EP2192894A2 - Novel method for producing dry hydrodispersible pharmaceutical forms - Google Patents

Novel method for producing dry hydrodispersible pharmaceutical forms

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Publication number
EP2192894A2
EP2192894A2 EP08827662A EP08827662A EP2192894A2 EP 2192894 A2 EP2192894 A2 EP 2192894A2 EP 08827662 A EP08827662 A EP 08827662A EP 08827662 A EP08827662 A EP 08827662A EP 2192894 A2 EP2192894 A2 EP 2192894A2
Authority
EP
European Patent Office
Prior art keywords
polyoxyethylene
active ingredient
dispersed
microcrystalline cellulose
fatty acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP08827662A
Other languages
German (de)
French (fr)
Inventor
Patrice Binay
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BIONETWORK
Original Assignee
Coretecholding
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Filing date
Publication date
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Publication of EP2192894A2 publication Critical patent/EP2192894A2/en
Withdrawn legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1617Organic compounds, e.g. phospholipids, fats
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1611Inorganic compounds
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1629Organic macromolecular compounds
    • A61K9/1635Organic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyvinyl pyrrolidone, poly(meth)acrylates
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1629Organic macromolecular compounds
    • A61K9/1652Polysaccharides, e.g. alginate, cellulose derivatives; Cyclodextrin
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2013Organic compounds, e.g. phospholipids, fats

Definitions

  • the drugs have low solubility in water or are poorly salifiable during passage into the stomach, so that they are only partially resorbed.
  • Previous literature has indicated that digestive resorption can be favorably modified by the study of particle size, by the addition of nonionic surfactants in particular, as well as by the addition of a solubilizing agent.
  • micronization of the active ingredient adequately increases the external surface area of the powdery product and is already an approach to this problem.
  • micronization is only appropriate for certain pharmaceutical forms, such as dispersions, or as a filler in capsules. It can not be a general solution for this problem of resorption because some active ingredients are difficult to micronize since too fusible or having a too fragile chemical structure.
  • surfactants can increase the solubility of certain active ingredients and thereby improve the resorption kinetics, but this does not systematically result in higher blood levels.
  • This improvement in the passage through the digestive tract seems to be the result of a decrease in surface tension involving an increase in the permeability of the digestive mucosa. Nevertheless, these large amounts of surfactants are often accompanied by a laxative effect that does not contribute to good absorption.
  • This vitreous state is not very orderly and easy to break. It contributes significantly to an increase in the dissolution rate, especially for substances that are poorly soluble in aqueous media.
  • this technique has had limited development because of the difficulty in generalizing it. In some cases, the dissolution rate is large. In other cases, the dissolution rate is lower and tends to reach an asymptotic value.
  • Another approach to this problem has been the production of solid dispersions of a therapeutic agent in a hydrophilic vehicle having increased solubility in the aqueous medium.
  • This approach consists, first of all, in dissolving the therapeutic active ingredient in a very volatile organic solvent, in which a very hydrophilic polymer such as polyvinylpyrrolidone has been added. Then, the solvent is evaporated to dryness to form a co-precipitate of therapeutic agent and hydrophilic polymer.
  • This technique has made it possible to obtain a marked improvement in absorption kinetics, but it is not suitable for any type of active ingredient.
  • this technique often requires the addition to the solution of a surfactant which increases the wetting ability by the digestive media and possibly limits the phenomenon of crystal formation occurring during the conservation of solid dispersions.
  • the formation of crystalline products contributes to a decrease in the dissolution rate in time function (see Kigudin et al Chem Pharma Bull 9 (1961) 866-872, Duchene D. Pharma 1 (11) (1985) 1064-1073).
  • this technique requires the formation of co-precipitates in a very hydrophilic lactam, such as polyvinylpyrrolidone, having a molecular weight ranging from 10,000 to 5,000, and an oxygenated or chlorinated solvent or mixtures thereof (see patent US-5776495).
  • a very hydrophilic lactam such as polyvinylpyrrolidone, having a molecular weight ranging from 10,000 to 5,000, and an oxygenated or chlorinated solvent or mixtures thereof (see patent US-5776495).
  • the solvent described herein is a vehicle which can be hydrophobic or hydrophilic, which is miscible with water and has a melting point of less than 250 ° C.
  • the preferred solvent is polyethylene glycol with or without Poloxamer 188.
  • Polyethylene stearate 32 is not mentioned in this document and the inert material necessary for the spraying of the vehicle is not micro-crystalline cellulose but lactose.
  • the present invention provides a much simpler and much more satisfactory solution to the problem of the dissolution and intestinal resorption of active ingredients with little or no water-soluble or non-salifiable in the gastric juice.
  • the process according to the invention consists in producing a dispersion of one or more active principle (s) in a polyoxyethylene fatty acid ester 32 easily fusible. This dispersion is sprayed on a granular excipient in a fluidized bed. The powder mixture thus formed is dispensed into pharmaceutical compositions after optional dilution with a pharmaceutically acceptable non-toxic inert carrier.
  • active principle s
  • the expression “easily fuse” here means that this ester melts below 80 0 C and more particularly between 40 and 50 0 C.
  • the polyoxyethylene 32 fatty acid ester used is a polyoxyethylene 32 distearate which melts at around 50 ° C. to 60 ° C.
  • Polyoxyethylene distearate 32 is a product of the invention. commercially available. A product belonging to the same family is sold under the brand Kessco ® PEG 1540 DS (Stepan).
  • the granular excipient is an inert material such as cellulose, dextran, colloidal silica, vinylpyrrolidone polymers or copolymers, polyvinylpyrrolidones, acrylic polymers such as polycarbophil and similar products .
  • a preferred granular material is micro-crystalline cellulose and preferably the pharmaceutical quality marketed under the name AVICEL PH and in particular the quality sold under the name AVICEL PH 105.
  • the content of active ingredient dispersed in the polyoxyethylene fatty acid ester 32 may vary in large proportions because these esters are very good solvents. It is possible to perform both dilute solutions and concentrated solutions.
  • a preferred concentration of active ingredient varies from 30 to 50% of active ingredient in the fatty acid ester. Such contents allow easy entry into solution.
  • a preferred concentration is that consisting of 40 to 50% of active ingredient.
  • compositions according to the invention mention may in particular be made of:
  • Nifedipine and analogues (Nitrendipine, Nisoldipine ).
  • analgesics Fentanyl, Dextropropoxyphene, Sufentanyl.
  • opiate derivatives Nalbuphine, Naltrexone, Dihydrocodeinone, Buprenorphine, or Methadone.
  • the invention finds particular use for the production of pharmaceutical forms whose bioavailability is greatly improved and whose active ingredient is an antilipemic agent and / or cholesterol-lowering agents. More specifically, the preparations based on derivatives of clofibric acid or fenofibric acid such as clofibrate, fenofibrate, gemfibrozil, bezafibrate, ciprofibrate, pirifibrate or simfibrate.
  • HMG coA reductase inhibitors such as Atorvastatin, Cerivastatin, Fluvastatin, Pravastatin and its sodium salt or Simvastatin, or triptans such as Sumatriptan or Frovatriptan.
  • the advantage of a solvent such as a polyoxyethylene fatty acid ester 32 lies in the fact that this product is not likely to promote or produce a transesterification or to increase the toxicity of the active ingredient.
  • Another peculiarity of the present invention is to be able to produce bioavailable forms of hormonal products which are not or hardly absorbable in the digestive tract, such as progesterone, androsterone, chlormadinone acetate or Melengestrol.
  • the alkylated derivatives are used in the 17 ⁇ or 6 ⁇ position to obtain digestive-active compounds (cyproterone, demegestone, promegestone, norethynodiol acetate, ethynyl estradiol).
  • This substitution has the disadvantage of inducing annoying side effects (androgenic or anti-androgenic action, anti-estrogenic action and especially hepatotoxic effects) which are to be avoided in particular.
  • natural progesterone or its derivatives dihydroprogesterone, 17 ⁇ -hydroxyprogesterone
  • the dispersions according to the invention allow the production of pharmaceutical compositions containing, in addition to the active ingredient dispersed on the inert support, one or more pharmaceutically acceptable non-toxic inert excipients.
  • the content of active ingredient is calculated so that the final pharmaceutical formulation contains an effective and non-toxic active ingredient content.
  • the amount of excipient is calculated so that the concentration of active fraction is of the order of 50%, that is to say, it does not exceed 50% and is preferably between 20 and 40%.
  • a particular example is the preparation of pharmaceutical compositions based on fenofibrate absorbate in microcrystalline cellulose.
  • the active ingredient content ranges from 50 to 150 mg per unit dose and preferably 60 mg, 90 mg or 130 mg of fenofibrate.
  • the microcrystalline cellulose content varies from 40 to 60 mg per unit dose.
  • compositions whose active ingredient content ranges from 5 to 50 mg and in particular from 25 to 40 mg per unit dose.
  • the content of polyoxyethylene distearate 32 will also be 5 to 100 mg per unit dose and the excipient content will also be between 5 and 100 mg.
  • Fenofibrate, progesterone or amiodarone preparations are provided hereinafter by way of example. They do not limit the invention.
  • the present invention also relates to the production of sublingual forms or oral tablets. They are intended to be placed under the tongue for sublingual tablets or glued to the palate for oral tablets. These types of tablets made according to the process of the invention show an even greater bioavailability.
  • sublingual or oral tablets are made by the process according to the invention but the granular powdery product is then tabletted by adding a binding agent, a compressing agent and a slip agent.
  • Figures 1 to 4 show the results of pharmacokinetic studies carried out with compositions according to the invention for different active ingredients.
  • the minimum efficiency concentration (MEC) is indicated for each of the compounds.
  • the terms “formulation” and “preparation” are equivalent to the term “composition”.
  • FIG. 1 is a graph showing the average blood concentration (in ⁇ g / ml) as a function of the resorption time after ingestion of the paracetamol tablets (in hours).
  • the results are obtained with a preparation based on 0.350 g of paracetamol produced according to the method of the invention. These results are compared with those obtained with commercial tablets containing the same dosage of paracetamol.
  • FIG. 2 is a graph showing the blood concentration (in ⁇ g / ml) as a function of the resorption time after administration of indomethacin (in hours). This figure represents the results obtained with a formulation prepared according to the method of the invention, and whose active ingredient is indomethacin, in comparison with the results obtained with a commercial formulation of indomethacin.
  • the peak blood concentration for the formulation according to the invention appears rapidly since only 1 hour after the administration of indomethacin.
  • the maximum concentration (Cmax) observed during this peak is 6 ⁇ g / mL for the formulation according to the invention.
  • Cmax the maximum concentration observed during this peak
  • the maximum concentration (C'max) of the commercial formulation is then less than 4 ⁇ g / ml.
  • the EMC of indomethacin is reached 3 hours after the administration of the formulation according to the invention whereas this concentration is never reached for the commercial formulation.
  • FIG. 3 is a graph showing the blood concentration (in ⁇ g / ml) as a function of the resorption time after administration of sumatriptan (in hours). The curves represent the results obtained with a composition according to the invention whose active ingredient is sumatriptan in comparison with those obtained with the commercial product.
  • FIG. 4 is a graph showing the plasma concentration (in ⁇ g / ml) as a function of the resorption time after oral administration of frovatriptan (in hours). The results are obtained from a preparation according to the invention, the active ingredient of which is frovatriptan. These results are compared with those obtained with the commercial formulation of this drug.
  • compositions according to the invention show that in the case of the compositions according to the invention, the active ingredients are reabsorbed more quickly by the body and in greater quantities. Indeed, the resorption of the active ingredients is technically facilitated by the compositions according to the invention and the Cmax concentrations obtained with the compositions according to the invention much higher than the C'max obtained with the similar products of commerce.
  • EMFs are never achieved with the commercial compositions.
  • the EMFs are reached for each of the active ingredients presented in these examples.
  • these concentrations are reached at most about 3 hours after administration of the compositions according to the invention.
  • the compositions according to the invention allow not only a faster resorption but also to reach the concentrations of efficiencies in a short time in cases where these concentrations are not reached with the commercial compositions.

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  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Molecular Biology (AREA)
  • Chemical & Material Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Biophysics (AREA)
  • Epidemiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Medicinal Preparation (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)

Abstract

The invention relates to life's necessities and in particular those relating to health, more particularly a method for dissolving and improving the intestinal absorption of active ingredients which are poorly-water-soluble or water-insoluble or which cannot be turned into salts in gastric juice, containing one or more active ingredients dispersed in a polyoxyethylene 32 fatty acid ester then hot spraying said dispersion onto a granular excipient in a fluid bed. The powder mixture thus formed is distributed in pharmaceutical compositions after optional dilution in a pharmaceutically-acceptable non-toxic inert excipient. The above is of use in the production of pharmaceutical compositions containing one or more pharmaceutically-acceptable non-toxic inert excipients.

Description

Nouveau procédé de production de formes pharmaceutiques sèches hydrodispersibles et les compositions pharmaceutiques ainsi obtenues . A novel process for producing water-soluble dry dosage forms and the pharmaceutical compositions thus obtained.
On sait depuis de nombreuses années que par le côté de l'exploration classique des propriétés pharmacologiques et toxicologiques des médicaments, un des facteurs déterminants de l'activité est l'aspect quantitatif de la résorption du composant actif. La cinétique devient de plus en plus le sujet d'études systématiques étant donné que l'intensité de la réponse et souvent sa nature sont fonction de la concentration obtenue au niveau de l'organe récepteur. L'importance de ces études sur la pharmacocinétique, et par conséquent sur la bio disponibilité, a montré tout l'intérêt des modifications notamment galéniques apportées au cours de la préparation des formes pharmaceutiques, principalement en vue d'obtenir celles les plus adaptées pour l'administration par la voie digestive.It has been known for many years that by the conventional exploration side of the pharmacological and toxicological properties of drugs, one of the determining factors of activity is the quantitative aspect of the resorption of the active component. Kinetics is becoming more and more the subject of systematic studies since the intensity of the response and often its nature is a function of the concentration obtained at the level of the receptor organ. The importance of these studies on pharmacokinetics, and consequently on bioavailability, has shown the interest of the modifications, especially galenical, made during the preparation of pharmaceutical forms, mainly in order to obtain the most appropriate ones for administration by the digestive tract.
Le problème majeur de la faible résorption intestinale des médicaments semble être lié au fait que celle-ci s'effectue pendant un temps assez court sur une surface réduite de l'intestin. Pour augmenter cette résorption, il est donc important que le principe actif y soit convoyé rapidement et complètement, sous une forme rendue soluble.The major problem of low intestinal resorption of drugs seems to be related to the fact that it occurs for a short time on a small area of the intestine. To increase this resorption, it is therefore important that the active ingredient is conveyed quickly and completely, in a form made soluble.
Les médicaments ont une faible solubilité dans l'eau ou sont faiblement salifiables pendant le passage dans l'estomac, de sorte qu'ils ne sont que partiellement résorbés. La littérature antérieure a indiqué que la résorption par voie digestive peut être modifiée d'une manière favorable par l'étude de la taille des particules, par l'adjonction d'agents tensio-actifs non ioniques notamment, ainsi que par l'addition d'un agent solubilisant.The drugs have low solubility in water or are poorly salifiable during passage into the stomach, so that they are only partially resorbed. Previous literature has indicated that digestive resorption can be favorably modified by the study of particle size, by the addition of nonionic surfactants in particular, as well as by the addition of a solubilizing agent.
Par ailleurs, la micronisation du principe actif augmente d'une manière adéquate la surface spécifique externe du produit pulvérulent et constitue déjà une approche de ce problème. Toutefois, la micronisation n'est appropriée que pour certaines formes pharmaceutiques, telles que des dispersions, ou comme charge dans des gélules. Elle ne peut être une solution générale pour ce problème de résorption car certains principes actifs sont difficiles à microniser puisque trop fusibles ou ayant une structure chimique trop fragile .Moreover, the micronization of the active ingredient adequately increases the external surface area of the powdery product and is already an approach to this problem. However, micronization is only appropriate for certain pharmaceutical forms, such as dispersions, or as a filler in capsules. It can not be a general solution for this problem of resorption because some active ingredients are difficult to micronize since too fusible or having a too fragile chemical structure.
L'addition d'agents tensio-actifs peut augmenter la solubilité de certains principes actifs et par là améliorer la cinétique de résorption, mais cela ne permet pas systématiquement d'obtenir des taux sanguins plus élevés. En outre, il est souvent nécessaire d'ajouter des quantités importantes d'agents tensio-actifs (de 25 à 50 %) pour obtenir un résultat significatif. Cette amélioration dans le passage par le tube digestif semble être le résultat d'une diminution de tension superficielle impliquant une augmentation de la perméabilité de la muqueuse digestive. Néanmoins, ces quantités importantes d'agents tensio-actifs s'accompagnent souvent d'un effet laxatif qui ne contribue pas à une bonne absorption.The addition of surfactants can increase the solubility of certain active ingredients and thereby improve the resorption kinetics, but this does not systematically result in higher blood levels. In addition, it is often necessary to add significant amounts of surfactants (from 25 to 50%) to obtain a significant result. This improvement in the passage through the digestive tract seems to be the result of a decrease in surface tension involving an increase in the permeability of the digestive mucosa. Nevertheless, these large amounts of surfactants are often accompanied by a laxative effect that does not contribute to good absorption.
Une autre approche a consisté à ajouter un agent émulsionnant et notamment un ester d'acide gras d'un hydrate de carbone (sucrose ester) et procède d'un autre principe. Cet ester augmente la lipophilie de la molécule et facilite ainsi le passage à travers la barrière intestinale. Néanmoins, ce type de processus ne donne de résultats concluants qu'avec des molécules très lipophiles et nécessite des concentrations élevées de cet ester.Another approach has been to add an emulsifier including a fatty acid ester of a carbohydrate (sucrose ester) and proceeds from another principle. This ester increases the lipophilicity of the molecule and thus facilitates the passage through the intestinal barrier. Nevertheless, this type of process gives conclusive results only with very lipophilic molecules and requires high concentrations of this ester.
Plus récemment, pour améliorer la résorption de substances actives dont la solubilité dans les liquides biologiques est faible, on a essayé d'augmenter la cinétique de dissolution en produisant des dispersions solides. Ces dispersions solides, telles que définies par Chiou et al, dans J. Pharm. Sci. 60 (194) 1281-1302, ont consisté à réaliser un système qui en fonction du processus, utilisé en vue de leur production, peut présenter différentes structures (voir Fort et al. Pharm Acta HeIv. 61 (3) (1986) 69-88 ou Bloc et al. Pharm Acta HeIv. 62 (1987) 23-27) correspondant à différents états cristallins. L'état vitreux, bien qu'il soit considéré comme un état solide, comporte une phase liquide qui contribue à son désordre structural. Cet état vitreux est peu ordonné et facile à rompre. Il contribue d'une manière importante à une augmentation de la vitesse de dissolution, notamment pour les substances peu solubles dans les milieux aqueux. Cependant, malgré le grand nombre de publications relatives à la production de dispersions solides, tout spécialement à base de Macrogols ou de Poloxamères, cette technique n'a connu qu'un développement limité en raison de la difficulté à la généraliser. Dans certains cas, la vitesse de dissolution est grande. Dans d'autres cas, la vitesse de dissolution est plus faible et tend à atteindre une valeur asymptotique .More recently, to improve the absorption of active substances whose solubility in biological liquids is low, an attempt has been made to increase the kinetics of dissolution by producing solid dispersions. These solid dispersions, as defined by Chiou et al, in J. Pharm. Sci. 60 (194) 1281-1302, has been to realize a system which depending on the process, used for their production, may have different structures (see Fort and al., Pharm Acta HeIv 61 (3) (1986) 69- 88 or Bloc et al., Pharm Acta HeIv 62 (1987) 23-27) corresponding to different crystalline states. The vitreous state, although considered a solid state, has a liquid phase which contributes to its structural disorder. This vitreous state is not very orderly and easy to break. It contributes significantly to an increase in the dissolution rate, especially for substances that are poorly soluble in aqueous media. However, despite the large number of publications relating to the production of solid dispersions, especially based on Macrogols or Poloxamers, this technique has had limited development because of the difficulty in generalizing it. In some cases, the dissolution rate is large. In other cases, the dissolution rate is lower and tends to reach an asymptotic value.
C'est ainsi que, pour un même principe actif et à des concentrations semblables, on a constaté des variations très importantes dans la vitesse de mise en solution selon la nature de l'agent co-fondant. Il a même été constaté, dans certains cas, l'impossibilité d'obtenir une solubilisation complète du principe actif, même après un temps de contact prolongé, ou surtout une tendance à la recristallisation.Thus, for the same active ingredient and at similar concentrations, there were very significant variations in the dissolution rate depending on the nature of the co-melt agent. It has even been found, in some cases, the impossibility of obtaining a complete solubilization of the active ingredient, even after a prolonged contact time, or especially a tendency to recrystallization.
Une autre voie d' approche de ce problème a été la réalisation de dispersions solides d'un agent thérapeutique dans un véhicule hydrophile ayant une solubilité accrue dans le milieu aqueux. Cette approche consiste, tout d'abord, à dissoudre le principe actif thérapeutique dans un solvant organique très volatil, dans lequel on a ajouté un polymère très hydrophile comme la polyvinylpyrrolidone . Ensuite, le solvant est évaporé à sec pour former un co-précipité d'agent thérapeutique et de polymère hydrophile.Another approach to this problem has been the production of solid dispersions of a therapeutic agent in a hydrophilic vehicle having increased solubility in the aqueous medium. This approach consists, first of all, in dissolving the therapeutic active ingredient in a very volatile organic solvent, in which a very hydrophilic polymer such as polyvinylpyrrolidone has been added. Then, the solvent is evaporated to dryness to form a co-precipitate of therapeutic agent and hydrophilic polymer.
Cette technique a permis d'obtenir une nette amélioration de la cinétique d'absorption mais elle n'est pas adaptée à tout type de principe actif. En outre, cette technique nécessite souvent l'adjonction à la solution d'un agent tensioactif qui augmente l'aptitude au mouillage par les milieux digestifs et éventuellement limite le phénomène de formation de cristaux survenant pendant la conservation de dispersions solides. La formation de produits cristallins contribue à une diminution de la vitesse de dissolution en fonction du temps (voir Kigudin et al Chem. Pharma. Bull 9 (1961) 866-872, Duchène D. Pharma 1 (11) (1985) 1064-1073) .This technique has made it possible to obtain a marked improvement in absorption kinetics, but it is not suitable for any type of active ingredient. In addition, this technique often requires the addition to the solution of a surfactant which increases the wetting ability by the digestive media and possibly limits the phenomenon of crystal formation occurring during the conservation of solid dispersions. The formation of crystalline products contributes to a decrease in the dissolution rate in time function (see Kigudin et al Chem Pharma Bull 9 (1961) 866-872, Duchene D. Pharma 1 (11) (1985) 1064-1073).
Par ailleurs, cette technique nécessite la formation de co-précipités dans un lactame très hydrophile, comme la polyvinylpyrrolidone, ayant un poids moléculaire variant de 10.000 à 5.000, et d'un solvant oxygéné ou chloré ou des mélanges de ceux-ci (voir brevet US-5776495) .Moreover, this technique requires the formation of co-precipitates in a very hydrophilic lactam, such as polyvinylpyrrolidone, having a molecular weight ranging from 10,000 to 5,000, and an oxygenated or chlorinated solvent or mixtures thereof (see patent US-5776495).
Une approche plus récente se trouve dans le document WO2005/034920 au nom de Life Cycle Pharma qui décrit la technique MeIt Dose. Cette technique permet une meilleure absorption orale des molécules ayant une faible solubilité dans l'eau. Cette technique consiste à dissoudre les molécules dans un solvant qui facilite la pénétration dans l'épithélium du tube intestinal pour permettre le passage dans le courant sanguin.A more recent approach is found in WO2005 / 034920 in the name of Life Cycle Pharma which describes the MeIt Dose technique. This technique allows better oral absorption of molecules with low solubility in water. This technique involves dissolving the molecules in a solvent that facilitates penetration into the epithelium of the intestinal tract to allow passage into the bloodstream.
Le solvant décrit dans ce document est un véhicule qui peut être hydrophobe ou hydrophile, qui est miscible à l'eau et qui possède un point de fusion inférieur à 250° C. Le solvant préféré est un polyéthylène glycol additionné ou non de Poloxamer 188.The solvent described herein is a vehicle which can be hydrophobic or hydrophilic, which is miscible with water and has a melting point of less than 250 ° C. The preferred solvent is polyethylene glycol with or without Poloxamer 188.
Le stéarate de polyéthylène 32 n' est pas mentionné dans ce document et le matériau inerte nécessaire pour la pulvérisation du véhicule n'est pas la cellulose micro cristalline mais le lactose.Polyethylene stearate 32 is not mentioned in this document and the inert material necessary for the spraying of the vehicle is not micro-crystalline cellulose but lactose.
La présente invention apporte une solution bien plus simple et bien plus satisfaisante au problème de la mise en solution et de la résorption intestinale des principes actifs peu ou pas solubles dans l'eau ou non salifiables dans le suc gastrique.The present invention provides a much simpler and much more satisfactory solution to the problem of the dissolution and intestinal resorption of active ingredients with little or no water-soluble or non-salifiable in the gastric juice.
Le procédé selon l'invention consiste à réaliser une dispersion d'un ou plusieurs principe (s) actif (s) dans un ester d'acide gras de polyoxyéthylène 32 facilement fusible. Cette dispersion est pulvérisée à chaud sur un excipient granulaire en lit fluidisé. On distribue le mélange pulvérulent ainsi formé dans des compositions pharmaceutiques après dilution éventuelle par un excipient inerte non toxique pharmaceutiquement acceptable. L'expression « facilement fusible » signifie ici que cet ester fond en dessous de 800C et plus particulièrement entre 40 et 500C.The process according to the invention consists in producing a dispersion of one or more active principle (s) in a polyoxyethylene fatty acid ester 32 easily fusible. This dispersion is sprayed on a granular excipient in a fluidized bed. The powder mixture thus formed is dispensed into pharmaceutical compositions after optional dilution with a pharmaceutically acceptable non-toxic inert carrier. The expression "easily fuse "here means that this ester melts below 80 0 C and more particularly between 40 and 50 0 C.
Selon une forme préférée de l'invention, on utilise comme ester d'acide gras de polyoxyéthylène 32 un distéarate de polyoxyéthylène 32 dont la fusion s'effectue aux environs de 500C à 600C. Le distéarate de polyoxyéthylène 32 est un produit disponible commercialement. Un produit appartenant à la même famille est vendu sous la marque Kessco ® PEG 1540 DS (Stepan) .According to a preferred form of the invention, the polyoxyethylene 32 fatty acid ester used is a polyoxyethylene 32 distearate which melts at around 50 ° C. to 60 ° C. Polyoxyethylene distearate 32 is a product of the invention. commercially available. A product belonging to the same family is sold under the brand Kessco ® PEG 1540 DS (Stepan).
Selon une autre forme préférée de l'invention, l'excipient granulaire est un matériau inerte comme la cellulose, le dextrane, la silice colloïdale, les polymères ou copolymères de vinylpyrrolidone, les poly vinylpyrrolidones, les polymères acryliques comme le polycarbophil et les produits similaires.According to another preferred form of the invention, the granular excipient is an inert material such as cellulose, dextran, colloidal silica, vinylpyrrolidone polymers or copolymers, polyvinylpyrrolidones, acrylic polymers such as polycarbophil and similar products .
Un matériau granulaire préféré est la cellulose micro cristalline et de préférence la qualité pharmaceutique commercialisée sous la dénomination AVICEL PH et en particulier la qualité vendue sous la dénomination AVICEL PH 105.A preferred granular material is micro-crystalline cellulose and preferably the pharmaceutical quality marketed under the name AVICEL PH and in particular the quality sold under the name AVICEL PH 105.
La teneur en principe actif dispersé dans l'ester d'acide gras de polyoxyéthylène 32 peut varier dans des proportions importantes car ces esters sont de très bons solvants. Il est possible de réaliser aussi bien des solutions diluées que des solutions concentrées.The content of active ingredient dispersed in the polyoxyethylene fatty acid ester 32 may vary in large proportions because these esters are very good solvents. It is possible to perform both dilute solutions and concentrated solutions.
Une concentration en principe actif préférée varie de 30 à 50 % de principe actif dans l'ester d'acide gras. De telles teneurs permettent d'entrer facilement en solution. Une concentration préférée est celle constituée de 40 à 50 % de principe actif.A preferred concentration of active ingredient varies from 30 to 50% of active ingredient in the fatty acid ester. Such contents allow easy entry into solution. A preferred concentration is that consisting of 40 to 50% of active ingredient.
Parmi les principes actifs qu' il est possible d'incorporer dans les compositions selon l'invention, on pourra citer notamment :Among the active ingredients that can be incorporated into the compositions according to the invention, mention may in particular be made of:
• des anti-inflammatoires et antalgiques• anti-inflammatories and analgesics
Salsalatesalsalate
Benorylatebenorylate
Oxametacine IndometacineOxametacine indomethacin
ParacétamolParacetamol
Piroxicampiroxicam
Acide TiéniliqueTiénilique acid
L' EthenzamideEthenzamide
Le TramadolTramadol
• des immunosuppresssants Cyclosporine Tacrolimus• immunosuppressants Cyclosporine Tacrolimus
• des anti-histaminiques Terfenadine Brompheniramine Chlorpheniraminé• antihistamines Terfenadine Brompheniramine Chlorpheniramine
• des antifongiques et des anti-trichomonas Metronidazole• antifungals and anti-trichomonas Metronidazole
Ornidazole Dapsone Itraconazole TerbinafineOrnidazole Dapsone Itraconazole Terbinafine
• des antiviraux Cytarabine Gancyclovir Acyclovir• antivirals Cytarabine Gancyclovir Acyclovir
• des antipsychotiques Sulpiride Sultopride Amisulpride• Antipsychotic Sulpiride Sultopride Amisulpride
• des hormones• hormones
L'Estradiol et ses esters (17β-valérate)Estradiol and its esters (17β-valerate)
L' EstroneThe Estrone
L'EstriolThe estriol
La progestérone et ses dérivés • des agents cardio vasculaires et vasodilatateurs DobutamineProgesterone and its derivatives • cardiovascular and vasodilator agents Dobutamine
Diltiazemdiltiazem
Nifedipine et analogues (Nitrendipine, Nisoldipine ... )Nifedipine and analogues (Nitrendipine, Nisoldipine ...)
• des agents antiulcéreux Pirenzépine Ranitidine• Antiulcer agents Pirenzepine Ranitidine
Oméprazole LansoprazoleOmeprazole Lansoprazole
• des agents antibactériens Erythromycine Flumequine Oxytetracycline Piperacilline Cefuroxime Amphotéricine• Antibacterial agents Erythromycin Flumequine Oxytetracycline Piperacillin Cefuroxime Amphotericin
• des agents anti-arythmiques Propafenone• Propafenone anti-arrhythmic agents
Amiodaroneamiodarone
CordaroneCordarone
Flecainideflecainide
Gallopamil,gallopamil,
Verapamil,verapamil,
Dipyridamole,dipyridamole,
DiisopyramideDiisopyramide
• des agents uricosuriques Benzbromarone Probenécid• uricosuric agents Benzbromarone Probenecid
Suifinpyrazone AllopurinolSuifinpyrazone Allopurinol
• des agents antimigraineux Flunarizine Les dérivés de l'Ergotamine Sumatriptan• Flunarizine antimigraine agents Derivatives of Ergotamine Sumatriptan
• des agents antidépresseurs Fluvoxamine• Fluvoxamine antidepressant agents
Fluanisone Fluoxétine ParoxétineFluanisone Fluoxetine Paroxetine
• des agents anti-hormonaux Flutamide• Flutamide anti-hormonal agents
• des bronchodilatateurs Tulobutérol Talinolol Prenaltérol• Bronchodilators Tulobutol Talinolol Prenalterol
• des agents anxiolytiques Thiothixène• anxiolytic Thiothixene agents
Trazodonetrazodone
DoxepineDoxepin
Carbamazépinecarbamazepine
• des coronarodilatateurs L' Ethaverine• coronarodilators Ethaverine
La Pentoxyphylline L' EburnamoninePentoxyphylline Eburnamonine
• des Diurétiques Le Furosemide• Diuretics Furosemide
Le TriamterèneThe Triamterene
Le TorasemideThe Torasemide
L' HydrochlorothiazideHydrochlorothiazide
• des antispasmodiques Flavoxate Trimébutine Phlorogucinol • des agents inhibant l'excrétion du calcium Clodronate• antispasmodics Flavoxate Trimebutine Phlorogucinol • agents that inhibit the excretion of calcium Clodronate
Pamidronate AlendronatePamidronate Alendronate
• des agents anticoagulants Pindione• Pindione anticoagulants
TromexanTromexan
des antalgiques le Fentanyl, le Dextropropoxyphène, le Sufentanyl.analgesics Fentanyl, Dextropropoxyphene, Sufentanyl.
des dérivés opiacés la Nalbuphine, la Naltrexone, la Dihydrocodéïnone, la Buprenorphine, ou la Méthadone.opiate derivatives Nalbuphine, Naltrexone, Dihydrocodeinone, Buprenorphine, or Methadone.
L' invention trouve un emploi tout particulier pour la réalisation de formes pharmaceutiques dont la biodisponibilité est grandement améliorée et dont le principe actif est un agent antilipémique et/ou hypocholestérolémiants . On peut citer plus précisément les préparations à base de dérivés de l'acide clofibrique ou de l'acide fenofibrique comme par exemple le clofibrate, le fénofibrate, le gémfibrozil, le bezafibrate, le ciprofibrate, le pirifibrate ou le simfibrate. On peut citer également les inhibiteurs de HMG coA réductases (statines) comme 1' Atorvastatine, le Cérivastatine, la Fluvastatine, la Pravastatine et son sel de sodium ou la Simvastatine, ou encore des triptans comme le Sumatriptan ou le Frovatriptan.The invention finds particular use for the production of pharmaceutical forms whose bioavailability is greatly improved and whose active ingredient is an antilipemic agent and / or cholesterol-lowering agents. More specifically, the preparations based on derivatives of clofibric acid or fenofibric acid such as clofibrate, fenofibrate, gemfibrozil, bezafibrate, ciprofibrate, pirifibrate or simfibrate. Mention may also be made of HMG coA reductase inhibitors (statins) such as Atorvastatin, Cerivastatin, Fluvastatin, Pravastatin and its sodium salt or Simvastatin, or triptans such as Sumatriptan or Frovatriptan.
Dans le cas particulier des dérivés de l'acide clofibrique, l'intérêt d'un solvant comme un ester d'acide gras de polyoxyéthylène 32 réside dans le fait que ce produit n'est pas susceptible de favoriser ou de produire une transesterification ou bien encore d'augmenter la toxicité du principe actif.In the particular case of clofibric acid derivatives, the advantage of a solvent such as a polyoxyethylene fatty acid ester 32 lies in the fact that this product is not likely to promote or produce a transesterification or to increase the toxicity of the active ingredient.
Une autre particularité de la présente invention est de pouvoir réaliser des formes biodisponibles de produits hormonaux qui sont peu ou pas résorbables dans le tube digestif comme la progestérone, l' androstérone, la chlormadinone acétate ou le Melengestrol . Habituellement, on utilise les dérivés alkylés en position 17α ou en position 6α pour obtenir des composés actifs par voie digestive (cyproterone, demegestone, promegestone, norethynodiol acétate, éthynyl estradiol) . Cette substitution à l'inconvénient d'induire des effets secondaires gênants (action androgène ou anti-androgène, action anti-estrogène et surtout des effets hépatotoxiques) qui sont à éviter tout particulièrement. C'est pourquoi on utilise souvent la progestérone naturelle ou ses dérivés (dihydroprogestérone, 17α-hydroxyprogestérone) , ces derniers étant actifs par voie digestive et peu toxiques mais toutefois moins actifs que la progestérone elle-même.Another peculiarity of the present invention is to be able to produce bioavailable forms of hormonal products which are not or hardly absorbable in the digestive tract, such as progesterone, androsterone, chlormadinone acetate or Melengestrol. Usually, the alkylated derivatives are used in the 17α or 6α position to obtain digestive-active compounds (cyproterone, demegestone, promegestone, norethynodiol acetate, ethynyl estradiol). This substitution has the disadvantage of inducing annoying side effects (androgenic or anti-androgenic action, anti-estrogenic action and especially hepatotoxic effects) which are to be avoided in particular. This is why natural progesterone or its derivatives (dihydroprogesterone, 17α-hydroxyprogesterone) are often used, the latter being active digestive and not very toxic but less active than progesterone itself.
Les dispersions selon l'invention permettent la réalisation de compositions pharmaceutiques renfermant, outre le principe actif dispersé sur le support inerte, un ou plusieurs excipients inertes non toxiques pharmaceutiquement acceptables .The dispersions according to the invention allow the production of pharmaceutical compositions containing, in addition to the active ingredient dispersed on the inert support, one or more pharmaceutically acceptable non-toxic inert excipients.
Il sera ainsi possible d'additionner les préparations obtenues après incorporation dans un matériau inerte suivi d'un séchage sur lit fluidisé, d'agent diluant, d'agent de charge, d'agent aromatisant, d'agent colorant, d'agent de délitement, d'agent gélifiant, ou d'un agent filmogène.It will thus be possible to add the preparations obtained after incorporation in an inert material followed by fluidized bed drying, diluent, bulking agent, flavoring agent, coloring agent, disintegration, gelling agent, or a film-forming agent.
La teneur en principe actif est calculée de telle sorte que la formule pharmaceutique finale contienne une teneur efficace et non toxique en principe actif. La quantité d' excipient est calculée pour que la concentration en fraction active soit de l'ordre de 50 %, c'est-à-dire qu'elle ne dépasse pas 50% et soit comprise de préférence entre 20 et 40%. Un exemple particulier réside dans la préparation de compositions pharmaceutiques à base d' absorbât de fénofibrate dans de la cellulose microcristalline. Dans ces compositions, la teneur en principe actif s'échelonne de 50 à 150 mg par prise unitaire et de préférence 60 mg, 90 mg ou 130 mg de fénofibrate. La teneur en cellulose microcristalline varie de 40 à 60 mg par prise unitaire.The content of active ingredient is calculated so that the final pharmaceutical formulation contains an effective and non-toxic active ingredient content. The amount of excipient is calculated so that the concentration of active fraction is of the order of 50%, that is to say, it does not exceed 50% and is preferably between 20 and 40%. A particular example is the preparation of pharmaceutical compositions based on fenofibrate absorbate in microcrystalline cellulose. In these compositions, the active ingredient content ranges from 50 to 150 mg per unit dose and preferably 60 mg, 90 mg or 130 mg of fenofibrate. The microcrystalline cellulose content varies from 40 to 60 mg per unit dose.
Dans le cas de la progestérone, on pourra réaliser des compositions pharmaceutiques dont la teneur en principe actif s'échelonne de 5 à 50 "mg et en particulier de 25 à 40 mg par prise unitaire. La teneur en distéarate de polyoxyéthylène 32 sera également de 5 à 100 mg par prise unitaire et la teneur en excipient sera également comprise entre 5 et 100 mg.In the case of progesterone, it will be possible to produce pharmaceutical compositions whose active ingredient content ranges from 5 to 50 mg and in particular from 25 to 40 mg per unit dose.The content of polyoxyethylene distearate 32 will also be 5 to 100 mg per unit dose and the excipient content will also be between 5 and 100 mg.
Des préparations à base de fénofibrate, à base de progestérone ou à base d' amiodarone sont fournies ci-après à titre d'exemple. Elles ne limitent en rien l'invention.Fenofibrate, progesterone or amiodarone preparations are provided hereinafter by way of example. They do not limit the invention.
Exemple IExample I
Fénofibrate 25 gFenofibrate 25 g
Distéarate de polyoxyéthylène 32 26 gPolyoxyethylene distearate 32 26 g
Cellulose microcristalline 44 gMicrocrystalline cellulose 44 g
Stéarate de magnésium 0,5 g Le mélange ainsi réalisé a été réparti en 1 000 gélules de gélatine contenant 25 mg de fénofibrate par prise unitaire .Magnesium Stearate 0.5 g The resulting mixture was divided into 1000 gelatin capsules containing 25 mg fenofibrate per unit dose.
Exemple IIExample II
Progestérone 30 gProgesterone 30 g
Distéarate de polyoxyéthylène 32 25 gPolyoxyethylene distearate 32 25 g
Cellulose microcristalline 55 gMicrocrystalline cellulose 55 g
Malto dextrine 12 gMalto dextrine 12 g
Carbonate de Calcium 5 gCalcium carbonate 5 g
Talc 5 g pour 1 000 gélules contenant chacune 30 mg de progestérone .Talc 5 g per 1000 capsules each containing 30 mg of progesterone.
Exemple IIIExample III
Amiodarone 150 g IZAmiodarone 150 g IZ
Distéarate de polyoxyéthylène 32 180 g Polyvinylpyrolidone 20 gPolyoxyethylene Distearate 32 180 g Polyvinylpyrrolidone 20 g
Silice colloïdale 45 gColloidal silica 45 g
Amidon de riz 105 g pour 1 000 comprimés contenant chacun 150 mg d' Amiodarone .Rice starch 105 g per 1,000 tablets each containing 150 mg of Amiodarone.
La présente invention a également pour objet la production de formes sublinguales ou de comprimés buccaux. Elles sont destinées à être placées sous la langue pour les comprimés sublinguaux ou collées au palais pour les comprimés buccaux. Ces types de comprimés réalisés selon le procédé de l'invention manifestent une biodisponibilité encore accrue.The present invention also relates to the production of sublingual forms or oral tablets. They are intended to be placed under the tongue for sublingual tablets or glued to the palate for oral tablets. These types of tablets made according to the process of the invention show an even greater bioavailability.
Ces comprimés sublinguaux ou buccaux sont réalisés grâce au procédé selon l' invention mais le produit granulaire pulvérulent est ensuite transformé en comprimés par addition d'un agent liant, d'un agent de compression et d'un agent de glissement .These sublingual or oral tablets are made by the process according to the invention but the granular powdery product is then tabletted by adding a binding agent, a compressing agent and a slip agent.
Les figures 1 à 4 montrent les résultats des études pharmacocinétiques réalisées avec des compositions selon l'invention pour différents principes actifs. La concentration d'efficacité minimale (CEM) est indiquée pour chacun des composés. Dans les exemples suivants, les termes « formulation » et « préparation » sont équivalents au terme « composition ».Figures 1 to 4 show the results of pharmacokinetic studies carried out with compositions according to the invention for different active ingredients. The minimum efficiency concentration (MEC) is indicated for each of the compounds. In the following examples, the terms "formulation" and "preparation" are equivalent to the term "composition".
La figure 1 est un graphique montrant la concentration sanguine moyenne (en μg/mL) en fonction du délai de résorption après ingestion des comprimés de paracétamol (en heures) . Pour la formulation selon l'invention, les résultats sont obtenus avec une préparation à base de 0,350 g de paracétamol produite selon le procédé de l'invention. Ces résultats sont comparés à ceux obtenus avec des comprimés commerciaux contenant le même dosage de paracétamol.FIG. 1 is a graph showing the average blood concentration (in μg / ml) as a function of the resorption time after ingestion of the paracetamol tablets (in hours). For the formulation according to the invention, the results are obtained with a preparation based on 0.350 g of paracetamol produced according to the method of the invention. These results are compared with those obtained with commercial tablets containing the same dosage of paracetamol.
On peut voir sur cette figure que, dans le cas de la formulation selon l'invention, le pic de concentration est atteint seulement 1 heure après l'ingestion des comprimés de paracétamol et que la concentration maximale (Cmax) est alors de 6,0 μg/ml. Ce pic de concentration sanguine n' apparaît qu'au bout de 4 heures avec la formulation commerciale et la concentration maximale (C'max) est alors inférieure à 4,0 μg/ml. Par ailleurs, la CEM du paracétamol est atteinte en seulement 1/2 heure pour la formulation de paracétamol selon l'invention alors que cette concentration n'est atteinte qu'au bout de 2 heures avec la formulation commerciale.It can be seen in this figure that, in the case of the formulation according to the invention, the peak concentration is reached only 1 hour after ingestion of paracetamol tablets and that the maximum concentration (Cmax) is then 6.0 mcg / ml. This peak of blood concentration does not appear that after 4 hours with the commercial formulation and the maximum concentration (C'max) is then less than 4.0 μg / ml. Moreover, the CEM of paracetamol is reached in only 1/2 hour for the formulation of paracetamol according to the invention whereas this concentration is reached after 2 hours with the commercial formulation.
La figure 2 est un graphique montrant la concentration sanguine (en μg/ml) en fonction du délai de résorption après administration de l' indométacine (en heures) . Cette figure représente les résultats obtenus avec une formulation préparée selon le procédé de l'invention, et dont le principe actif est de l' indométacine, en comparaison avec les résultats obtenus avec une formulation d' indométacine du commerce .FIG. 2 is a graph showing the blood concentration (in μg / ml) as a function of the resorption time after administration of indomethacin (in hours). This figure represents the results obtained with a formulation prepared according to the method of the invention, and whose active ingredient is indomethacin, in comparison with the results obtained with a commercial formulation of indomethacin.
D'après les courbes représentées, le pic de concentration sanguine pour la formulation selon l'invention apparaît rapidement puisque seulement 1 heure après l'administration de l' indométacine . De plus, la concentration maximale (Cmax) constatée lors de ce pic est de 6 μg/mL pour la formulation selon l'invention. Pour la formulation commerciale, il faut attendre 4 heures après l'administration pour que le pic de concentration sanguine soit constaté et la concentration maximale (C'max) de la formulation commerciale est alors inférieure à 4 μg/ml. De plus, la CEM de l' indométacine est atteinte 3 heures après l'administration de la formulation selon l'invention alors que cette concentration n'est jamais atteinte pour la formulation commerciale.From the curves shown, the peak blood concentration for the formulation according to the invention appears rapidly since only 1 hour after the administration of indomethacin. In addition, the maximum concentration (Cmax) observed during this peak is 6 μg / mL for the formulation according to the invention. For the commercial formulation, it is necessary to wait 4 hours after the administration so that the peak of blood concentration is found and the maximum concentration (C'max) of the commercial formulation is then less than 4 μg / ml. In addition, the EMC of indomethacin is reached 3 hours after the administration of the formulation according to the invention whereas this concentration is never reached for the commercial formulation.
La figure 3 est un graphique montrant la concentration sanguine (en μg/ml) en fonction du délai de résorption après administration de sumatriptan (en heures) . Les courbes représentent les résultats obtenus avec une composition selon l'invention dont le principe actif est le sumatriptan en comparaison avec ceux obtenus avec le produit commercial.FIG. 3 is a graph showing the blood concentration (in μg / ml) as a function of the resorption time after administration of sumatriptan (in hours). The curves represent the results obtained with a composition according to the invention whose active ingredient is sumatriptan in comparison with those obtained with the commercial product.
On peut voir sur ce graphique que le pic de concentration sanguine est atteint seulement 1 heure après l'administration de la composition selon l'invention et la concentration maximale (Cmax) est alors de 3 μg/ml. Dans le cas du produit commercial, le pic sanguin n'apparaît que 4 heures après l'administration et la concentration maximale (C'max) est inférieure à 2 μg/ml pour ce produit commercial. Par ailleurs, la CEM pour le sumatriptan est atteinte 3 heures après l'administration de la composition selon l'invention alors qu'avec le produit commercial cette concentration n'est jamais atteinte.It can be seen from this graph that the peak of blood concentration is reached only 1 hour after the administration of the composition according to the invention and the maximum concentration (Cmax) is then 3 μg / ml. In the case of the commercial product, the peak blood appears only 4 hours after the administration and the maximum concentration (C'max) is less than 2 μg / ml for this commercial product. Moreover, the CEM for sumatriptan is reached 3 hours after the administration of the composition according to the invention whereas with the commercial product this concentration is never reached.
La figure 4 est un graphique montrant la concentration plasmatique (en μg/ml) en fonction du délai de résorption après administration orale de frovatriptan (en heures) . Les résultats sont obtenus à partir d'une préparation selon l'invention dont le principe actif est le frovatriptan. Ces résultats sont comparés avec ceux obtenus avec la formulation commerciale de ce médicament.FIG. 4 is a graph showing the plasma concentration (in μg / ml) as a function of the resorption time after oral administration of frovatriptan (in hours). The results are obtained from a preparation according to the invention, the active ingredient of which is frovatriptan. These results are compared with those obtained with the commercial formulation of this drug.
Cette figure montre que le pic de concentration est atteint seulement 1/2 heure après l'administration de la préparation selon l'invention et la concentration maximale (Cmax) est alors de 7,5 μg/ml. Pour la formulation commerciale, il faut attendre 2 heures pour voir apparaître le pic de concentration, la concentration maximale (C'max) étant alors inférieure à 5 μg/ml. En outre, la CEM du frovatriptan est atteinte environ 1 heure 30 après l'administration de la préparation selon l'invention alors que cette concentration n'est jamais atteinte avec la formulation commerciale.This figure shows that the peak concentration is reached only 1/2 hour after administration of the preparation according to the invention and the maximum concentration (Cmax) is then 7.5 μg / ml. For the commercial formulation, it is necessary to wait 2 hours to see appear peak concentration, the maximum concentration (C'max) being then less than 5 μg / ml. In addition, the EMF of frovatriptan is reached approximately 1 hour 30 after administration of the preparation according to the invention, whereas this concentration is never reached with the commercial formulation.
Tous ces résultats montrent que dans le cas des compositions selon l'invention, les principes actifs sont résorbés plus rapidement par l'organisme et en plus grande quantité. En effet, la résorption des principes actifs est franchement facilitée par les compositions selon l'invention et les concentrations Cmax obtenues avec les compositions selon l'invention bien plus élevées que les C'max obtenues avec les produits similaires du commerce.All these results show that in the case of the compositions according to the invention, the active ingredients are reabsorbed more quickly by the body and in greater quantities. Indeed, the resorption of the active ingredients is frankly facilitated by the compositions according to the invention and the Cmax concentrations obtained with the compositions according to the invention much higher than the C'max obtained with the similar products of commerce.
De plus, dans le cas de l' indométacine, du sumatriptan et du frovatriptan, les CEM ne sont jamais atteintes avec les compositions commerciales. Or dans le cas des compositions selon l'invention, les CEM sont atteintes pour chacun des principes actifs présentés dans ces exemples. De plus, ces concentrations sont atteintes au maximum environ 3 heures après l'administration des compositions selon l'invention. Ainsi, les compositions selon l'invention permettent non seulement une résorption plus rapide mais également d' atteindre les concentrations d' efficacités en peu de temps dans les cas où ces concentrations ne sont pas atteintes avec les compositions du commerce. In addition, in the case of indomethacin, sumatriptan and frovatriptan, EMFs are never achieved with the commercial compositions. However, in the case of the compositions according to the invention, the EMFs are reached for each of the active ingredients presented in these examples. In addition, these concentrations are reached at most about 3 hours after administration of the compositions according to the invention. Thus, the compositions according to the invention allow not only a faster resorption but also to reach the concentrations of efficiencies in a short time in cases where these concentrations are not reached with the commercial compositions.

Claims

REVENDICATIONS
1. Procédé de production de formes pharmaceutiques sèches hydrodispersibles, caractérisé en ce qu'on disperse un ou plusieurs principes actifs dans un ester d'acide gras de polyoxyéthylène 32, facilement fusible puis on pulvérise à chaud la dite dispersion sur un excipient granulaire en lit fluidisé et on distribue le mélange pulvérulent ainsi formé dans des compositions pharmaceutiques après dilution éventuelle par un excipient inerte non toxique pharmaceutiquement acceptable.1. Process for producing water-soluble dry dosage forms, characterized in that one or more active ingredients are dispersed in a polyoxyethylene fatty acid ester 32, easily fusible, and then said dispersion is heated to a granular excipient in a bed. fluidized and distributes the powder mixture thus formed in pharmaceutical compositions after optional dilution with a pharmaceutically acceptable inert non-toxic excipient.
2. Procédé selon la revendication 1 dans lequel l'ester d'acide gras de polyoxyéthylène 32 est le distéarate de polyoxyéthylène 32.The process of Claim 1 wherein the polyoxyethylene 32 fatty acid ester is polyoxyethylene distearate 32.
3. Procédé selon la revendication 1 ou 2 dans lequel l'ester d'acide gras de polyoxyéthylène 32 fond en dessous de 80° C.The process of claim 1 or 2 wherein the polyoxyethylene fatty acid ester 32 melts below 80 ° C.
4. Procédé selon l'une des revendications précédentes dans lequel l'ester d'acide gras de polyoxyéthylène 32 est un distéarate de polyoxyéthylène 32 dont la fusion s'effectue aux environs de 50 à 600C.4. Method according to one of the preceding claims wherein the fatty acid ester of polyoxyethylene 32 is a polyoxyethylene distearate 32 whose melting is carried out at about 50 to 60 ° C.
5. Procédé selon l'une des revendications précédentes dans lequel l'excipient granulaire est un matériau inerte.5. Method according to one of the preceding claims wherein the granular excipient is an inert material.
6. Procédé selon la revendication 5 dans lequel l'excipient granulaire est la cellulose micro cristalline.The method of claim 5 wherein the granular excipient is microcrystalline cellulose.
7. Procédé selon l'une des revendications précédentes dans lequel la concentration du ou des principes actifs dans l'ester d'acide gras de polyoxyéthylène 32, s'échelonne de 30 à 50 %.7. Method according to one of the preceding claims wherein the concentration of active ingredient (s) in the polyoxyethylene fatty acid ester 32, ranges from 30 to 50%.
8. Procédé selon l'une des revendications précédentes dans lequel la quantité de matériau granulaire par prise unitaire est calculée pour que la concentration en fraction active soit de l'ordre de 50 %.8. Method according to one of the preceding claims wherein the amount of granular material per unit dose is calculated so that the concentration of active fraction is of the order of 50%.
9. Procédé selon l'une des revendications précédentes dans lequel le principe actif ou le mélange de principes actifs dispersé sur le support inerte, est (sont) mélangé (s) avec un ou plusieurs excipients inertes, non-toxiques pharmaceutiquement acceptables en vue de réaliser des compositions pharmaceutiques. 9. Method according to one of the preceding claims wherein the active ingredient or mixture of active ingredients dispersed on the inert support, is (are) mixed with one or more inert excipients, non-toxic pharmaceutically acceptable for the purpose of to produce pharmaceutical compositions.
10. Procédé selon l'une des revendications précédentes dans lequel le principe actif est le fénofibrate dissous dans le distéarate de polyoxyéthylène 32 puis dispersé sur un support à base de cellulose micro cristalline.10. Method according to one of the preceding claims wherein the active ingredient is fenofibrate dissolved in polyoxyethylene distearate 32 and then dispersed on a support based on microcrystalline cellulose.
11. Procédé selon l'une des revendications 1 à 9 dans lequel le principe actif est la progestérone dissoute dans le distéarate de polyoxyéthylène 32 puis dispersée sur un support à base de cellulose micro cristalline.11. Method according to one of claims 1 to 9 wherein the active ingredient is progesterone dissolved in polyoxyethylene distearate 32 and then dispersed on a support based on microcrystalline cellulose.
12. Procédé selon l'une des revendications 1 à 9 dans lequel le principe actif une statine dissoute dans le stéarate de polyoxyéthylène 32, puis dispersée sur un support à base de cellulose micro cristalline.12. Method according to one of claims 1 to 9 wherein the active ingredient a statin dissolved in polyoxyethylene stearate 32, and then dispersed on a support based on microcrystalline cellulose.
13. Procédé selon l'une des revendications 1 à 9 dans lequel le principe actif est le paracétamol dissous dans le distéarate de polyoxyéthylène 32 puis dispersée sur un support à base de cellulose micro cristalline.13. Method according to one of claims 1 to 9 wherein the active ingredient is paracetamol dissolved in polyoxyethylene distearate 32 and then dispersed on a support based on microcrystalline cellulose.
14. Procédé selon l'une des revendications 1 à 9 dans lequel le principe actif est un produit antimigraineux comme un triptan dissous dans le distéarate de polyoxyéthylène 32 puis dispersée sur un support à base de cellulose micro cristalline .14. Method according to one of claims 1 to 9 wherein the active ingredient is an antimigraine product such as a triptan dissolved in polyoxyethylene distearate 32 and then dispersed on a support based on microcrystalline cellulose.
15. Procédé selon l'une des revendications 1 à 9 dans lequel la forme hydrodispersible est une solution d'Amiodarone dans le distéarate de polyoxyéthylène 32 puis dispersée sur un support à base de cellulose micro cristalline .15. Method according to one of claims 1 to 9 wherein the water-dispersible form is a solution of Amiodarone in polyoxyethylene distearate 32 and then dispersed on a support based on micro-crystalline cellulose.
16. Procédé selon l'une des revendications 1 à 9 dans lequel le principe actif est la buprénorphine ou un de ses sels dissous dans le distéarate de polyoxyéthylène 32 puis dispersée sur un support à base de cellulose micro cristalline .16. Method according to one of claims 1 to 9 wherein the active ingredient is buprenorphine or a salt thereof dissolved in polyoxyethylene distearate 32 and then dispersed on a support based on microcrystalline cellulose.
17. Procédé de production de formes pharmaceutiques selon l'une des revendications précédentes dans lequel on réalise les formes sublinguales ou des comprimés buccaux.17. Process for producing pharmaceutical forms according to one of the preceding claims, in which the sublingual forms or oral tablets are produced.
18. Compositions pharmaceutiques telles qu'elles sont obtenues par le procédé selon l'une quelconque des revendications précédentes. 18. Pharmaceutical compositions as obtained by the process according to any one of the preceding claims.
EP08827662A 2007-07-06 2008-07-07 Novel method for producing dry hydrodispersible pharmaceutical forms Withdrawn EP2192894A2 (en)

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FR0704874A FR2918277B1 (en) 2007-07-06 2007-07-06 NOVEL PROCESS FOR THE PRODUCTION OF HYDRODISPERSIBLE DRY PHARMACEUTICAL FORMS AND THE HYDRODISPERSIBLE COMPOSITIONS THUS OBTAINED
PCT/FR2008/000973 WO2009024686A2 (en) 2007-07-06 2008-07-07 Novel method for producing dry hydrodispersible pharmaceutical forms

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BRPI0814027A2 (en) 2015-02-03
KR20100038188A (en) 2010-04-13

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