature of 60° C. The mobile phases were acetonitrile and 0.1% (v/v) ortho-phosphoric acid in water used in gradient.
Determination of residual solvents were carried out using Perkin Elmer Clarus 680 Gas Chromatograph with flame-ionization detector (FID) with carrier gas split, equipped with TurboMatrix 110 Trap a headspace autosampler. The capillary column 60 m×0.32 mm ID×1.8 μm and stationary phase (6%)-cyanopropyl-phenyl-(94%)-dimethylsiloxane DB-624 Agilent Technologies at the temperature gradient were used.
Water content in samples of Apremilast were determined using Mettler Toledo V30 Karl Fisher Titrator. The analysis were carried out using acetonitrile:methanol (50:50) solution and the Combi Titrant 2 Merck titrant.
The analysis of the crystals by X-Ray diffraction was performed using X-ray Diffractometer Rigaku MiniFlex 600 in Bragg-Brentano geometry Cu Kα radiation, D/teX Ultra Detector in a range of λ=36° of 2θ angle. The wavelength of the Cu-Kα radiation used herein is λ=1.5406 Angstrom. The patterns were recorded at a tube voltage of 40 kV, tube current of 15 mA, applying a step size of 0.013° 2° with 80 s per step.
DSC analysis were carried out using DSC 1 Mettler Toledo Stare thermal analysis system at the temperature range of 25−250° C. with the gradient of 5° C./min. Melting, aluminum crucible with the capacity of 40 μl were used. Nitrogen was used as carried gas with the flow of 50 ml/min.
TGA analysis were carried out using TGA/SDTA85 Mettler Toledo Stare thermal analysis system at the temperature range of 25−220° C. with the gradient of 7° C./min. Melting, aluminum crucible with the capacity of 100 μl were used. Nitrogen was used as carried gas with the flow of 50 ml/min.
Water Vapour Sorption isotherms were obtained using a Dynamic Vapour Sorption apparatus (model: DVS—Advantage, supplier: Surface Measurement Systems Limited). The DVS apparatus consists of an ultra-microbalance housed inside a temperature-controlled cabinet. The sample was placed into a DVS sample pan under a stream of nitrogen (200 sccm) at 25° C. The humidity was increased ramping in 10% RH (relative humidity) steps from close to 0% RH to 90% RH (sorption phase). Next the humidity was decreased in a similar fashion for the desorption phase. The sample was held at each RH step for mass stabilization (dm/dt 0.02%/min) but not less than 10 minutes. Two cycles of sorption and desorption were investigated.
Dissolution studies were performed using a Hanson SR8PLUS dissolution apparatus, according to European Pharmacopoeia apparatus, paddle method. The samples were tested in 900 mL pH 6.8 with 0.3% SLS at 37.0° C.+/−0.5° C. and the paddle rotation speed was set at 75 rpm. Dissolution study was conducted for 60 min and samples were analyzed using HPLC method.
A test for stability against humidity can be performed as follows: The sample is exposed to a relative humidity of 75% (+/−5%) at 50° C. (+/−2° C.) for 2 weeks. The expression “polymorphically stable” means that no conversion to another crystalline form occurs, as determined by XRPD.
The equilibrium relative humidity of a sample is measured by determining the relative humidity in % in the air above a test sample, after establishment of a humidity equilibrium in a closed/open system at a constant temperature.
The step of formulating the crystalline forms into a dosage form may be carried out by applying techniques known in the art, in particular as described herein. For example, the crystalline forms can be formulated into tablets by using direct compression, granulation processes, and spraying processes as described above. Examples are also given in the experimental part herein.
Exemplary pharmaceutically acceptable excipients which can be contemplated for use in the present invention are described in the following:
Binding agents are excipients which increase the adhesion of the active agents and excipients during granulation. Examples of binding agents are: sugars, such as sorbitol, glucose, fructose, disaccharides as saccharose, polysaccharides; acacia gum; cellulose derivatives, such as soluble celluloses like microcrystalline cellulose, methylcellulose, hydroxypropylmethylcellulose and hydroxypropylcellulose; tragacanth; polyvinylpyrrolidone, such as polyvinylpyrrolidone-vinyl acetate copolymer, or N-vinylpyrrolidone; sodium alginate and alginate derivatives and gelatin.
Disintegrants are excipients which can take up water and swell and thus improve disintegration of a tablet or granules. Examples of disintegrants are: crospovidone, croscarmellose sodium; starch (paste and pre-gelatinized), such as sodium starch glycolate, methacrylic acid polymer with divinylbenzene, potassium salt, Maltodextrin; croscarmellose sodium and low substituted hydroxypropylcellulose and crospovidone.
Lubricants are excipients which reduce the friction between excipients and compression tooling surfaces. Examples of lubricants are magnesium stearate, magnesium fumarate, fumaric-acid, talc, steraric acid and sodium stearylfumarate.
Fillers are excipients which increase the volume of e.g. tablets. Examples of fillers are mannitol, celluloses such as microcrystalline cellulose, synthetic polymers, Ca-phosphate, inorganic calcium salts, maize starch, polyols and pregelatinzed starch.
A polymer, or a plurality of polymers may be used for coating tablets, including for example cellulose derivatives, e.g. hydroxypropylmethylcellulose, polyvinylpyrrolidones, polyethyleneglycols, polyvinylalcohols, acrylates, such as polymethacrylate, cyclodextrins and copolymers and derivatives thereof, including for example polyvinylpyrolidine-vinylacetate. In some preferred embodiments the polymer or the plurality of polymers are pH dependent enteric polymers. Such polymers include cellulose derivatives, e.g. cellulose acetate phthalate, hydroxypropyl methyl cellulose phthalates, hydroxypropyl methyl acetate succinate, hydroxypropyl methyl cellulose acetate, carboxymethylcellulose or a salt thereof, e.g the sodium salt, cellulose acetate trimellitate, hydroxypropylcellulose acetate phthalate, or polymethylacrylates, e.g. Eudragit®S.
Surfactants include but are not limited to, sorbitan fatty esters, polyoxyethylene sorbit esters, sodium laurylsulfate, sodium docedylbenzenesulfate, dioctyl sodium sulfosuccinate, sodium stearate, EDTA or vitamin E or tocol derivates.
Most preferred for preparing pharmaceutical compositions/dosage forms is the use of one or more, preferably all, of lactose monohydrate, microcrystalline cellulose, magnesium stearate and croscarmellose sodium.
Other excipients are known in the art and can be chosen by a skilled person depending on their function.
The preparation of Form N is described in Example 1. Crystalline Form N of Apremilast can be characterized as already described above. It has an X-ray powder diffraction pattern as depicted in
Form N of Apremilast may also (further) be characterized by thermal analysis. A representative DSC plot for Form N of Apremilast is shown in
A representative TGA plot for Form N of Apremilast is shown in
Form N of Apremilast may be characterized by moisture sorption analysis. A representative moisture sorption isotherm plot is shown in
Crystalline Form N of Apremilast can be characterized by having a dissolution profile as shown in
The preparation of Form M is described in Example 2 (see also
The crystalline Form M of Apremilast can be characterized as described above and has an X-ray powder diffraction pattern as depicted in
Form M of Apremilast may be also (further) characterized by thermal analysis. A representative DSC plot for Form M of Apremilast is shown in
A representative TGA plot for Form M of Apremilast is shown in
Form M of Apremilast may be characterized by moisture sorption analysis. A representative moisture sorption isotherm plot is shown in
Table 8 shows the atomic coordinates and equivalent isotropic temperature parameters for non-hydrogen atoms.
Table 9 shows the Bond lengths (A) in Form M of Apremilast.
Table 10 shows the Bond Angles (Q) in Form M of Apremilast.
166(3)
The crystal structure is additionally stabilized by the presence of strong N—H . . . O hydrogen bonds and many weaker C—H . . . O interactions (Table 11). Table 11 shows the inter- and intramolecular hydrogen bonds (Å, °).
Characterization of Form O (containing dimethyl acetamide solvent molecules) of Apremilast
The preparation of Form O is described in Example 3 (see also
Form O of Apremilast may be also (further) characterized by thermal analysis. A representative DSC plot for Form O of Apremilast is shown in
A representative TGA plot for Form O of Apremilast is shown in
The preparation of Form P is described in Example 4 and
Form P of Apremilast may be also (further) characterized by thermal analysis. A representative DSC plot for Form P of Apremilast is shown in
A representative TGA plot for Form P of Apremilast is shown in
The following examples describe the present invention in detail, but are not to be construed to be in any way limiting for the present invention.
The below preparation serves as a non-limiting example for preparing APM. Any other method for preparing APM is also suitable in the context of the present invention.
Reference is made to
When the reaction was finished (after 2-4 h at 110-120° C.) the solution was cooled down to a temperature of 20-25° C. Ethyl acetate (180 ml) and water (180 ml) were added to the reaction mixture and the reaction mass was stirred for 10 min at 20-30° C. After separation, the ethyl acetate phase was left and the water phase was extracted with ethyl acetate (2×50 ml). The combined ethyl acetate phases were washed with 8% NaHCO3 solution (2×50 ml), 1N HCl (2×50 ml), and water (1×50 ml). The organic solvent was evaporated under reduced pressure (200-30 mbar) at 35° C. giving compound APM (as an oil residue left after ethyl acetate distillation).
Reference is made to
10 g of Apremilast were suspended in diethyl ether (200 ml) and stirred for 12 h at 25±5° C. to give a white to cream color suspension. Obtained solid was filtered under reduced pressure and dried at 85° C. and gave product APM Form N (as confirmed by XRPD, DSC and TGA) with purity above 99.90% (80-90% yield).
Reference is made to
Reference is made to
Crystallization of N-[2-[(1S)-1-(3-ethoxy-4-methoxyphenyl)-2-(methylsulfonyl)ethyl]-1,3-dioxo-2,3-dihydro-1H-isoindol-4-yl]acetamide) (APM) Form M as the hemi ethyl acetate solvate is shown in
10 g Apremilast were dissolved in ethyl acetate (52 ml) and heated to 77° C. The solution was stirred for 30 min at boiling temperature and then cooled down to −5 to −10° C. The mass was stirred for 3-6 h at about −5 to −10° C. to give a white to cream color suspension. The obtained solid was filtered under reduced pressure and the cake was washed with cold ethyl acetate (2×5 ml). Drying at reduced pressure at 50° C. gave product APM hemi-ethyl acetate form (as confirmed by XRPD, DSC, GC and TGA) with a purity of above 99.90% (88-92% yield).
Crystallization of N-[2-[(1S)-1-(3-ethoxy-4-methoxyphenyl)-2-(methylsulfonyl)ethyl]-1,3-dioxo-2,3-dihydro-1H-isoindol-4-yl]acetamide) (APM) Form O as the hemi DMA solvate is shown in
10 g of Apremilast were dissolved in dimethyl acetamide (40 ml) and stirred for 30 min at 25±5° C. until a clear solution was obtained. The solution was stirred for 72 h at 25±5° C. to give a white to cream color suspension. The obtained solid was filtered under reduced pressure and dried at 50° C., which gave product APM Form O (as confirmed by XRPD, DSC and TGA) with purity above 99.90% (70-80% yield).
Reference is made to
Tablets comprising Form B were prepared as follows:
Apremilast, lactose monohydrate, microcrystalline cellulose, croscarmellose sodium were passed through a 0.425 mm sieve. The ingredients from the sieving step are mixed in a blender for 15 min at 25 RPM (rotations per minute). Magnesium stearate is added and the mixture is mixed for 5 min at 12 RPM. The resulting blend is compressed using a single punch machine equipped with an oval punch (14×8 mm) at a compression force of 7 kN. The composition of the tablets is shown in Table 14.
Stability Results after 2 Weeks (Conditions Either Closed or Open):
Tablets comprising an amorphous form of APM were prepared as follows:
Apremilast (Form M) was dissolved in acetone. Lactose monohydrate, microcrystalline cellulose, croscarmellose sodium were passed through a 0.425 mm sieve. The ingredients from the previous step were added to a fluid bed granulator (equipped with top spray nozzle) and granulated by spraying the solution. The obtained granulate was dried. Magnesium stearate was added and mixed for 5 min at 12 RPM. The blend was compressed using a single punch machine equipped with oval punch (14×8 mm) at a compression force of 7 kN.
Stability Results after 2 Weeks (Conditions Closed or Open):
Sample 004 comprising Form N was prepared as follows:
Apremilast Form N, lactose monohydrate, microcrystalline cellulose, croscarmellose sodium were passed through a 0.425 mm sieve. The ingredients from the previous step were mixed in a blender for 15 min at 25 RPM. Magnesium stearate was added and the resulting mixture was mixed for 5 min at 12 RPM. The resulting blend was compressed using a single punch machine equipped with oval punch (14×8 mm) at a compression force of 7 kN
Stability Results after 2 Weeks:
The dissolution profile of Apremilast Form N and Form B, prepared above, in buffer at pH 6.8+0.3% SLS is shown in Table 20 (see also
When compared with prior art Form B, Form N exhibits a higher dissolution rate by more than 50% at 30 minutes.
Number | Date | Country | Kind |
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16169453.4 | May 2016 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/PL2016/000129 | 11/21/2016 | WO | 00 |