Patent Application
20130084335
The present invention relates to a pharmaceutical composition containing ivabradine or a pharmaceutically acceptable salt thereof. Further, the invention relates to a method for the preparation of such a composition.
Ivabradine has the chemical designation (S)-3-{3-[(3,4-dimethoxybicyclo[4.2.0]octa-1,3,5-triene-7-ylmethyl)methylamino]propyl}-7,8-dimethoxy-2,3,4,5-tetrahydro-1H-3-benzazepine-2-one. Ivabradine has the following structural formula (I):
Synthesis routes for the preparation of ivabradine and its use for preventing and treating various clinical conditions of myocardial ischaemia, supraventricular arrhythmias and coronary arteriosclerotic episodes are reported to be disclosed in EP 534 859.
Ivabradine is an active substance reported to have a bradycardiceffect for the treatment of stable angina pectoris, in particular in patients for whom beta-blockers are contraindicated or an intolerance of beta-blockers is present. Ivabradine is reported to selectively inhibit the If-ion current, which, as an intrinsic pacemaker in the heart, controls the spontaneous diastolic depolarisation in the sino-atrial node and thus regulates the heart rate. Under physiological conditions, ivabradine, the S-enantiomer of a racemate, is reported to have a very good solubility (>10 mg/ml).
The prior art apparently discloses administration forms of ivabradine, which release the active substance substantially without a time delay. The administration form Procoralan® (Servier), which is prepared by wet granulation, releases ivabradine rapidly and almost completely after oral intake. WO 2003-061662 apparently discloses an ivabradine-containing, orally dispersible tablet, which releases the active substance very rapidly in the mouth.
Moreover, various polymorphic forms of the ivabradine hydrochloride are reported to be described in the state of the art. WO 2005/110993 A1 apparently discloses polymorph alpha, WO 2006/092493 A1 apparently discloses polymorph beta, WO 2006/092491 A1 apparently discloses polymorph beta d (dehydrated). In addition, polymorph gamma, polymorph gamma d, polymorph delta, and polymorph delta d are reported to be known in the art. In addition, WO2008/065681 apparently reports the so-called Form I of Ivabradine HCl. WO 2008/146308 A2 apparently discloses amorphous ivabradine.
Also various salts of ivabradine are apparently known in the art. WO 2008/146308 A2 apparently discloses ivabradine oxalate, WO 2009/124940 A1 discloses ivabradine hydrobromide.
The problem with the salts and polymorphs of the ivabradine, in particular the polymorphs of the hydrochloride, is that these salt forms are not sufficiently stable under all conditions. This, in turn can lead to problems in the processing as well as the storage and to undesired reactions with the excipients employed in the preparation of the pharmaceutical composition.
Thus, it is an object of the present invention to provide a pharmaceutical composition in the preparation and later storage of which the employed polymorphic form of the active substance is stable.
A further problem with the ivabradine-containing pharmaceutical compositions is that the amount of active substance in the formulation to be administered is usually only small. This leads to problems in the preparation of the corresponding compositions due to possible variations in content that are for example conditional on separation tendencies of the active substances and excipients. Therefore, it is important that at first active substances and excipients can be mixed as homogenous as possible and corresponding mixtures do not separate again during further processing to the final formulation. An inhomogeneous distribution of the active substance can result in undesired side effects up to symptoms of poisoning. Also the bioavailability as well as the effectiveness of corresponding formulations may be affected adversely in an inhomogeneous distribution of the active substance.
It has been shown that neither problems regarding the stability of the employed polymorphic form of the active substance nor problems regarding the homogeneous distribution of the active substance in the final formulation can be solved by simply mixing and compressing the constituents.
Thus, a further object of the present invention is to provide a pharmaceutical composition that ensures a distribution of the active substance in the final formulation that is as homogeneous as possible. At the same time, the employed polymorphic form should remain stable both in the preparation of the composition and the later storage.
Now, it has surprisingly been found that the above-mentioned problems can be solved in that at least 95% by weight of the active substance in the pharmaceutical composition have an average particle size in the range of 0.5 μm to 250 μm.
Thus, the present invention relates to a pharmaceutical composition containing ivabradine as active substance or a pharmaceutically acceptable salt thereof wherein at least 95% by weight of the active substance based on the total weight of the active substance have an average particle size in the range of 0.5 μm to 250 μm.
Presently, by “active substance” ivabradine in the form of the free base or a pharmaceutically acceptable salt thereof is meant. A suitable pharmaceutically acceptable salt is for example the hydrochloride, the hydrobromide, the oxalate, the sulfate, the phosphate, the acetate, the propionate, however also salts of the ivabradine with propionic acid, maleic acid, fumaric acid, tartaric acid, nitric acid, benzoic acid, methanesulfonic acid, isethionic acid, benzenesulfonic acid, citric acid, toluenesulfonic acid, trifluoroacetic acid, and camphoric acid and also the lactate, pyruvate, malonate, succinate, glutarate, and ascorbate of the ivabradine. Further, the following salts can be employed: L-aspartate, glutamate, sorbate, acinotate, gluconate, hippurate, and salts of the ivabradine with ethanesulfonic acid, mandelic acid, adipic acid, or sulfamic acid. The salts of the ivabradine can be obtained in accordance to methods reported to be known in the art by reacting the free base of the ivabradine with the corresponding acid or by the presence of the corresponding acid in the synthesis of the ivabradine, as reported to be described for example in US 2005/0228177 A1. Preferred are ivabradine hydrochloride, hydrobromide, and oxalate, particularly preferred is ivabradine adipate.
In particular, if ivabradine is used as adipate salt, the pharmaceutical composition according to the present invention is stable under usual storage conditions.
The active substance can be present in the pharmaceutical composition of the present invention both in the crystalline and amorphous form. The active substance includes all polymorphic forms of ivabradine or a pharmaceutically acceptable salt thereof, including hydrates and solvates. Preferably, the active substance is present in the crystalline form.
Ivabradine adipate can be obtained by adding adipic acid, e.g. about one equivalent, in a suitable solvent, such as ethanol, to a solution of ivabradine in a suitable solvent, such as dichlormethane. Crystalline ivabradine adipate product can be obtained by removal of the solvent, e.g. under vacuum at about 40° C. Crystalline ivabradine adipate can also be obtained by adding a solution of adipic acid in water to a solution of ivabradine in ethanol, and removal of the solvent.
The DSC thermogramm of ivabradine adipate shows a peak at about 115° C. The melting point is in the range of about 113° C. to about 117° C.
Ivabradine adipate is characterized by an XRD pattern having a characteristic peak at 20.6±0.2 degrees 2-theta, in particular having characteristic peaks at 14.6±0.2, 16.0±0.2, 18.8±0.2, 20.6±0.2, 23.2±0.2, 24.3±0.2, 25.9±0.2 and 26.3±0.2 degrees 2-theta, and further at 8.6±0.2, 9.6±0.2, 12.1±0.2 and 12.9±0.2 degrees 2-theta. The XRD pattern of ivabradine adipate is shown in
It has been shown that the uniformity of the content of active substance of ivabradine-containing pharmaceutical compositions can be ensured when the average particle size of the active substance is in the range of 0.5 μm to 250 μm. This way, the separation tendency in the preparation of the composition is reduced so that the variations in content in the finished composition can be prevented. Moreover, it has surprisingly shown that the pharmaceutical composition can be prepared by simple mixing and compressing with correspondingly small active substance particles without leading to a change of otherwise instable polymorphic forms of the active substance. This way it is possible to obtain the pharmaceutical composition according to the invention without the necessity of an otherwise usual and for the commercial ivabradine-containing drug Procoralan® used wet granulation by a simple dry processing of the constituents. So, the employment of special machines necessary for the wet granulation can be avoided. Moreover, the employment of solvents for the preparation of the wet mass can be avoided. It is also not necessary to expose the active substance for a longer period to the granulation liquid until the completion of the drying. In addition, the drying step following the wet granulation requires additional energy and the active substance is exposed to thermal influences over a longer period. In contrast, using the active substance with a particle size in the range of 0.5 μm to 250 μm permits the preparation of the pharmaceutical composition according to the invention by direct compressing or dry compaction in the absence of solvents so that the above-mentioned problems in the preparation of conventional ivabradine-containing formulations are overcome. The preparation of the pharmaceutical composition according to the invention by direct compressing is particularly preferred.
The pharmaceutical composition according to the invention contains at least 95% by weight, in particular at least 98% by weight of the active substance based on the total weight of the active substance in an average particle size in the range of 0.5 μm to 250 μM, preferably in the range of 0.8 μm to 200 μm, in particular in the range of 1 μm to 150 μm.
In a further embodiment of the present invention the pharmaceutical composition contains particles of the active substance having an average particle size D50 in the range of 1 μm to 70 μm, preferably of 5 μm to 50 μm, most preferably of 10 μm to 25 μm.
In a further embodiment of the present invention the pharmaceutical composition contains particles of the active substance having an average particle size D90 in the range of 0.5 μm to 250 μm, preferably of 30 μm to 80 μm, most preferably of 40 μm to 60 μm.
The term “particle size” according to the present invention relates to the maximum diameter of the equivalent product assuming spherical opaque particles showing the same light scattering pattern and the same diffraction as the active substance particles. According to the invention the particle size is determined by means of laser light diffraction. The determination of the size distribution results from the analysis of the diffraction pattern that is obtained if particles are exposed to a monochromatic light beam. The particles refract the light with small particles refracting the light in a greater angle than large particles. The refracted light is measured by a number of photo detectors arranged in different angles. On the other hand, the light spectra of the small particles have to be recorded by light-sensitive detectors in greater angles over the laser beam. Large particles result in greater intensity maxima with small angles, small particles to weaker intensity maxima with greater angles. Thus, in the laser light diffraction the pattern resulting from the interaction of the light with the particles is used for the determination of the particle size.
The “particle size distribution” is a statistical frequency distribution. Here, the particles are divided into classes according to their size.
The particle size distribution of the particle size D50 value includes 50% of the particles based on their volume with a particle size smaller than the D50 value and 50% of the particles based on their volume with a particle size greater than the D50 value.
The particle size distribution of the particle size D90 value includes 90% of the particles based on their volume with a particle size smaller than the D90 value and 90% of the particles based on their volume with a particle size greater than the D90 value.
The particle size distribution according to the present invention can be monomodal or bimodal. In the preferred embodiment of the invention the particle size distribution of the active substance is monomodal. The term “monomodal” relates to the peak resulting in a histogram and/or graph representing the distribution frequency. Generally, in the graphical representation of a particle size distribution there are plotted the diameter x on the abscissa and the measure of a set Q on the ordinate.
According to the invention the particle size is determined by means of laser diffractometry. For that, a Mastersizer 2000 by Malvern Instruments having the corresponding sample dispersing unit Hydro S is used. The wet measurement (2500 rpm, ultrasound 10-20 min., shading 5 to 20%) takes place in a dispersion of sunflower oil with the particle spacing in the dispersion being about 3-5 times greater than the particle diameter.
Here, the average particle size of the active substance is determined according to the following method: In principle, the Fraunhofer diffraction theory is used for particle fractions the particle size of which is significantly greater than the wave length of the laser light. (ISO 13320)
Moreover, the Mie theory defines the secondary scattering caused by the refraction of the light on small particles, as in the international rules of the laser diffraction measurement. (ISO 13320)
The determination of the particle size for particles D50 smaller than 5.0 μm is carried out according to the Mie method and for particles D50 greater than 5.0 μm according to the Fraunhofer method.
In a further aspect of the present invention it has been shown that the separation tendency of ready-made mixtures containing the active substance and the excipients is reduced in the further processing by addition of an adhesion enhancer. Additionally, it has been shown that an adhesion enhancer is suitable to stabilize the polymorphic form of the employed active substance in compacted or compressed form. By adding the adhesion enhancer it usually comes to an enlargement of the interparticle surfaces at which more easily (e.g. in the compressing operation) contact points can be formed. Moreover, adhesion enhancers are wherein they increase the plasticity of the tabletting mixture so as to form solid tablets during compressing.
Particularly suitable as adhesion enhancers are polymers, fats, waxes, non-polymeric compounds having at least one polar side group. The employed adhesion enhancer should be in the solid form at room temperature.
In one embodiment of the present invention the employed adhesion enhancer is a polymer that has a glass transition temperature (Tg) of >15° C., preferably 40° C. to 150° C., and in particular 50° C. to 100° C. Here, the glass transition temperature is that temperature at which the amorphous or partly crystalline polymer changes from the solid to the liquid state. Here, a significant change of physical parameters such as hardness and elasticity occurs. Typically, below the glass transition temperature a polymer is glassy and hard, above the glass transition temperature it changes into a rubber-like to viscous state. The determination of the glass transition temperature takes place in the context of this invention by means of differential scanning calorimetry (DSC). For that, for example a device of Mettler Toledo DSC 1 can be used. It works with a heating rate of 10° C.
The polymer used as the adhesion enhancer preferably has a number average molecular weight of 1,000 g/mol to 500,000 g/mol, more preferred of 2,000 g/mol to 90,000 g/mol. Additionally, the polymer used should have a viscosity of 0.1 mPa/s to 8 mPa/s, preferably of 0.3 mPa/s to 7 mPa/s, and in particular of 0.5 mPa/s to 4 mPa/s in a 2% by weight solution in water, each measured at 25° C.
Preferably, there can be employed hydrophilic polymers as the adhesion enhancers. This refers to polymers having hydrophilic groups, for example hydroxy, alkoxy, acrylate, methacrylate, sulfonate, carboxylate, and quarternary ammonium groups.
According to the invention the polymer used as the adhesion enhancer can be selected from the group consisting of polysacharides, such as hydroxypropylmethylcellulose (HPMC), carboxymethylcellulose (CMC), ethylcellulose, methylcellulose, hydroxyethyl-cellulose, ethylhydroxyethylcellulose, and hydroxypropylcellulose (HPC), micro-crystalline cellulose, guar gum, alginic acid, alginates, polyvinylpyrrolidone, polyvinylacetates (PVAC), polyvinyl alcohols (PVA), polymers of the acrylic acid and its salts, polyacrylamides, polymethacrylates, vinylpyrrolidone vinylacetate copolymers, polyalkylene glycoles, such as poly(propylene glycol) and polyethylene glycol, co-blockpolymers of the polyethylene glycol, in particular co-blockpolymers of polyethylene glycol and poly(propylene glycol) as well as mixtures of two or more of the mentioned polymers.
Preferably used as the adhesion enhancers are polyvinylpyrrolidone, especially having a weight average molecular weight of 10,000 g/mol to 60,000 g/mol, in particular 12,000 g/mol to 40,000 g/mol, copolymers from vinylpyrrolidone and vinylacetate, in particular having a weight average molecular weight of 40,000 g/mol to 70,000 g/mol, polyethylene glycol, in particular having a weight average molecular weight of 2,000 g/mol to 10,000 g/mol, as well as HPMC, in particular having a weight average molecular weight of 20,000 g/mol to 90,000 g/mol and/or a proportion of methyl groups of 10% to 35% and/or a proportion of hydroxy groups of 1% to 35%. Further, microcrystalline cellulose can be used, in particular those having a specific surface area of 0.7 m2/g to 1.4 m2/g. The determination of the specific surface area takes place by means of the gas adsorption method in accordance to Brunauer, Emmet and Teller.
Suitable non-polymeric compounds having at least one polar side group are in particular sugar alcohols and disaccharides, wherein the term sugar alcohols in this case also comprises monosaccharides. Examples of suitable sugar alcohols/disaccharides are lactose, mannitol, sorbitol, xylitol, isomalt, glucose, fructose, maltose, and mixtures of two or more of these compounds.
Alternatively, also waxes such as for example hexadecyl palmitate or carnauba wax can be used as adhesion enhancers. Also, fats such as glycerol fatty acid esters (e.g., glycerolpalmitate, glycerolbehenate, glycerollaurate, and glycerolstearate) or PEG glycerol fatty acid esters can be used.
All of the above-mentioned adhesion enhancers can be employed alone or as a mixture of two or more of the mentioned compounds.
It is advantageous if the adhesion enhancer is used in the particulate form and has a volume average particle size (D50) of less than 500 μm, preferably 5 μm to 200 μm.
The weight ratio of the active substance to the adhesion enhancer in the pharmaceutical composition according to the invention can be freely selected by the skilled person depending on the active substance used and the adhesion enhancer as well as the desired composition. Preferably, the weight ratio of ivabradine based on the free base to adhesion enhancer is in the range of 10:1 to 1:100, more preferred in the range of 1:1 to 1:75, more preferred in the range of 1:2 to 1:50, and most preferred in the range of 1:5 to 1:35.
For example, the pharmaceutical composition of the present invention can contain 1-80% by weight, more preferred 2-60% by weight, in particular 2-40% by weight, and especially 3-5% by weight ivabradine, based on the free base of the active substance and the total weight of the composition. Here and in the following, by total weight of the composition the weight of the composition without optionally present film coatings is to be understood.
Additionally, the pharmaceutical composition can contain one or more further pharmaceutically acceptable excipients, such as e.g. fillers, glidants, flow regulators, release agents, and disintegrants. (“Lexikon der Hilfsstoffe für Pharmazie, Kosmetik and angrenzende Gebiete”, edited by H. P. Fiedler, 4th Edition, and “Handbook of Pharmaceutical Excipients”, 3rd Edition, edited by Arthur H. Kibbe, American Pharmaceutical Association, Washington, USA, and Pharmaceutical Press, London).
Fillers: The pharmaceutical composition can contain one or more filler(s). In general, a filler is a substance that increases the bulk volume of the mixture and thus the size of the resulting pharmaceutical dosage form. Preferred examples of fillers are lactose and calcium hydrogenphosphate. The filler may be present in a proportion of 0 to 80% by weight, preferred between 10 and 60% by weight of the total weight of the composition.
Glidants: The function of the glidant is to ensure that the pelletizing and the ejection take place without much friction between the solids and the walls. Preferably, the glidant is an alkaline earth metal stearate, e.g. magnesium stearate, or a fatty acid, such as stearic acid. Typically, the glidant is present in an amount of 0 to 2% by weight, preferably between 0.5 and 1.5% by weight of the total weight of the pharmaceutical composition.
Disintegrants: Usually, by a disintegrant is meant a substance that is capable of breaking up the tablet into smaller pieces as soon as it is in contact with a liquid. Preferred disintegrants are croscarmellose sodium, sodium carboxymethyl starch, cross-linked polyvinylpyrrolidone (crospovidon), sodium carboxymethyl glycolate (e.g. explotab) and sodium bicarbonate, Typically, the disintegrant is present in an amount of 0 to 20% by weight, preferably between 1 and 15% by weight of the total weight of the composition.
Flow regulators: As the flow regulator there can be used e.g. colloidal silica. Preferably the flow regulator is present in an amount of 0 to 8% by weight, more preferably in an amount between 0.1 and 3% by weight of the total weight of the composition.
Release agents: The release agent can be e.g. talcum and is present in an amount between 0 and 5% by weight, preferably in an amount between 0.5 and 3% by the weight of the composition.
Normally, the pharmaceutical composition according to the invention has a uniformity of the active substance content (content uniformity) of 85% to 115%, preferably 90% to 110%, in particular 95% to 105% of the average content. That is, all dosage forms, for example tablets, have a content of active substance between 85% and 115%, preferably between 90% and 110%, in particular between 95% and 105% of the average active substance content. The “content uniformity” is determined according to Ph. Eur. 6.0, section 2.9.6.
The pharmaceutical composition of the present invention may be for example in the form of tablets, granules, or pellets. Here, the granule or the pellets for example may be present in capsules or sachets. Preferred are tablets that may have a film coating.
In a further preferred embodiment the pharmaceutical composition of the present invention is obtainable by dry granulation methods or direct compression methods in the absence of solvents.
Moreover, the present invention relates to a method for the preparation of a pharmaceutical composition as described above wherein the method comprises the steps:
In the above step a) the active substance is obtained in the mentioned average particle size. This can be done in that the active substance is either provided with the desired particle size or an active substance having a greater particle size is at first transferred to particles of a smaller particle size, for example by grinding and/or screening.
In a preferred embodiment of the method according to the invention as an additional step there is admixed an adhesion enhancer. Suitable adhesion enhancers are the above-mentioned compounds. When an adhesion enhancer is admixed, it is preferred that at least a part of the adhesion enhancer, preferably the complete adhesion enhancer, is (pre-)mixed with the active substance some time, preferably about 5 to about 30 min., more preferably about 5 to about 10 min., e.g. about 10 min., before subjecting the mixture and optionally further excipients, to further process steps, e.g. dry granulation or direct compression, preferably direct compression. It has been surprisingly found that premixing the active substance and at least part of the adhesion enhancer followed by a short time delay advantageously influences the dissolution profile of the obtained composition, in particular of tablets.
Finally, the method according to the invention in a further preferred embodiment comprises the additional step of dry granulation or direct compressing in the absence of solvents, preferably direct compression. Doing so, there may be obtained for example tablets, which if desired subsequently can be provided with a film coating.
Preferably, the pharmaceutical composition according to the invention is present as a tablet containing ivabradine in an amount preferably of 1 mg to 20 mg, more preferred 3 mg to 15 mg, in particular 5 mg to 10 mg, based on ivabradine free base. Thus, object of the invention are in particular tablets containing 5 mg or 7.5 mg ivabradine, based on ivabradine free base.
Preferably, the pharmaceutical composition according to the invention is administered twice a day.
In a preferred embodiment, the oral administration of the formulation according to the invention to a human as a patient leads to a plasma level profile which is distinguished by a cmax (maximum plasma level) based on a twice daily intake of 5 mg of the active substance ivabradine, in the steady state, of about 5 to 40 ng/ml, preferably 10 to 30 ng/ml.
The abovementioned values for the plasma level are preferably mean values, obtained by investigations of blood samples of a group of 10 test subjects (having an average body weight of 70 kg), the corresponding blood samples having been taken 0, 1, 2, 4, 6, 8, 12, 24 and 48 hours after oral administration of the composition according to the invention in the steady state. The determination of the plasma level values can preferably be carried out by suitable HPLC-MSMS methods.
Attached
XRD samples were analysed on a Bruker-AXS D8 Advance powder X-Ray diffractometer. The measurement conditions were as follows:
Now, the present invention is explained in more detail with respect to the following examples without these should be interpreted as being restrictive.
Ivabradine adipate together with Avicel PH101 was sieved through a 355 μm sieve and pre-mixed for 10 minutes in the tumbling mixer (Turbula T10B). Subsequently, all the other constituents except for magnesium stearate were added through the 355 μm sieve and stirred for further 30 minutes in the tumbling mixer. After the addition of magnesium stearate it was stirred again for 2 minutes in the tumbling mixer. The finished mixture was compressed on a rotary press (Riva Piccola) with 7 mm round biconvex punch. The tablets had a hardness of about 50-85 N.
Ivabradine adipate together with Povidon VA 64 and Prosolv SMCC 90 was sieved through a 355 μm sieve and pre-mixed for 10 min, in the tumbling mixer (Turbula T10B).
Subsequently, all the other constituents except for magnesium stearate were added through the 355 μm sieve, and stirred for further 30 min. in the tumbling mixer. After the addition of magnesium stearate it was stirred again for 2 min. in the tumbling mixer. The finished mixture was compressed on a rotary press (Riva Piccola) with 7 mm round biconvex punch. The tablets had a hardness of about 50-85 N.
Ivabradine adipate together with Povidon VA 64 and half of the Prosolv SMCC 90, magnesium stearate, Aerosil and the total amount of sodium bicarbonate were pre-mixed for 5 min. in the tumbling mixer (Turbula T10B) and compacted. Subsequently, the material was broken over a 1000 μm screen-type mill (Comil), the remaining excipients were added and the composition was mixed for 5 min. in the tumbling mixer. The finished mixture was compressed on a rotary press (Riva Piccola) with 7 mm round biconvex punch. The tablets had a hardness of about 50-85 N.
Ivabradine together with Avicel PH101 was pre-mixed for 10 min. in the tumbling mixer (Turbula T10B). Subsequently, all other constituents except for magnesium stearate were added, and stirred for further 30 min. in the tumbling mixer. After the addition of magnesium stearate it was stirred again for 2 min. in the tumbling mixer. The finished mixture was compressed on a rotary press (Riva Piccola) with 7 mm round biconvex punch. The tablets had a hardness of about 50-85 N.
Ivabradine together with Povidon VA 64 and Prosolv SMCC 90 was sieved through a 355 μm sieve and pre-mixed for 10 min. in the tumbling mixer (Turbula T10B). Subsequently, all other constituents except for magnesium stearate were added through the 355 μm sieve and stirred for further 30 min. in the tumbling mixer. After the addition of magnesium stearate it was stirred again for 2 min. in the tumbling mixer. The finished mixture was compressed on a rotary press (Riva Piccola) with 7 mm round biconvex punch. The tablets had a hardness of about 50-85 N.
The dissolution profile (conditions: 500 mL 0.1 nHCl pH 1.2, 37° C., 50 rpm baskets (USP app. l)) of the tablets of Example 5 is shown in
Ivabradine and Povidon VA 64 together with half of the Prosolv SMCC 90, magnesium stearate, Aerosil and the total amount of sodium bicarbonate were pre-mixed for 5 min. in the tumbling mixer (Turbula T10B) and compacted. Subsequently, the material was broken over a 1000 μm screen-type mill (Comil), the remaining excipients were added, followed by mixing for 5 min. in the tumbling mixer (Turbula T10B). The finished mixture was compressed on a rotary press (Riva Piccola) with 7 mm round biconvex punch. The tablets had a hardness of about 50-85 N.
The dissolution profile (conditions: 500 mL 0.1 nHCl pH 1.2, 37° C., 50 rpm baskets (USP app. I)) of the tablets of Example 6 is shown in
As can be seen in comparison to Example 5 (direct compression), the direct compression of the same amount of active agents provide an improved dissolution profile compared to the dissolution profile of tablets obtained by compacting.
The pre-mixing of the active agent with the adhesion enhancer for 10 min. prior to further processing of the mixture provides an advantageous effect on the dissolution profile.
The stability of ivabradine adipate in comparison to ivabradine hydrochloride form I was investigated at different temperatures and humidities in open or closed containers for different storage times. The results are summarized in the following table.
Ivabradine adipate according to the present invention is stable at various conditions. The ivabradine HCl form I undergoes phase transition into ivabradine HCl, form beta, or form d, in particular in open containers.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 165 881.3 | Jun 2010 | EP | regional |
| 10 165 884.7 | Jun 2010 | EP | regional |
| 1760/CHE/2010 | Jun 2010 | IN | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2011/059865 | 6/14/2011 | WO | 00 | 12/14/2012 |
