Patent Application
20140148507
The present invention relates to pharmaceutical compositions intended for use in solid galenic form for oral administration, comprising primarily dronedarone or at least one derivative thereof, and also to solid galenic forms as such that are manufactured from said compositions, preferably tablets. The present invention likewise concerns a process for preparing such solid galenic forms on the basis of said pharmaceutical compositions by a hot melt route, and also pertains to the therapeutic application of such compositions or of such solid galenic forms.
Dronedarone, or 2-n-butyl-3-[4-(3-di-n-butylaminopropoxy)benzoyl]-5-methylsulfonamidobenzofuran, is represented by the formula (I) below:
Dronedarone and a method for preparing it are described in patents EP 0 471 609 B1 and U.S. Pat. No. 5,223,510.
Dronedarone blocks potassium, sodium, and calcium channels and also possesses antiadrenergic properties.
Dronedarone is an antiarrhythmic which is effective in maintaining sinus rhythm in patients exhibiting atrial fibrillation or an atrial flutter.
Dronedarone may be administered by means of dosage units containing an effective amount of said active principle, as for example 400 mg of dronedarone for an adult.
For its use as a medicament, dronedarone or a derivative thereof is advantageously formulated in solid galenic forms which are administered orally, such as tablets, for example.
However, certain physical properties of dronedarone present a real challenge in terms of development of formulations suited to the preparation of such solid galenic forms, combining both an effective amount of active principle and a size of said galenic form that is small enough to be easily swallowable.
Specifically, reducing the size of the tablets while maintaining the same amount of active principle involves reducing the amount of the excipients, which poses a number of problems in terms of wettability, disintegration or even total and immediate release of the dronedarone from said tablet.
At the present time, the granulation of dronedarone in the context of the manufacture of a solid galenic form is performed by a wet route. Document EP 1 007 030 B1 describes such a process. The addition of the excipients required for the tableting of this grain and for the assimilation of dronedarone after absorption from a tablet result in a final mass of 650 mg for one unit.
The characteristics of dronedarone form part of the factors which limit the possibilities for increasing its concentration within solid galenic forms. The dronedarone tablet on the market comprises a maximum 65.54% by weight of dronedarone, in the form of dronedarone hydrochloride, relative to the total weight of said tablet.
On the other hand, wet granulation gives rise to unsatisfactory levels of dust emission during the manufacture of the solid galenic forms, following a drying phase which is vital in such a process.
The applicant has discovered, surprisingly, a pharmaceutical composition and a solid galenic form, administrable orally, having a high content of dronedarone and/or of at least one derivative thereof. This capacity to increase the content of dronedarone and/or at least one derivative thereof within solid galenic forms makes it possible to decrease the size of said forms, advantageously tablets, relative to the galenic form currently on the market. The applicant has also discovered a process for hot-melt manufacture of solid galenic forms from such a composition, having the advantage of allowing an increase in the concentration of active principle, advantageously a combined concentration of greater than 80% by weight.
This process via hot-melt granulation has, furthermore, the advantage of overcoming the problems normally encountered in the context of a process via wet granulation. The reason is that this process provides a significantly reduced water content in the galenic form, relative to the use of a conventional process, and the drying step is avoided. The omission of this drying step allows the process to be simplified and made less energy-consuming. The results are a time saving and a cost reduction.
Furthermore, it allows the production of grains based on a composition rich in dronedarone and/or in at least one derivative thereof, these grains being tabletable directly after their production, thereby allowing the implementation of a continuous industrial manufacturing process for dosage units, allowing both a time saving and a cost saving in the industrial production of solid galenic forms, more particularly tablets.
The reduction in the size of the galenic form has a number of advantages:
Dronedarone and the meltable excipient make up the internal phase of the formulation (components used to form the grain). The additional excipients optionally used constitute the external phase of the formulation.
According to another aspect, the invention is likewise directed to a solid galenic form, administrable orally, formed from a pharmaceutical composition according to the invention.
The invention further concerns a process for manufacturing solid galenic forms, comprising at least the following steps, in the indicated order:
According to one embodiment, the process for manufacturing solid galenic forms comprises the following steps, in the indicated order:
According to one embodiment, the process is characterized in that it further comprises, following step B, the following steps in the indicated order:
The process is characterized in that the solid galenic forms are tablets and/or in that it is a continuous process.
Lastly, the invention relates to a solid galenic form featuring a composition according to the invention, administrable orally and obtainable at the outcome of the process according to the invention, (i) the process advantageously being a continuous process.
The pharmaceutical compositions or the solid galenic forms according to the invention comprise dronedarone or at least one derivative thereof.
In the context of the present invention, the following definitions apply:
Dronedarone Derivatives:
Dronedarone compounds which may also exist in the form of bases or of addition salts with acids. Such addition salts form part of the invention. These salts may be prepared with pharmaceutically acceptable acids, although the salts of other acids useful, for example, for purifying or isolating dronedarone compounds also form part of the invention. The dronedarone derivatives are advantageously addition salts with acids as defined above. More particularly, the derivatives are addition salts with pharmaceutically acceptable acids.
According to one embodiment, the dronedarone derivative is dronedarone hydrochloride.
Excipient: an inactive or inert substance which facilitates the preparation and administration of a medicament;
Disintegrant: an excipient which allows satisfactory breakdown of the galenic form and hence the disintegration of the active principle in the stomach, by increasing the friability and reducing the hardness of the galenic form;
Lubricant: an excipient for facilitating the steps of manufacture of galenic forms, by virtue of its slip-increasing role, i.e., its role in increasing the fluidity of the particles in the pipes of the machines.
Hot-melt excipient: an excipient which softens or becomes fluid under the effect of heat. Such excipients have either a melting temperature: a temperature at which the solid crystal state and the liquid state of the excipient coexist (measured under standard atmospheric pressure of 1 atmosphere), or a glass transition temperature: a temperature below which the molecules forming the excipient have low relative mobility, or the temperature at which the excipient passes from the amorphous solid state into a viscous fluid state.
A pharmaceutical composition or a solid galenic form according to the invention may comprise up to 92% by weight of dronedarone and/or of at least one derivative thereof, advantageously between about 81% and 92% by weight, more advantageously between about 81% and 86% by weight, relative to the total weight of said composition or of said galenic form.
A pharmaceutical composition or a galenic form according to the invention further comprises at least one pharmaceutically acceptable excipient which is hot-meltable at a temperature of greater than or equal to about 35° C., advantageously greater than or equal to about 50° C. and less than or equal to about 120° C., advantageously less than or equal to about 100° C.
The melting temperatures (abbreviated to Tf) or the glass transition temperatures (abbreviated to Tg), where appropriate, that are indicated below are given by way of indication, and are not limitative. Most of them are taken from the “Handbook of Pharmaceutical Excipients”, fifth edition, Pharmaceutical Press.
Hot melt excipients suitable for the invention include citric acid monohydrate (Tf±100° C.), stearic acid (Tf±54-67° C.), palmitic acid (Tf±63-64° C.), lauric acid (Tf±43° C.), myristic acid (Tf±48-55° C.), hydrogenated castor oil (Tf±83-88° C.), hydrogenated plant oil (Tf±57-70° C.), stearyl alcohol (Tf±57-70° C.), cetostearyl alcohol (Tf±49-56° C.), cetyl alcohol (Tf±47-53° C.), vanillin (Tf±76-78° C.), amorphous chlorocresol (Tf±64-67° C.), cetylpyridinium hydrochloride (Tf±80-84° C.), sorbitan monostearate (Tf±43-48° C.), sorbitan monopalmitate (Tf±53-57° C.), xylitol (Tf±92-96° C.), dextrose (Tf±83° C.), ethyl maltol (Tf±89-93° C.), butylated hydroxyanisole (Tf±47° C.), benzalkonium hydrochloride (Tf±40° C.), ascorbyl palmitate (Tf±107-117° C.), erythritol (Tf±119-122° C.), sorbitol (Tf±93-112° C.), shellac (Tf±115-120° C.), maltose (Tf±120-121° C.), sucralose (Tf±130° C.), anhydrous raffinose (Tf±80 118° C.), phenylmercuric borate (Tf±112-113° C.), zinc stearate (Tf±120-122° C.), polyethylene glycol 3000, abbreviated to PEG3000 (Tf±48-54° C.), PEG4000 (Tf±50-58° C.), PEG6000 (Tf±55-63° C.), PEG8000 (Tf±60-63° C.) and PEG20000 (Tf±60-63° C.), polyethylene oxides (Tf±65-70° C.), polyoxyethylene polyoxypropylene copolymers, glyceryl monostearate (Tf±55° C.), glyceryl palmitostearate (Tf±52-55° C.), glyceryl behenate (Tf±65-77° C.), such as, for example, Compritol®888 ATO, ethyl maltol (Tf±89-93° C.), waxes such as, for example, carnauba wax (Tf±80-88° C.), microcrystalline wax (Tf±54-102° C.), white wax or yellow wax (Tf±61-65° C.), beeswax (Tf±61-65° C.), sodium acetate trihydrate (Tf±58° C.), polymethacrylates, in particular Eudragit® E (Tg±48° C.), polyvinyl acetate phthalate (Tg±42.5° C.), carbomers (Tg±100-105° C.), polycarbophils (Tg±100-105° C.), hypromellose acetate succinate (Tg±105° C.), copovidone (Tg±106° C.), and mixtures thereof.
This hot-melt excipient may be advantageously selected from binders, plasticizers, and mixtures thereof. It is advantageously selected from polyoxyethylene polyoxypropylene copolymers, polyethylene glycols abbreviated to PEG, PEG3000 (Tf±48-54° C.), PEG4000 (Tf±50-58° C.), PEG6000 (Tf±55-63° C.), PEG8000 (Tf±60-63° C.) and PEG20000 (Tf±60-63° C.), polyethylene oxides (Tf±65-70° C.), glyceryl monostearate (Tf55° C.), glyceryl palmitostearate (Tf±52-55° C.), glyceryl behenate (Tf±65-77° C.) such as, for example, Compritol®888 ATO, ethyl maltol (Tf±89-93° C.), waxes such as, for example, carnauba wax (Tf±80-88° C.), microcrystalline wax (Tf±54 102° C.), white wax or yellow wax (Tf±61-65° C.), beeswax (Tf±61-65° C.), sodium acetate trihydrate (Tf±58° C.), and mixtures thereof.
With particular advantage the hot-melt excipient or excipients are selected from polyoxyethylene polyoxypropylene copolymers, more advantageously from polyoxyethylene polyoxypropylene copolymers which are hot-meltable at a temperature of between about 50° C. and about 70° C.
Examples include, for example, poloxamer 188 (Tf±52-57° C.), poloxamer 237 (Tf±49° C.), poloxamer 338 (Tf±57° C.), poloxamer 407 (Tf±52-57° C.).
According to one embodiment, the hot-melt excipient is poloxamer 407.
Advantageously, a hot-melt excipient will be selected that has a melting temperature or a glass transition temperature of between about 50° C. and about 120° C., advantageously between about 50° C. and about 100° C. for the manufacture of tablets.
The amount of hot-melt excipient may be from about 7% to 20% by weight, advantageously between about 7% and 10% by weight, relative to the total weight of said composition or of said galenic form.
According to one embodiment, said amount of hot-melt excipient may also be expressed relative to the total weight of dronedarone base equivalent. It will then be between 1% and 20%, particularly between 5% and 15% and even more particularly 10% by weight relative to the total weight of dronedarone base equivalent.
Accordingly, said amount of hot-melt excipient may be defined both relative to the total weight of the composition and relative to the total weight of the dronedarone base equivalent present in the composition.
Base equivalent means the amount corresponding to the amount of dronedarone in base form, in other words unsalified form.
Apart from dronedarone and/or at least one derivative thereof, at least one pharmaceutically acceptable hot-melt excipient, the compositions or the galenic forms according to the invention may include a disintegrant.
This disintegrant may be selected from crosslinked polyvinylpyrrolidone, crosslinked carboxymethylcellulose, alginic acid, sodium alginate, sodium carboxymethylcellulose, microcrystalline cellulose, cellulose powder, sodium croscarmellose, crospovidone, pregelatinized starch, sodium starch glycolate, sodium carboxymethylstarch, starch, and mixtures thereof. The disintegrant advantageously is crospovidone, sodium croscarmellose, or mixtures thereof.
The amount of disintegrant may be between 0% and 10% by weight, advantageously between 3% and 10% by weight, more advantageously between 5% and 10% by weight, relative to the total weight of said composition or said galenic form.
The compositions or the galenic forms according to the invention may further comprise at least one additional excipient other than said hot-melt excipient, which may advantageously have a melting temperature of greater than about 100° C. The additional excipient or excipients is or are selected from customary excipients known to the skilled person, according to the pharmaceutical form and the desired mode of administration. This or these additional excipient or excipients may be selected, for example, from flow agents, lubricants, and disintegrants.
A pharmaceutical composition or a galenic form according to the invention may further comprise at least one lubricant.
This lubricant may advantageously be selected from magnesium stearate, stearic acid, glycerol tribehenate, sodium stearylfumarate, calcium stearate, glyceryl monostearate, glyceryl palmitostearate, sodium lauryl sulfate, zinc stearate, stearic acid, hydrogenated plant oils, polyethylene glycol, sodium benzoate, talc, and mixtures thereof. Advantageously the lubricant is magnesium stearate.
The amount of lubricant may be between 0% and 1% by weight, more preferably between 0% and 0.5% by weight, relative to the total weight of lubricant in said composition or said galenic form.
A pharmaceutical composition or a galenic form according to the invention may further comprise at least one flow agent. The flow agent advantageously is silicone dioxide.
The amount of flow agent may be between 0% and 1% by weight, advantageously between 0% and 0.4% by weight, relative to the total weight of said composition or said galenic form.
According to one embodiment, the composition or the galenic form according to the invention comprises between 81% and 92% by weight of dronedarone hydrochloride, between 7% and 10% by weight of hot-melt excipient, between 5% and 10% by weight of disintegrant, between 0% and 0.5% by weight of lubricant and between 0% and 0.4% by weight of flow agent, relative to the total weight of said composition or of said galenic form.
The pharmaceutical compositions of the present invention are generally formulated in dosage units for daily administration, one or more times a day. In the context of the invention, a dosage unit is a solid galenic form administrable orally, advantageously a tablet.
Accordingly, the dosage unit or solid galenic form, for an adult, may have a mass of 466 mg to 523 mg, and contains 400 mg of dronedarone base equivalent.
They may be plain or coated with various polymers or other appropriate substances.
Starting from the compositions described above, solid galenic forms according to the invention are obtainable by means of the following process.
The process, according to the invention, for manufacturing solid galenic forms, advantageously tablets, takes place continuously.
The process comprises the following steps:
Said steps A and B may take place successively, one after the other, in the indicated order, or at the same time.
and subsequently
Step F is a step of tableting by punching, using a press and punches.
The first step, or step A in said process involves mixing the ingredients of a single composition, manually or mechanically, in mixers, batchwise or continuously.
The continuous granulation step, or step B, may take place in a continuous granulator with corotating screws rotating in a jacketed sheath. This step may be carried out
A third step, also called step. C, then involves cooling, which may be performed, for example, by spreading of the grains obtained in the granulation step on a plate (or by extractive transfer) at about 20-25° C.
A fourth, calibration step D is then conducted, for example, on a Frewitt® TC150 calibrator equipped, for example, with a grille with a mesh size of 1.5 mm. The grille and in particular the mesh size thereof will be chosen according to the desired calibration. The components of the external phase will optionally be added during this step.
Where the formulation contains additional components added as external phase during step D, an optional mixing step, or step E, may take place, by means of a tumbling mixer, for example.
Lastly, the grains undergo galenic shaping, advantageously tableting, by means, for example, of a Korsh® XL 100 rotary press of between 10 and 20 KN with a D-type oblong punch with dimensions of 15.5×8 mm, depending on the desired size and shape.
The pharmaceutical compositions, galenic forms, and manufacturing processes according to the present invention may be marked by the presence of the factors or combinations of factors that are set out below. These factors are, among others:
The percentages of the ingredients in the compositions or galenic forms, according to the invention, are selected so as to give a total of 100% by weight, relative to the total weight of said composition or of said galenic form.
The example which follows describes the preparation of pharmaceutical compositions and of galenic forms that are in accordance with the invention. This example is not limiting and merely illustrates the present invention.
Unless otherwise indicated, the percentages of the compounds below are expressed by weight, relative to the total weight of the composition or of the galenic form in which they are located, depending on the specific case.
By way of example, a pharmaceutical composition 1A and a pharmaceutical composition 1B according to the invention, comprising solely dronedarone hydrochloride as active principle, are indicated illustratively in table 1 below.
The nature of the components in these compositions is indicated in said table, along with the concentration of said components, expressed in % by weight of component relative to the total weight of the composition.
Among these components, there are two used to manufacture the grain—dronedarone hydrochloride and the poloxamer. The other components are additional excipients which improve the processability of the formulation.
Other grains were obtained according to steps A, B and C, described below, using dronedarone hydrochloride as active principle, and other hot-melt excipients. These results are summarized in table 1′ below:
Tablets were manufactured using the abovementioned compositions, by the process described below.
A step of mixing (step A) in said process involves mixing in a Turbula® or Servolift® tumbling mixer, for approximately 210 turns, the ingredients of the internal phase of one of the compositions defined above.
This is followed by a step of granulating (step B) using a Consigma® 25 granulator with corotating screws rotating in a jacketed sheath. The parameters are as follows: a powder mixture throughput of 5 to 6 kg/h, a screw speed of 250 to 300 revolutions per minute, a jacket temperature of 80 to 100° C., the temperature of the composition reaching a maximum of 86° C.
A step of cooling (step C) then involves cooling to about 20-25° C. by spreading on a plate or by pneumatic transportation of said grains.
Next, a step of calibrating (step D) is conducted on a Frewitt® TC-150 calibrator by means of a grille with a mesh size of 1.5 mm.
Magnesium stearate, silicone dioxide and crospovidone are optionally added to the grains during step D, where appropriate, with the grains and additional excipients being mixed for approximately 210 turns in a Turbula® or Servolift® tumbling mixer (step E).
The grains, lastly, undergo a tableting step (step F) by means of a Korsh® XL 100 rotary press or a Kilian S100 rotary press at between 10 and 25 KN with an oblong punch 15.5 mm long and 8 mm wide, to form tablets.
Table 2 below collates the characteristics of the tablets 1A and 1B obtained at the outcome of a continuous process with the aid of the compositions described respectively above, and also the characteristics of the reference tablet obtained by wet granulation. For each tablet, table 2 below indicates its total mass and its mass of dronedarone base equivalent (base eq).
Accordingly, for a given amount of active principle, the compositions according to the invention have a mass and a size reduced relative to the reference tablet.
3.1. Procedure for Measuring the Dissolution of the Active Principle:
A tablet is placed in a container containing 1000 ml of pH 4.5 phosphate buffer at a temperature of 37° C. The system is stirred at a speed of 75 rpm by means of a blade, and after 30 minutes the amount of dissolved active principle is measured.
3.2. Results
The percentage by weight of dronedarone dissolved for tablet 1B is 83.3%. It is found that the % of dronedarone dissolution is greater than or equal to 80% by weight of dronedarone, relative to the total weight of dronedarone present in the tablet, and this proves to be in agreement with the regulatory recommendations for immediate-release pharmaceutical forms.
The dose used is 60 mg/animal irrespective of the period/condition, corresponding to 6 mg/kg (assuming a weight of 10 kg for a dog) and to the dose of 400 mg given to a human (that is, about 6 mg/kg for a human weighing 70 kg).
The administration conditions are as follows:
The blood samples are collected in plastic tubes containing lithium heparin as anticoagulant, at the following sampling times: before treatment and 0.5, 1, 2, 3, 4, 6, 8 and 24 hours after administration of each treatment.
The plasma concentration of dronedarone is determined using an exploratory assay method by liquid chromatography coupled to a mass spectrometer (LC-MS/MS). The lower limit of detection with this method for the compounds tested is 0.5 ng/ml.
The pharmacokinetic parameters are calculated from the individual concentrations by a noncompartmental analysis using the WinNonLin 5.2.1 software (Pharsight, USA) and using the theoretical sampling times (provided that the actual sampling times do not differ by more than 15% from the theoretical times).
The following pharmacokinetic parameters were measured for each treatment:
Cmax (ng/ml): corresponds to the maximum plasma concentration observed,
tmax (h): corresponds to the time observed for obtaining the maximum concentration,
AUClast: corresponds to the area under the curve or integral of the plasma concentration as a function of the time t calculated by the trapezium method, from to up to the time corresponding to the last quantifiable concentration.
AUC: corresponds to the area under the curve or integral of plasma concentration as a function of time, extrapolated to infinity.
T1/2z; terminal elimination half-life
Table 3 summarizes the pharmacokinetic parameters following a single oral dose of 60 mg of dronedarone to dogs with controlled gastric pH:
Table 4 shows the relative bioavailability of each formulation tested, under fasting conditions, by comparison with the reference tablet.
Under fasting conditions, the Cmax and the AUC observed with the dronedarone hydrochloride tablets according to the invention are similar to those calculated for the reference tablet (Multaq®).
Table 5 shows the meal effect on the bioavailability of the tablet according to the invention.
There is a positive meal effect tendency when the tablet according to the invention is administered with high-fat food. Specifically, Cmax is increased by a factor of 2.3, AUClast by a factor of 1.5, and AUC 1.4.
| Number | Date | Country | Kind |
|---|---|---|---|
| 1156153 | Jul 2011 | FR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2012/063312 | 7/6/2012 | WO | 00 | 1/7/2014 |
