AU2002228579A1 - Novel modified released formulation - Google Patents
Novel modified released formulationInfo
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- multiparticulate
- modified release
- solid dispersion
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- release solid
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Description
NOVEL MODIFIED RELEASE FORMULATION
Field of the Invention
The present invention is directed to a multiparticulate, modified release solid dispersion formulation comprising a drug substance having a low water-solubility, to a unit dosage of the same, as well as to a process for the preparation thereof. The invention also concerns the use of a multiparticulate, modified release solid dispersion formulation for the manufacture of a medicament for the treatment of various medical conditions such as hypertension.
Background of the invention
Solubility of a drug in the gastrointestinal fluids and its permeability through the cell membrane determines its oral bioavailability (Leaner and Dressman, Eur. J. Pharm.
Biopharm 50, (2000) 47-60). For drugs with low aqueous solubility, the dissolution rate in the lumen is the rate-limiting step. Particle size reduction, solubilization, and salt formation are commonly used formulation methods to improve the dissolution rate. However, there are limitations to each of these techniques.
Many drugs do not only have low water solubility, but they might also have a narrow therapeutical index, which means that the drug levels in the blood have to be carefully controlled. This can be achieved by a controlled release formulation. These have other benefits compared to regular dosage forms; patient acceptability is usually better due to fewer doses per day, and the drug is usually more efficiently used so less active drug is needed.
Gel matrix tablets is a common drug form for modified release. The release rate is controlled either by erosion or by the diffusion of drug molecules in the swelled polymer matrix, which is the reason why drug solubility in the matrix material has great influence on the release rate. One disadvantage of matrix tablets is that they cannot always be divided, whereas multiparticulate tablets can be divided.
Solid dispersions have been studied as a possibility to control the drug release rate (Aceves et al, Int. J. Pharm. 195, (2000) 45-53). Solid dispersion is a dispersion of one or more active ingredients in an inert carrier or matrix at solid state, prepared by the melting (fusion), solvent or melting-solvent method (Chiou and Riegelman., J. Pharm. Sci. 60, (1971) 1281-1302). In J. Pharm. Sci. 58, (1969) 1505-1509, Chiou and Riegelman have classified the solid dispersions into following groups: Eutetic mixtures; solid solutions; glass solutions and glass suspensions; amorphous precipitations in crystalline carrier; and combinations of those above.
Melt processing (fusion method) was presented for the first time by Segikuchi, K. and Obi, N. in 1961, in Chem. Pharm. Bull. 9 (1961), 866-872 to prepare solid dispersions. In the melt method a physical mixture of the carrier and the drug is melted and then solidified. Cooling leads to supersaturation, but due to solidification the dispersed drug is trapped in to the carrier matrix. Melt method is often recommended, because no organic solvents are needed, so it is often less costly and better for the environment than the solvent method. However, it is not a suitable manufacturing method for thermolabile drugs. Thermal degradation, sublimation and polymorphic transformations may also occur during fusion (Goldberg et al, J. Pharm. Sci.54, (1965) 1145-1148).
The principle of solid dispersions has been used in many pharmaceutical formulations, mostly in order to increase the bioavailability but in some cases for obtaining sustained release. Solid dispersions can be prepared of Hpophilic matrix materials. The release rate is adjusted by varying the drug-excipient ratio. The amount of drug released increases with increased loading (Bodmeier et al, Drug. Dev. Ind. Pharm. 16 (9), (1990) 1505-1519).
Besides waxes and polar lipids, different polymers have been used to control drug release rate from solid dispersions. Ozeki et al. have shown that the release rate of phenacetin from a solid dispersion composed of poly(ethylene oxide)-carboxyvinylpolymer interpolymer complex can be controlled (Ozeki et al, J. Control. Release 58, (1999) 87-95).
US 6, 132, 772 (corresponding to WO 96/23499) discloses an oral, extended release solid pharmaceutical composition comprising polyethylene glycol having a molecular weight of at least 1000, a drug having a solubility of less than 0.1 % by weight in water at 20 °C and a hydrophilic gel-forming polymer having a mean molecular weight of at least 20 000.
US 5,965,163 discloses a solid dosage form comprising a plurality of particles. The drug may according to this document be soluble or water insoluble.
US 5,405,617 discloses the preparation of carrier matrices and spray congealed powders comprising an admixture of aliphatic or fatty acid esters and pharmaceutical actives which can be compressed into tablet and caplet dosage form.
US 4,629,621 discloses a sustained release preparation of bioactive material having erodible characteristics.
Stearic acid has been used as a controlled release matrix excipient in spray congealing (Rodriguez et al, Int. J. Pharm. 183, (1999) 133-143). The drug substances used by Rodriguez are theophylline having a water solubility at 25 °C of 8.3 mg/ml, and fenbufen having a water solubility at 25 °C of 0.11 mg/ml.
Outline of the invention
The object of the present invention is to provide a pharmaceutical formulation of a drug substance having low solubility in water.
More particularly, the present invention is directed to a multiparticulate, modified release solid dispersion formulation, comprising
(i) an active drug substance having a water-solubility of, or below, 8 mg/ml at room temperature;
(ii) at least one hydrophobic matrix former which is a meltable, non-swelling amphiphilic lipid having a water-solubility below 1 mg/g; and
(iii) at least one hydrophilic matrix former which is a meltable excipient having a water- solubility above 0.1 g/g;
wherein
the weight ratio hydrophobic matrix former/ hydrophilic matrix former is > 1 ; and the particle size is less than 300 μm.
The term "modified release" is herein defined as a formulation that releases less than 90% of its drug contents during the first three hours of the release.
The wording "at least one hydrophobic matrix former" as used herein, is defined such that one hydrophobic matrix former can be used alone, or in an alternative embodiment of the invention a mixture of hydrophobic matrix formers may be used.
The wording "at least one hydrophilic matrix former" as used herein, is defined such that one hydrophilic matrix former can be used alone, or in an alternative embodiment of the invention a mixture of hydrophilic matrix formers may be used.
The term "solid dispersion" is herein defined as a dispersion of the active compound in an inert carrier or matrix at solid state. Solid dispersion is more particularly defined herein as eutetic mixtures, solid solutions, glass solutions or glass suspensions, amorphous precipitations in crystalline carrier or combinations thereof.
The wording "low solubility in water" used herein, is defined as a substance which at room temperature, such as at a temperature of 23 °C, has a solubility in water of, or below, 8 mg/ml.
The wording "multiparticulate formulation" used in accordance with the present invention is defined as a formulation comprising individual units of the drug substance, the hydrophobic matrix former and the hydrophilic matrix former, filled into capsules or compressed into e.g. one single tablet which may be a rapidly disintegrating tablet.
The hydrophobic matrix formers are in accordance with the present invention water- insoluble, non-swelling fatty acids having a melting point above 50 °C, more particularly a melting point within the range of from 55-75 °C. Examples of specific fatty acids useful in accordance with the present invention are stearic acid, palmitic acid and myristic acid, or mixtures thereof.
In a further aspect of the invention the hydrophobic matrix former is a fatty acid ester such as, but not limited to, glyceryl monostearate, glyceryl behenate, glyceryl dipalmitostearate, and glyceryl di/tri stearate, or mixtures thereof.
In still a further aspect of the invention the hydrophobic matrix former is a hydrogenated fatty acid ester such as, but not limited to, hydrogenated castor oil, also known under the trade mark Cutina HR®.
In still a further aspect of the invention the hydrophobic matrix former is a mixture of mono-, di- and triglycerides and polyethyleneglycol mono- and diesters of fatty acids, such as Gelucire® 50/02.
The hydrophobic matrix former may also be selected from waxes such as carnauba wax; fatty alcohols such as, but not limited to, cetyl alcohol, stearyl alcohol or cetostearyl alcohol, or mixtures thereof.
The hydrophilic matrix formers are in accordance with the present invention meltable, water soluble excipients which are solid at room temperature, such as polyethyleneoxides; polyethylene glycols; and polyethyleneoxide and polypropyleneoxide block-co-polymers, e.g. poloxamers. Specific examples of poloxamers useful in accordance with the present
® invention are poloxamer 188, also known under the trade name Pluronic F68 , and
poloxamer 407, which is also known under the trade name Pluronic F127 . Pluronic F68
® and Pluronic F127 are commercially available from BASF. Specific examples of polyethylene glycols useful in accordance with the present invention are PEG 4000, known
® under the trade name Macrogol 4000 , and PEG 6000, known under the trade name
® Macrogol 6000 . Any poloxamer and PEG which are solid at room temperature may be used in accordance with the present invention. A comprehensive list of poloxamers and PEG's useful in accordance with the present invention can be found in Handbook of Pharmaceutical Excipients 3rd Ed., American Pharmaceutical Association and Pharmaceutical Press (2000), Washington, 665, which is hereby incorporated by reference, but which list however should not in any way be interpreted as exhaustive. Also other hydrophilic excipients which are miscible with the hydrophobic matrix formers as melts are useful in accordance with the present invention. Also other hydrophilic
excipients which are miscible with the hydrophobic matrix formers as melts are useful in accordance with the present invention.
The weight ratio of hydrophobic matrix former/ hydrophilic matrix former is > 1 , the excess amount of the hydrophobic matrix providing a modified release effect.
In one aspect of the invention, felodipine which has the chemical name 2,6-dimethyl-4- (2,3-dichlorophenyl)-l ,4-dihydropyridine-3,5-dicarboxylic acid-3-methyl ester-5-ethyl ester, is used as the active drug substance. Felodipine is an antihypertensive substance disclosed in EP 0 007 293, having a water-solubility of about 0.5 μg/ml at an ambient temperature of 22-25 °C.
A further aspect of the invention is to use bicalutamide, a non-steroidal anti-androgen which is the racemate of 4'-cyano-α',α',α'-trifluoro-3-(4-fluorophenylsulphonyl)-2- hydroxy-2-methylpropiono-m-toluidide, as the active drug substance. Bicalutamide is
TM known under the trade name CASODEX . Bicalutamide is useful in prostate cancer therapy, and EP 100172 discloses 4'-cyano-α',α',α'-trifluoro-3-(4- fluorophenylsulphonyl)-2-hydroxy-2-methylpropiono-m-toluidide (named in EP 100172 as 4-cyano-3-trifluoromethyl-N-(3-/7-fluorophenylsulphonyl-2-hydroxy-2- methylpropionyl)aniline). 4'-cyano-α',α',α'-trifluoro-3-(4-fluorophenylsulphonyl)-2- hydroxy-2-methylpropiono-m-toluidide as well as the racemate thereof, as well as where >50% of the 4'-cyano-α',α',α'-trifluoro-3-(4-fluorophenylsulphonyl)-2-hydroxy-2- mefhylpropiono-m-toluidide is provided in the form of the R-enantiomer, is also within the scope of the invention. The water-solubility for bicalutamide is about 0.0046 mg/ml at physiological pH and at an ambient temperature of 22-25 °C.
In one embodiment of the invention, the total amount of the active drug substance is below about 40% by weight. In a further aspect of the invention the total amount of the drug substance is 30-40% by weight, and in still a further embodiment of the invention the total amount of the active drug substance is 20-30% by weight.
The wording "unit dosage form" is herein defined as a composition where the amount of active drug substance is administered as one single tablet, capsule or other suitable form in accordance with the present invention.
The pharmaceutical formulation according to the present invention is useful for the treatment of various medical conditions such as cardiovascular diseases or in the treatment of cancer, e.g. prostate cancer.
Thus, one aspect of the present invention is the use of a multiparticulate, modified release formulation as claimed and described herein, for the manufacture of a medicament for the treatment of hypertension or cancer such as prostate cancer.
Another aspect of the present invention, is a method for the treatment of hypertension or cancer such as prostate cancer, whereby a multiparticulate, modified release formulation as claimed and described herein, is administered to a patient in need of such treatment.
The multiparticulate, modified release formulation according to the present invention may be formulated into a unit dosage form, preferably as a tablet or a capsule, which may also comprise standard excipients known to the skilled person in the art of formulation.
Examples of such excipients are fillers, binders, disintegrants and lubricants, but this list should however not be interpreted as being exhaustive.
The multiparticulate, modified release solid dispersion formulation according to the present invention provides the possibility of formulating drug substances having a water- solubility of, or below, 8 mg/ml at room temperature. The novel formulation is particularly useful when formulated into a tablet. The multiparticulate system makes it possible to divide the tablet without disturbing the release rate of the active drug substance.
Methods of preparation
In spray congealing, or spray chilling as it is also called, the melted mass is atomized into droplets, which solidify quickly in cool air (Killeen, Pharm. Eng., July/August 1993, 56-64). The process differs from spray drying in that in spray drying the main action is evaporation of solvent caused by warm air, whereas in spray congealing it is a phase change from liquid to solid.
The spray congealing process used in accordance with the present invention comprises the following steps:
(i) melting the hydrophobic matrix former;
(ii) dissolving or emulsifying the active compound into the melt;
(iii) dissolving the hydrophilic matrix former into the melt;
(iv) atomizing the melt into droplets; (v) solidifying the droplets; and
(vi) collecting the particles.
The produced particles can then be further formulated and into tablets or filled into capsules.
The atomization into droplets can be done with different techniques, such as with a capillary nozzle, with a pneumatic nozzle, with an ultrasonic nozzle, with a hydraulic nozzle, with electrospraying, with rotary atomization, and preferably with a pneumatic nozzle using warm air as atomization gas.
The solidification of droplets can take place in liquid nitrogen, in or on carbondioxide ice or in air with a temperature lower than the melt point of the droplets. The particles may be collected into a vessel directly, or with a cylinder connected to a cyclone. The resulted particles are smaller than 300 μm, preferably spherical, and the drug is present in the particles in the form of a solid dispersion.
Additives may be added into the melt prior to the atomization. Examples of such additives are surface active agents, excipients increasing viscosity, and buffering agents, but this list should however not in any way be interpreted as limiting the invention.
Information on the particle size distribution and on the roundness of the particles may be obtained by image analysis system (BeadCheck 300/MC, PharmaNision AB, Lund, Sweden). The particles are distributed on a glass plate with a sample preparation device. The number of particles from each batch are photographed to analyze number size distribution and roundness distribution.
Mean diameter is used for particle size distribution. The radius from the center of mass to the particle perimeter is measured in incremental steps of 3° (BeadCheck™ 830 User's Manual). The diameter of each particle is calculated from the mean value of these measurements.
Roundness is a measurement of the length-width relationship, with a value in the range [0.0, 1.0] (BeadCheck™ 830 Configuration Manual). A perfect circle has roundness 1.0 and a very narrow object has roundness close to 0.
Detailed description of the invention
The invention will now be described in more detail by way of the following examples, which however should not be construed as limiting the invention in any way.
The following multiparticulate, modified release solid dispersion formulations were prepared. For each of these Examples, the number of 5000 particles (Examples 1-7) or 10 000 particles (Examples 8-11) from each batch were photographed to analyze number size distribution and roundness distribution.
Example 1 amount Tel
(i) felodipine 1
(ii) cetanol 4
(iii) PEG 4000 2
I. Preparation of the multiparticulate, modified release formulation
Felodipine (1 g) was dissolved in a melt of 4 g cetanol at 1 10°C. The amount of 2 g PEG
4000 was added into the melt. The melted mixture was kept at 110°C and atomized with a pneumatic nozzle by using an atomization air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice
(temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 78 μm and roundness of 0.85.
Example 2 amount Tel
(i) felodipine 1
(ii) cetanol 4
(iii) poloxamer 407 2
I. Preparation of the multiparticulate, modified release formulation
Felodipine (1 g) was dissolved in a melt of 4 g cetanol at 110°C. The amount of 2 g
® poloxamer 407 (Pluronic F127 ) was added into the melt. The melted mixture was kept at
110°C and atomized with a pneumatic nozzle by using an atomization air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and-2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 77 μm and a roundness of 0.87.
Example 3 amount Tεl
(i) felodipine 1
(ii) hydrogenated castor oil 4 (iii) PEG 4000 2
I. Preparation of the multiparticulate, modified release formulation
Felodipine (1 g) was dissolved in a melt of 4 g hydrogenated castor oil (Cutina HR®) at
1 10°C. The amount of 2 g PEG 4000 was added into the melt. The melted mixture was kept at 110°C and atomized with a pneumatic nozzle by using an atomization air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 73 μm and a roundness of 0.90.
Example 4 amount Tgl (i) felodipine 1
(ii) hydrogenated castor oil 4
(iii) poloxamer 407 2
I. Preparation of the multiparticulate, modified release formulation Felodipine (1 g) was dissolved in a melt of 4 g hydrogenated castor oil (Cutina HR®) at
® 1 10°C. The amount of 2 g poloxamer 407 (Pluronic F127 ) was added into the melt. The melted mixture was kept at 110°C and atomized with a pneumatic nozzle by using an atomization air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 69 μm and a roundness of 0.92.
Example 5 amount fgl
(i) felodipine 1
(ii) glyceryl palmitostearate 4
(iii) poloxamer 407 2
I. Preparation of the multiparticulate, modified release formulation
Felodipine (1 g) was dissolved in a melt of 4 g glyceryl palmitostearate (Precirol® ATO 5)
® at 110°C. The amount of 2 g poloxamer 407 (Pluronic FI 27 ) was added into the melt.
The melted mixture was kept at 110°C and atomized with a pneumatic nozzle by using an atomization air temperature of 400°C and a pressure of 7 bar. The particles were collected
into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 72 μm and a roundness of 0.94.
Example 6 amount ϊμ]
(i) felodipine 1
(ii) Stearic acid 4 (iii) PEG 4000 2
I. Preparation of the multiparticulate, modified release formulation
Felodipine (1 g) was dissolved in a melt of 4 g stearic acid at 110°C. The amount of 2 g
PEG 4000 was added into the melt. The melted mixture was kept at 110°C and atomized with a pneumatic nozzle by using an atomization air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 77 μm and roundness of 0.93.
Example 7 amount \z\ (i) felodipine 1
(ii) Stearic acid 4 (iii) poloxamer 407 2
I. Preparation of the multiparticulate, modified release formulation
Felodipine (1 g) was dissolved in a melt of 4 g stearic acid at 110°C. The amount of 2 g
® poloxamer 407 (Pluronic F127 ) was added into the melt. The melted mixture was kept at 1 10°C and atomized with a pneumatic nozzle by using an atomization air temperature of
400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 70 μm and a roundness of 0.94.
Example 8 amount [gl
(i) felodipine 2 (ii) stearic acid 6
(iii) poloxamer 407 6
Felodipine (2 g) was dissolved in a melt of 6 g stearic acid at 110°C. The amount of 6 g poloxamer 407 (Pluronic F127®) was added into the melt. The melted mixture was kept at 110°C and atomised with a pneumatic nozzle by using an atomisation air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 56 μm and roundness of 0.96.
Example 9 amountrgl
(i) felodipine 2 (ii) glyceryl ditristearate 8
(iii) poloxamer 407 4
Felodipine (2 g) was dissolved in a melt of 8 g glyceryl ditristearate (Precirol WL2155®) at 1 10°C.The amount of 4 g poloxamer 407 (Pluronic F127®) was added into the melt. The melted mixture was kept at 110°C and atomised with a pneumatic nozzle by using an
atomisation air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 49 μm and roundness of 0.93.
Example 10 amountrgl
(i) felodipine 2 (ii) glyceryl behenate 8
(iii) poloxamer 407 4
Felodipine (2 g) was dissolved in a melt of 8 g glyceryl behenate (Compritol 888®) at 1 10°C.The amount of 4 g poloxamer 407 (Pluronic F127®) was added into the melt. The melted mixture was kept at 1 10°C and atomised with a pneumatic nozzle by using an atomisation air temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 51 μm and roundness of 0.97.
Example 11 amountfgl
(i) felodipine 2 (ii) glyceryl monostearate 8
(iii) poloxamer 407 4
Felodipine (2 g) was dissolved in a melt of 8 g glyceryl monostearate at 110°C.The amount of 4 g poloxamer 407 (Pluronic F127®) was added into the melt. The melted mixture was kept at 1 10°C and atomised with a pneumatic nozzle by using an atomisation air
temperature of 400°C and a pressure of 7 bar. The particles were collected into a vessel which was kept on carbondioxide ice (temperature -50°C), and thereafter dried over night in a vacuum oven at 25°C and 2 mbar.
The resulted particles had a 90% fractile size (90% smaller than) of 50 μm and roundness of 0.99.
II. Tabletting Particles from step I of each of the examples 1-11 above, were compressed into tablets, which had a theoretical felodipine content of 10 mg. The target tablet weight was 200 mg. Tablet mass consisted of 35% particles and 65% microcrystalline cellulose. The mixture of microparticles, microcrystalline cellulose and sodium stearyl fumarate (0.14% of the total mixture weight) was mixed in a Turbula mixer of the type 72C, Willy A. Bachofen AG Maschinenfabrik, Basle, Switzerland, for 10 minutes. This mixture was compressed with an excentric tablet press Kilian SP300 (Examples 1-7) or Kilian EK0 (Examples 8-11) using 10.0 mm flat punches with maximum compression forces of 5.0-5.6 kN (Examples 1-7) or 2.7-7.0 kN (Examples 8-11).
The breaking force of resulting tablets was within the range 43-93 N.
III. Dissolution tests of tablets
The rate of release was tested from all tablet samples from examples using USP II paddle method. Dissolution test from each batch was run three times. Release testing was performed in a dissolution medium of 500 ml of sodium dihydrogen phosphate buffer at pH 6.5. 0.4 % cetyl trimethylammonium bromide was added to the buffer to increase the solubility of felodipine. The measurements were carried out at 37°C and the paddle was rotated 100 rpm. Each tablet was placed in a basket located about 1 cm above the paddle. Aliquots (10 ml) were withdrawn after 0.5, 1 , 2, 4, and 7 hours and filtered through 1.2 μm filter (Millipore® MF-Millipore). The first 5 ml of the filtrate was discarded.
The filtrated sample solutions were then analyzed with UV-spectrophotometer at wavelength 362 nm and 450 nm.
The results of the dissolution for each Example above, are summarized in Table 1 below.
Table 1
Claims (28)
1. A multiparticulate, modified release solid dispersion formulation, comprising
(i) an active drug substance having a water-solubility of, or below, 8 mg/ml at room temperature;
(ii) at least one hydrophobic matrix former which is a meltable, non-swelling amphiphilic lipid having a water-solubility below 1 mg/g; and
(iii) at least one hydrophilic matrix former which is a meltable excipient having a water- solubility above 0.1 g/g;
wherein
the weight ratio hydrophobic matrix former/ hydrophilic matrix former is > 1 ; and the particle size is less than 300 μm.
2. A multiparticulate, modified release solid dispersion formulation according to claim 1, wherein the hydrophobic matrix former or mixture thereof, is a water-insoluble, non-swelling fatty acid having a melting point above 50 °C.
3. A multiparticulate, modified release solid dispersion formulation according to claim 2, wherein the hydrophobic matrix former or mixture thereof, is a water-insoluble, non- swelling fatty acid having a melting point of from 55-75 °C.
4. A multiparticulate, modified release solid dispersion formulation according to any one of the preceding claims, wherein the hydrophobic matrix former or mixture thereof, is selected from any one of stearic acid, palmitic acid and myristic acid.
5. A multiparticulate, modified release solid dispersion formulation according to claim 1, wherein the hydrophobic matrix former is a fatty acid ester.
6. A multiparticulate, modified release solid dispersion formulation according to claim 5, wherein the hydrophobic matrix former or mixture thereof, is selected from any one of glyceryl monostearate, glyceryl behenate, glyceryl dipalmitostearate, and glyceryl di/tristearate.
7. A multiparticulate, modified release solid dispersion formulation according to claim 1, wherein the hydrophobic matrix former is a hydrogenated fatty acid ester.
8. A multiparticulate, modified release solid dispersion formulation according to claim 7, wherein the hydrophobic matrix former is hydrogenated castor oil.
9. A multiparticulate, modified release solid dispersion formulation according to claim 1, wherein the hydrophobic matrix former is a mixture of mono-, di- and triglycerides and polyethyleneglycol esters of fatty acids.
10. A multiparticulate, modified release solid dispersion formulation according to claim 1, wherein the hydrophobic matrix former is selected from waxes, fatty alcohols or mixtures thereof.
11. A multiparticulate, modified release solid dispersion formulation according to claim 10, wherein the hydrophobic matrix former is carnauba wax.
12. A multiparticulate, modified release solid dispersion formulation according to claim 10, wherein the hydrophobic matrix former is selected from any one of cetyl alcohol, stearyl alcohol and cetostearyl alcohol, or mixtures thereof.
5 13. A multiparticulate, modified release solid dispersion formulation according to any one of claims 1-12, wherein the hydrophilic matrix former is selected from any one of polyethyleneoxides, polyethyleneglycols, polyethyleneoxide and polypropyleneoxide block-co-polymers, or mixtures thereof.
o 14. A multiparticulate, modified release solid dispersion formulation according to claim 13, wherein the hydrophilic matrix former is a poloxamer.
15. A multiparticulate, modified release solid dispersion formulation according to claim 14, wherein the poloxamer is poloxamer 407. 5
16. A multiparticulate, modified release solid dispersion formulation according to claim 13, wherein the hydrophilic matrix former is a polyethylene glycol.
17. A multiparticulate, modified release solid dispersion formulation according to o claim 16, wherein the hydrophilic matrix former is PEG 4000 or PEG 6000.
18. A multiparticulate, modified release solid dispersion formulation according to any one of the previous claims, wherein the active drug substance is felodipine or bicalutamide.
5 19. A multiparticulate, modified release solid dispersion formulation according to any one of the previous claims, wherein the total amount of the drug substance is below about 40 % by weight.
20. A unit dosage form comprising a multiparticulate, modified release solid dispersion o formulation according to any one of claims 1-19.
21. A tablet comprising a multiparticulate, modified release solid dispersion formulation according to any one of claims 1-19, further comprising one or more pharmaceutically acceptable excipients.
22. A tablet according to claim 21 , wherein the pharmaceutically acceptable excipients are microcrystalline cellulose and sodium stearyl fumarate.
23. A process for the preparation of a multiparticulate, modified release formulation according to any one of claims 1-19, whereby said formulation is prepared by spray congealing.
24. A process according to claim 23, whereby the spray congealing comprises the following steps:
(i) melting the hydrophobic matrix former; (ii) dissolving or emulsifying the active compound into the melt; (iii) dissolving the hydrophilic matrix former into the melt; (iv) atomizing the melt into droplets; (v) solidifying the droplets; and (vi) collecting the particles.
25. Use of a multiparticulate, modified release solid dispersion formulation according to any one of claims 1-19, for the manufacture of a medicament for the treatment of a cardiovascular disease.
26. A method for the treatment of a cardiovascular disease, whereby a multiparticulate, modified release solid dispersion formulation according to any one of claims 1-19, is administered to a patient in need of such treatment.
27. Use of a multiparticulate, modified release solid dispersion formulation according to any one of claims 1-19, for the manufacture of a medicament for use in cancer therapy.
28. A method for the treatment of cancer, whereby a multiparticulate, modified release solid dispersion formulation according to any one of claims 1-19, is administered to a patient in need of such treatment.
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE0100477A SE0100477D0 (en) | 2001-02-13 | 2001-02-13 | Novel formulation |
| SE0100478-7 | 2001-02-13 | ||
| SE0100478A SE0100478D0 (en) | 2001-02-13 | 2001-02-13 | Novel formulation |
| SE0100477-9 | 2001-02-13 | ||
| PCT/SE2002/000228 WO2002064121A1 (en) | 2001-02-13 | 2002-02-08 | Novel modified released formulation |
Publications (2)
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| AU2002228579A1 true AU2002228579A1 (en) | 2003-02-20 |
| AU2002228579B2 AU2002228579B2 (en) | 2006-07-27 |
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Country Status (19)
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| EP (2) | EP1368006B1 (en) |
| JP (2) | JP2004518709A (en) |
| KR (1) | KR20040058103A (en) |
| CN (2) | CN1491104A (en) |
| AT (1) | ATE324871T1 (en) |
| AU (1) | AU2002228579B2 (en) |
| BR (1) | BR0206825A (en) |
| CA (2) | CA2434542A1 (en) |
| DE (1) | DE60211130T2 (en) |
| DK (1) | DK1368006T3 (en) |
| ES (1) | ES2261643T3 (en) |
| HK (1) | HK1059740A1 (en) |
| IL (1) | IL157075A0 (en) |
| MX (1) | MXPA03007092A (en) |
| NO (1) | NO20033564L (en) |
| NZ (2) | NZ526993A (en) |
| PT (1) | PT1368006E (en) |
| WO (2) | WO2002064118A1 (en) |
Families Citing this family (26)
| Publication number | Priority date | Publication date | Assignee | Title |
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| DE10026698A1 (en) | 2000-05-30 | 2001-12-06 | Basf Ag | Self-emulsifying active ingredient formulation and use of this formulation |
| AU2003220472A1 (en) * | 2002-09-28 | 2004-04-19 | Mcneil-Ppc, Inc. | Modified release dosage form with two cores |
| SE0301904D0 (en) | 2003-06-26 | 2003-06-26 | Astrazeneca Ab | Novel imidazopyridine compound II with therapeutic effect |
| US8025899B2 (en) | 2003-08-28 | 2011-09-27 | Abbott Laboratories | Solid pharmaceutical dosage form |
| US8377952B2 (en) | 2003-08-28 | 2013-02-19 | Abbott Laboratories | Solid pharmaceutical dosage formulation |
| AU2004268641A1 (en) * | 2003-08-29 | 2005-03-10 | Dynogen Pharmaceuticals, Inc. | Compositions useful for treating gastrointestinal motility disorders |
| BRPI0417348A (en) * | 2003-12-04 | 2007-03-13 | Pfizer Prod Inc | spray gelatinization process using an extruder for preparing multiparticulate crystalline drug compositions preferably containing a poloxamer and a glyceride |
| WO2005053652A1 (en) * | 2003-12-04 | 2005-06-16 | Pfizer Products Inc. | Multiparticulate crystalline drug compositions containing a poloxamer and a glyceride |
| JP2007513143A (en) * | 2003-12-04 | 2007-05-24 | ファイザー・プロダクツ・インク | Spray coagulation process for producing multiparticulate azithromycin compositions preferably using poloxamer and glycerides using an extruder |
| WO2005053639A2 (en) * | 2003-12-04 | 2005-06-16 | Pfizer Products Inc. | Controlled release multiparticulates formed with dissolution enhancers |
| SE0303451D0 (en) * | 2003-12-18 | 2003-12-18 | Astrazeneca Ab | New compounds |
| MY191349A (en) * | 2004-08-27 | 2022-06-17 | Bayer Pharmaceuticals Corp | New pharmaceutical compositions for the treatment of hyper-proliferative disorders |
| RS53624B1 (en) * | 2006-03-16 | 2015-04-30 | Euro-Celtique S.A. | Pharmaceutical spheroids |
| EP2259844A4 (en) * | 2008-03-05 | 2012-02-01 | Vicus Therapeutics Llc | Compositions and methods for mucositis and oncology therapies |
| WO2011000126A1 (en) * | 2009-06-29 | 2011-01-06 | Liu Yu | Pharmaceutical composition of liposoluble drugs, preparation method and use thereof |
| DK2921486T3 (en) | 2009-08-07 | 2017-11-13 | American Life Science Pharmaceuticals Inc | Compositions and Methods for Treating Beta-Amyloid-Related Diseases |
| US20130165880A1 (en) | 2010-09-17 | 2013-06-27 | David T. Amos | Antimicrobial disposable absorbent articles |
| WO2012070030A1 (en) * | 2010-11-26 | 2012-05-31 | University Of The Witwatersrand, Johannesburg | A pharmaceutical composition |
| US20130149383A1 (en) * | 2011-12-12 | 2013-06-13 | Cory Berkland | Sustained release particle formulations of guaifenesin |
| EP4035683A1 (en) * | 2011-12-12 | 2022-08-03 | Adare Pharmaceuticals USA, Inc. | Sustained release particle formulations |
| EP3319595A4 (en) * | 2015-06-30 | 2019-04-03 | Kemin Industries, Inc. | Encapsulated active ingredients for controlled enteric release |
| US9889120B2 (en) | 2016-01-14 | 2018-02-13 | Vicus Therapeutics, Llc | Combination drug therapies for cancer and methods of making and using them |
| DE102017108054A1 (en) | 2017-04-13 | 2018-10-18 | Natura Werk Gebr. Hiller GmbH & Co. KG | Edible composition for digestion promotion |
| EP4076527A4 (en) | 2020-01-10 | 2024-05-15 | Consynance Therapeutics, Inc. | Therapeutic combinations of drugs and methods of using them |
| JP2024526956A (en) | 2021-07-22 | 2024-07-19 | ザ リージェンツ オブ ザ ユニバーシティ オブ カリフォルニア | Compositions and methods for using purified human RNA editing enzymes |
| WO2023184282A1 (en) * | 2022-03-30 | 2023-10-05 | Guizhou Sinorda Biomedicine Co., Ltd | X842 formulation |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL248553A (en) * | 1959-02-18 | |||
| HU198844B (en) * | 1984-06-14 | 1989-12-28 | Sandoz Ag | Process for producing new galenic pharmaceutical composition ensuring retarded release of active ingredient |
| US4629621A (en) * | 1984-07-23 | 1986-12-16 | Zetachron, Inc. | Erodible matrix for sustained release bioactive composition |
| US5015479A (en) * | 1987-02-02 | 1991-05-14 | Seamus Mulligan | Sustained release capsule or tablet formulation comprising a pharmaceutically acceptable dihydropyridine |
| US4956182A (en) * | 1989-03-16 | 1990-09-11 | Bristol-Myers Company | Direct compression cholestyramine tablet and solvent-free coating therefor |
| US5405617A (en) * | 1991-11-07 | 1995-04-11 | Mcneil-Ppc, Inc. | Aliphatic or fatty acid esters as a solventless carrier for pharmaceuticals |
| US5281420A (en) * | 1992-05-19 | 1994-01-25 | The Procter & Gamble Company | Solid dispersion compositions of tebufelone |
| US5433951A (en) * | 1993-10-13 | 1995-07-18 | Bristol-Myers Squibb Company | Sustained release formulation containing captopril and method |
| KR100354702B1 (en) * | 1993-11-23 | 2002-12-28 | 유로-셀티크 소시에떼 아노뉨 | Manufacturing method and sustained release composition of pharmaceutical composition |
| NZ270439A (en) * | 1995-02-02 | 1996-04-26 | Bernard Charles Sherman | Solid slow release pharmaceutical composition: carrier is polyethylene glycol and hydrophilic gel-forming polymer |
| US5851555A (en) * | 1997-08-15 | 1998-12-22 | Fuisz Technologies Ltd. | Controlled release dosage forms containing water soluble drugs |
| SE9801526D0 (en) * | 1998-04-29 | 1998-04-29 | Astra Ab | New compounds |
| US8293277B2 (en) * | 1998-10-01 | 2012-10-23 | Alkermes Pharma Ireland Limited | Controlled-release nanoparticulate compositions |
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2002
- 2002-02-08 JP JP2002563916A patent/JP2004518709A/en active Pending
- 2002-02-08 CA CA002434542A patent/CA2434542A1/en not_active Abandoned
- 2002-02-08 EP EP02710645A patent/EP1368006B1/en not_active Expired - Lifetime
- 2002-02-08 US US10/467,900 patent/US20040067256A1/en not_active Abandoned
- 2002-02-08 BR BR0206825-7A patent/BR0206825A/en not_active IP Right Cessation
- 2002-02-08 EP EP02711597A patent/EP1361868A1/en not_active Withdrawn
- 2002-02-08 WO PCT/SE2002/000227 patent/WO2002064118A1/en not_active Application Discontinuation
- 2002-02-08 CN CNA028049144A patent/CN1491104A/en active Pending
- 2002-02-08 JP JP2002563914A patent/JP2004518708A/en active Pending
- 2002-02-08 NZ NZ526993A patent/NZ526993A/en unknown
- 2002-02-08 MX MXPA03007092A patent/MXPA03007092A/en active IP Right Grant
- 2002-02-08 DK DK02710645T patent/DK1368006T3/en active
- 2002-02-08 PT PT02710645T patent/PT1368006E/en unknown
- 2002-02-08 ES ES02710645T patent/ES2261643T3/en not_active Expired - Lifetime
- 2002-02-08 KR KR10-2003-7010577A patent/KR20040058103A/en active IP Right Grant
- 2002-02-08 WO PCT/SE2002/000228 patent/WO2002064121A1/en active IP Right Grant
- 2002-02-08 AT AT02710645T patent/ATE324871T1/en not_active IP Right Cessation
- 2002-02-08 CN CNA028049063A patent/CN1491105A/en active Pending
- 2002-02-08 IL IL15707502A patent/IL157075A0/en unknown
- 2002-02-08 NZ NZ526994A patent/NZ526994A/en unknown
- 2002-02-08 US US10/467,723 patent/US20040067252A1/en not_active Abandoned
- 2002-02-08 AU AU2002228579A patent/AU2002228579B2/en not_active Ceased
- 2002-02-08 CA CA002434835A patent/CA2434835A1/en not_active Abandoned
- 2002-02-08 DE DE60211130T patent/DE60211130T2/en not_active Expired - Fee Related
-
2003
- 2003-08-12 NO NO20033564A patent/NO20033564L/en not_active Application Discontinuation
-
2004
- 2004-04-15 HK HK04102657A patent/HK1059740A1/en not_active IP Right Cessation
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2007
- 2007-05-14 US US11/748,366 patent/US20080118560A1/en not_active Abandoned
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