Patent Application
20120093903
The present invention is concerned with a powdery or granulated composition comprising a copolymer, a salt of a fatty monocarboxylic acid and/or a fatty monocarboxylic acid and/or a fatty alcohol as ready to use aqueous dispersion for the coating or binding of active ingredients in the field of pharmacy, nutraceuticals or cosmetics.
WO02067906A1 (US20030064036A1) describes a coating and binding agent with improved storage stability, consisting essentially of
One of the beneficial effects of the invention is that the vapour permeability is reduced. Compound (a) is preferably EUDRAGIT® EPO. A preferred compound (b) in the examples is Sodium-Laurylsulfate, which can be used together with lauric acid, stearic acid or lauryl alcohol as compound (c). Dispersion processing times of the inventive examples are around 3 to 6 hours.
There is a permanent need for improved coating and binding agents for pharmaceutically, nutraceutically or cosmetically purposes. Customers prefer ready to use powdery or granulated compositions comprising suitable copolymers which can be used for coating or binding processes after dispersing them in water.
General problems are that additives like emulsifiers must be added to the copolymers to be used for coating or binding processes in order to allow a rapid dispersion times. However additives which allow rapid dispersion times may on the other hand sometimes effect the viscosity of the dispersion in negative way or increase the water vapor permeability. Especially if the viscosity of the dispersion is too high this may lead to problems in the subsequently coating or binding process.
Furthermore some frequently used additives like for instance sodium laurylsulfate (s. WO02067906A1) although in general suitable and accepted for pharmaceutical purposes, are in the meantime regarded as showing a too high level of toxicity. This may depend on the total amount of the polymer and additive composition that is present in a daily dosage of the intended pharmaceutical, nutraceutical or cosmetical form. However in general additives with a toxicity as low as possible are of course preferred.
Thus it is one object of the present invention to provide powdery or granulated compositions for coating or binding purposes that get completely dispersed in water with a processing time as short as possible. The additives employed to support the rapid dispersion time shall show a toxicity level as low as possible. Furthermore the viscosity of the dispersion must be in a range which allows subsequently successful coating or binding procedures.
The problem is solved by a powdery or granulated composition comprising at least by 30% by weight of a mixture of
The inventive composition is intended to be used as a rapidly in water dissolving powder or granulate. The dispersed aqueous compositions show a low viscosity and can therefore be processed directly as coating and binding agents for pharmaceutically, nutraceutically or cosmetically purposes. Preferred embodiments can be prepared as dispersions with dry weight contents of up to 30% (weight/volume). The main components (a), (b) and (c) preferably show extremely low toxicity data in the range 2000 mg/kg LD50 (rat) or even less toxic.
Component (a)
Component (a) is a copolymer composed of polymerized units of C1- to C4-alkyl esters of acrylic or methacrylic acid and of alkyl(meth)acrylate monomers with a tertiary amino group in the alkyl radical.
Amino Methacrylat Copolymer
The copolymer component (a) may be a so called “amino methacrylate copolymer (USP/NF)”, “basic butylated methacrylate copolymer (Ph. Eur)” or “aminoalkyl Methacrylate Copolymer E (JPE)” which are of the EUDRAGIT® E type. Suitable EUDRAGIT® E type copolymers are known, for example, from EP 0 058 765 B1.
The amino (meth)acrylate copolymer may be composed, for example, of 30 to 80% by weight of free-radically polymerized C1- to C4-alkyl esters of acrylic acid or of methacrylic acid, and 70 to 20% by weight of (meth)acrylate monomers having a tertiary amino group in the alkyl radical.
Suitable monomers with functional tertiary amino groups are detailed in U.S. Pat. No. 4,705,695, column 3 line 64 to column 4 line 13. Mention should be made in particular of dimethylaminoethyl acrylate, 2-dimethylaminopropyl acrylate, dimethylaminopropyl methacrylate, dimethylaminobenzyl acrylate, dimethylaminobenzyl methacrylate, (3-dimethylamino-2,2-dimethyl)propyl acrylate, dimethylamino-2,2-dimethyl)propyl methacrylate, (3-diethylamino-2,2-dimethyl)propyl acrylate, diethylamino-2,2-dimethyl)propyl methacrylate and diethylaminoethyl methacrylate. Particular preference is given to dimethylaminoethyl methacrylate.
The content of the monomers with tertiary amino groups in the copolymer may advantageously be between 20 and 70% by weight, preferably between 40 and 60% by weight. The proportion of the C1- to C4-alkyl esters of acrylic acid or methacrylic acid is 70-30% by weight. Mention should be made of methyl methacrylate, ethyl methacrylate, butyl methacrylate, methyl acrylate, ethyl acrylate and butyl acrylate.
A suitable amino (meth)acrylate copolymer may be polymerized out of, for example, from 20-30% by weight of methyl methacrylate, 20-30% by weight of butyl methacrylate and 60-40% by weight of dimethylaminoethyl methacrylate.
A specifically suitable commercial amino (meth)acrylate copolymer is, for example, formed from 25% by weight of methyl methacrylate, 25% by weight of butyl methacrylate and 50% by weight of dimethylaminoethyl methacrylate (EUDRAGIT® E100 or EUDRAGIT® E PO (powder form)). EUDRAGIT® E100 and EUDRAGIT® E PO are water-soluble below approx. pH 5.0 and are thus also gastric juice-soluble.
Component (b)
Component (b) is a, one or more, salt of a fatty monocarboxylic acid having 10 to 18 carbon atoms. Suitable amounts are 5 to 28, preferably 5 to 25, preferably 5 to 20, preferably 5 to15 or preferred 8 to 12% by weight based on the copolymer component (a). As a rule the salt of a fatty monocarboxylic acid having 10 to 18 carbon atoms is water soluble or water dispersible.
In relation to the cationic groups in the polymer component (a) the component (b) may be present in a molar ratio of 5 to 35, preferably 5 to 25 or preferably 12-25 mol-%.
In a further preferred embodiment of the present invention the salt in respect to component (b) is selected from the group consisting of alkali metal salt or an ammonium salt.
In a particularly preferred embodiment of the present invention, the salt in respect to component (b) is a salt of a saturated, preferably unbranched, preferably unsubstituted, mono carboxylic acid (fatty acid) having 10 to 18, preferably 10 to 14 or 16 to 18 carbon atoms which may be selected from the group of consisting of the salts of capric acid, lauric acid, myristic acid, palmitic acid, or stearic acid or mixtures thereof. Even more preferred is an alkali metal salt or ammonium salt thereof. Even further preferred is a salt of capric acid, particularly preferred is sodium capric acid=sodium caprate (C9H19COO−Na+),
The salts of the following saturated monocarbonic acids are suitable for the purposes of the invention:
Salts of organic or anorganic acids other than salts of mono carboxylic acids (fatty acids) having 10 to 18 carbon atoms are assumed to be not suitable for the purposes the present invention.
Saturated, mono carboxylic acids (fatty acids) having 10 to 18 carbon atoms are not suitable for the purposes of the invention as long as they are not applied together with an alkali metal or an ammonium hydroxide to react in situ to the salt form.
The salt of a saturated, preferably unbranched, mono carboxylic acid (fatty acid) having 10 to 18, preferably 10 to 14 or 16 to 18 carbon atoms is preferably unsubstituted.
It is understood that all the salts of a saturated, preferably unbranched, preferably unsubstituted, mono carboxylic acid (fatty acid) having 10 to 18, preferably 10 to 14 or 16 to 18 carbon atoms which are suitable in the sense of the present invention should be acceptable as a pharmaceutical or nutraceutical ingredient.
A salt of a fatty monocarboxylic acid having 10 to 18 carbon atoms may also be generated by adding the corresponding acid as component (c) and base, for instance sodium hydroxid (NaOH) or potassium hydroxid (KOH). This results in a balance between the acid of the fatty monocarboxylic acid (component (c)) and the corresponding salt (component (b)) by in situ salt formation. The amount of base needed can be determined by calculation of the degree of molar neutralisation.
Component (c)
Component (c) is a, one or more, fatty monocarboxylic acid having 8 to 18 carbon atoms and/or a, one or more, fatty alcohol having 8 to 18 carbon atoms. Suitable amounts are 10 to 30, preferably 10 to 28, preferably 10 to 20 or preferred 12 to 18% by weight based on the copolymer component (a).
In relation to the cationic groups in the polymer component (a) the component (c) may be present in a molar ratio of 10 to 50, preferably 15-40 mol-%.
Fatty Monocarboxylic Acid Having 8 to 18 Carbon Atoms
the following monocarbonic acids are suitable for the purposes of the invention:
Saturated, preferably unbranched, mono carboxylic acid (fatty acid) having 8 to 18, preferably 8 or 10 or 16 or 18 carbon atoms are preferably unsubstituted. Preferred are capric acid (C9H19COOH) or stearic acid (C17H35COOH) as single components (c) or mixtures thereof, most preferred in combination with sodium caprate (C9H19COONa) as component (b)
Fatty Alcohol Having 8 to 18 Carbon Atoms
The following C8-C18 fatty alcohols are suitable for the purposes of the invention:
Preferred are C8-C10 fatty alcohols. Most preferred is capryl alcohol (1-octanol) and dodecanol.
Pharmaceutical, Nutraceutical or Cosmetical Excipients
The compositions according to the invention are further characterised in that up to 200%, up to 70%, up to 60%, up to 50%, up to 40%, up to 30%, up to 20% or up to 10% by weight based on the total weight of the components (a), (b) and (c) of pharmaceutical, nutraceutical or cosmetical excipients which are different from the components (a), (b) and (c) may be contained. However the composition according to the invention may as well contain any or essentially any pharmaceutical, nutraceutical or cosmetical excipients. Thus the composition may essentially consist or consist to 100% of the components (a), (b) and (c).
The term pharmaceutical, nutraceutical or cosmetical excipients is well known to the skilled person. Such excipients are customary in pharmacy but also in the field of nutraceuticals or cosmetics, occasionally also they are referred as customary additives. It is, of course, always necessary for all the excipients or customary additives employed to be toxicologically acceptable and usable in particular in food or in medicaments without a risk for customers or patients.
Although the requirements are usually higher in the pharmaceutical field there is a widely overlap of excipients used for pharmaceutical purposes and those used for nutraceutical purposes. Usually all pharmaceutical excipients may be used for nutraceutical purposes and at least a large number of nutraceutical excipients are allowed to be used for pharmaceutical purposes as well. Excipients may be are added to the formulation of the invention, preferably during the mixing of the powders production of the granules, for the coating or binding of active ingredients, coating of solids or patches or dispersing semi solids.
Pharmaceutical, nutraceutical or cosmetical excipients with are different from the components (a), (b) and (c) may be contained for practical reasons, for instance to avoid stickiness or to add a colour. However these excipients usually do not contribute or do show any or almost no effect on the invention itself as claimed here.
Pharmaceutical, nutraceutical or cosmetical excipients with are different from the components (a), (b) and (c) do not contribute to the invention in a narrow sense which is based on the interaction of the components (a), (b) and (c). Pharmaceutical, nutraceutical or cosmetical excipients with are different from the components (a), (b) and (c) and which may have an essential adverse effect on the major beneficial effects of the present invention e.g. the preparation time or on the viscosity of the dispersion should be avoided and can be excluded. For instance the addition of essential amounts sodium dodecylsulfate or similar substances with emulgator properties different from the components (b) and (c) should be avoided. Preferably any addition of sodium dodecylsulfate or similar substances with emulgator properties different from the components (b) and (c) should be avoided.
Typical pharmaceutical, nutraceutical or cosmetical excipients with are different from the components (a), (b) and (c) are familiar to those skilled in the art. Examples are antioxidants, brighteners, flavouring agents, flow aids, fragrances, glidants (release agents), penetration-promoting agents, pigments, plasticizers, polymers, pore-forming agents or stabilizers. They may be used as processing adjuvants and are intended to ensure a reliable and reproducible preparation process as well as good long-term storage stability, or they achieve additional advantageous properties in the pharmaceutical form. They are added to the polymer formulations before processing and can influence the permeability of the coatings. This property can be used if necessary as an additional control parameter.
Anionic polymers or anionic (meth)acrylate copolymers which could interact with the polymer component (a) may be excluded. Dicarboxylic acids having 3 to 10 carbon atoms may be excluded as well.
Plasticizers
Plasticizers achieve through physical interaction with a polymer a reduction in the glass transition temperature and promote film formation, depending on the added amount. Suitable substances usually have a molecular weight of between 100 and 20 000 and comprise one or more hydrophilic groups in the molecule, e.g. hydroxyl, ester or amino groups.
Examples of suitable plasticizers are alkyl citrates, glycerol esters, alkyl phthalates, alkyl sebacates, sucrose esters, sorbitan esters, diethyl sebacate, dibutyl sebacate and polyethylene glycols 200 to 12 000. Preferred plasticizers are triethyl citrate (TEC), acetyl triethyl citrate (ATEC), diethyl sebacate and dibutyl sebacate (DBS). Mention should additionally be made of esters which are usually liquid at room temperature, such as citrates, phthalates, sebacates or castor oil. Esters of citric acid and sebacinic acid are preferably used.
Addition of the plasticizers to the formulation can be carried out in a known manner, directly, in aqueous solution or after thermal pre-treatment of the mixture. It is also possible to employ mixtures of plasticizers.
Glidants/Release Agents/Detackifier:
Glidants, release agents or detackifiers usually have lipophilic properties and are usually added to spray suspensions. They prevent agglomeration of cores during film formation. There are preferably used talc, Mg or Ca stearate, ground silica, kaolin or nonionic emulsifiers with an HLB value of between 2 and 8. Standard proportions for use of release agents in the inventive coating and binding agents range between 0.5 and 70 wt % relative to the components (a), (b) and (c).
Pigments:
Only rarely is the pigment added in soluble form. As a rule, aluminium oxide or iron oxide pigments are used in dispersed form. Titanium dioxide is used as a whitening pigment. Standard proportions for use of pigments in the inventive coating and binding agents range between 20 and 200 wt % relative to the components (a), (b) and (c).
Of course all kind of excipients used must of course be toxicologically safe and to be used in nutraceuticals or pharmaceuticals without risk for customers or patients.
The Preparation Process
Process for preparing a composition according to the invention may be characterized in that the components (a), (b) and (c) are intermixed with each other by powder mixture, dry granulation, wet granulation, melt granulation, spray drying or freeze drying.
Components (a), (b) and (c) may be intermixed with each other in a powdery stage or by a granulations process, which can be a dry, a wet or melt granulation process. As an alternative, the components can be added subsequently in the aqueous dispersing phase
Powder Mixture Process
Components (a), (b) and (c) are intermixed with each other in a powdery stage by using mixer equipment. Powdery stage can be defined in that the particle of components may have an average particle size of less than 1 mm, preferably of less than 0.5 mm, especially of 100 μm or less, preferably in the range 10 to 100 μm. The process of powder mixing is well known to a skilled person. The average particle size may be determined by sieving techniques or by laser diffraction methods.
Dry Granulation Process
Components (a), (b) and (c) are intermixed with each other in a form of granulates by using a mixer equipment. Granulates may have an average particle size of 1 mm or more, preferably in the range of 1 to 5 mm.
Wet Granulation Process
Powders or granules of components (a), (b) and (c) are intermixed with each other in a wet stage by wetting the powders or granulates with water or organic solvents and then using a mixer or kneading equipment. Wet stage shall mean that there is a wet mass than can be manually kneaded with a water content for instance in the range 10 to 100% by weight. After wetting and mixing respectively kneading the wet mass is dried and then again commuted to granules or powders. The process of wet granulation is well known to a skilled person. Solutions of the components (a), (b) or (c) or combinations thereof in organic solvents like methanol, ethanol, isopropanol, ethyl acetate or acetone may also be used in the wet granulation process. The organic solvents may optionally contain up to 50% (v/v) of water.
Melt Granulation Process
Powders or granules of components (a), (b) and (c) are intermixed with each other usually without the addition of solvents at elevated temperatures where at least the copolymer is in a molten stage. This can be performed in a heated mixer or in an extruder, preferably in a twin screw extruder. After mixing the molten mass is cooled and then again commuted to granules or to powders. The process of melt granulation is well known to a skilled person.
Spray Drying or Freeze Drying Process
Components (a), (b) and (c) are dissolved or dispersed in water or in organic solvents or mixtures of water with organic solvents, separately or as premix and subsequently dried and probably sieved. The compounds may have an average particle size in the range of 10 μm to 2 mm or more, preferably in the range of 20 μm to 1.5 mm.
Dispersion or Solution Process
The components (a), (b) and (c) are added to the aqueous dispersing or solution agent, preferably purified water, as powder mixtures, granules or single one after another while gentle stirring with a conventional stirrer at room temperature. Advantageously, according to this invention, the need of a high shear mixer or specific disperser will not be necessary. Additionally, the heating of the suspension will be not necessary. After stirring of less than 3 hours dispersions or solutions are formed being able to be sprayed in coating or granulation processes and/or to form films after drying. The dispersion or solution may have a total content of solids less than 35% by weight, preferably less than 25% by weight and pH-values between 7 and 11. The pH values of the dispersion or solution may in the range from 8 to 10, preferably from 9 to 10.
Dispersion Preparation Time
The dispersion preparation time can for instance be observed and determined by polarization microscopy. The time when the dry powdery or granulate mixture is stirred into the water is defined as starting point. The dispersing aqueous mixture is further stirred at room temperature (ca. 22° C.). At the beginning there is a turbid dispersion, that becomes first white and then more and more clear during stirring. Drops of the dispersing aqueous mixture are then taken every 10 minutes and observed under a polarization microscope with a magnification of 100-fold with the support of a phase filter. The time point when no or almost no particles (at least less than ten particles in the view field) are observed in the fluid of such a drop under the microscope is taken as end point of the dispersion process. The accuracy of this determination method is in most cases sufficient to differ the preparation times of the different dispersion preparations apart from each other. The inventive composition may be characterized by a dispersion or solution preparation time of less than 3 hours, preferably 2.5 hours or less most preferred 1.5 hours or less. The preparation time is starting from adding the dry powdery or granulate mixture into water at room temperature, further stirring and thereby dissolving the components to end up at a clear solution or dispersion respectively.
Practical Applications:
Dispersions according to this invention may be used in granulation or coating process in the development and manufacturing of nutrition supplements, nutraceuticals, cosmetics, cosmeceuticals, pharmaceutical intermediates or pharmaceuticals. Due to the physicochemical properties of the polymer, which are maintained in the dispersed compounds of this invention, functions such as coloring, taste masking, moisture protection, light protection, odor masking or eased swelling are introduced into the final dosage form.
Application procedures and processes known to the skilled person and published for example in:
G. Cole, J. Hogan, M. Aulton, Pharmaceutical coating Technology Taylor & Francis, 1995
K. H. Bauer, K. Lehmann, H. P. Osterwald, G. Rothgang, “Coated Dosage Forms”, CRC Press 1998
Pharmaceutical Manufacturing Encyclopedia, William Andrew Publishing; Third Edition, 2005
Encyclopedia of Pharmaceutical Technology, Third Edition, Informa Healthcare, 2006
J. W. McGinity, L. A. Felton, aqueous Polymeric Coatings for Pharmaceutical Dosage Forms, Third Edition, Informa Healthcare, 2008
Nutraceuticals
Nutraceuticals can be defined as extracts of foods claimed to have medical effects on human health. The nutraceutical is usual contained in a medical format such as capsule, tablet or powder in a prescribed dose. Examples for nutraceuticals are resveratrol from grape products as an antioxidant, soluble dietary fiber products, such as psyllium seed husk for reducing hypercholesterolemia, broccoli (sulphane) as a cancer preservative, and soy or clover (isoflavonoids) to improve arterial health.
Other nutraceuticals examples are flavonoids, antioxidants, alpha-linoleic acid from flax seed, beta-carotene from marigold petals or antocyanins from berries. Sometimes the expression neutraceuticals is used as synonym for nutraceuticals.
Cosmetics
Cosmetics are substances used to enhance or protect the appearance or odor of the human body. Typical cosmetical active ingredients may comprise vitamins, phytochemicals, enzymes, antioxidants, and essential oils. Cosmetics may include skin-care creams, lotions, powders, perfumes, lipsticks, fingernail and toe nail polish, eye and facial makeup, permanent waves, colored contact lenses, hair colors, hair sprays and gels, deodorants, baby products, bath oils, bubble baths, bath salts, butters and many other types of products. Their use is widespread, especially among women but also by men. A subset of cosmetics is called “make-up,” which refers primarily to colored products intended to alter the user's appearance. Many manufacturers distinguish between decorative cosmetics and care cosmetics. The term cosmetics shall include topically applied forms such as so called cosmeceuticals as well as orally ingested forms such as so called nutricosmetics.
Active Ingredients
The inventive composition may be used as a coating and binding agent in combination with all kinds of pharmaceutical, nutraceutical or cosmeceutical active ingredients. However additionally beneficial effects may be gained in combination with those kinds of active ingredients, which need to be formulated in a taste masked form or in a moisture resistant form.
Pharmaceutically, nutraceutically or cosmetically active ingredients have in common that they are active ingredients which have a positive effect on the health of an organism, e.g the human health. They have also in common that their formulations are often the same or very similar. Often also the same kind of excipients or additives are used in combination with these kind of active ingredients. Pharmaceutically active ingredients are used to cure diseases and effect the health of an organism, e.g the human health more or less directly. Nutraceutical active ingredients are used to supplement the nutrition and thus support the health of an organism, e.g the human or animal health indirectly. Cosmetically active ingredients are meant to support the human health indirectly for instance by balancing the water content of the human skin.
Process
The invention also relates to a process for preparing the inventive composition, characterized in that the components (a), (b) and (c) are intermixed with each other by powder mixture, dry granulation, wet granulation or melt granulation. In the case of wet granulation and the components (a), (b) or (c) or combinations thereof may be used in the form an organic solution.
Use
The invention discloses the use of the composition as a coating or binding agent for the spray coating or binding of pharmaceutical, nutraceutical or cosmetical compositions. Preferred active ingredient containing compositions may be in the form of powders, pellets, granules, minitablets, sachets, dry syrups, tablets or capsules or nutraceutical compositions or cosmetical compositions. The use as a coating solution shall include the use as a subcoat or a topcoat in combination with other coatings.
The following copolymers were used in the Examples.
Copolymer:
BASIC BUTYLATED METHACRYLATED COPOLYMER EUDRAGIT® E PO or EUDRAGIT® E 100.
EUDRAGIT® E is a copolymer composed of 25% by weight of methyl methacrylate, 25% by weight of butyl methacrylate and 50% by weight of dimethylaminoethyl methacrylate.
Model Drug
Studies were conducted using tablets (300 mg) with quinidine sulphate (immediate bitter taste) or silicagel (550 mg total weight, 11 mm diameter) as marker.
Excipients
All excipients were used in pharmaceutical quality
Disintegration Studies:
Disintegration was tested according USP 28 <701> Disintegration
Dissolution Studies
Coated tablets were tested according to USP 28-NF23, General Chapter <711>, Dissolution,
Dissolution Parameters:
Apparatus: USP Type-II (Paddle)
RPM: 50/min.
Temperature: 37.5±0.5° C.
Dissolution volume: 900 ml.
Wavelength: 250 nm
Dissolution Medium 1:
0.1 molar Hydrochloric acid (HCl), (European Pharmacopoeia=EP)
Dissolution Medium 2:
Phosphate buffer pH 6.0 (European Pharmacopoeia=EP)
Results
The following tables explain formulation examples 1-25 according to the invention as well as non inventive comparative examples:
Dispersion are prepared by adding the component (b), (a) and (c) in this order separately or as a granulated or blended premixture of all components in purified water in a quantity, providing the specified dry solid content. Stirring was performed with a magnetic stirrer or a simple agitator providing low shear forces.
In examples 23, 24 and 25 organic solvents are used for granulation. EUDRAGIT® E 100 was dissolved in isopropanol (95% w/w) to form a 15% (w/w) solution while gentle stirring. The components (b) and (c) were added subsequently and stirred until complete dissolution. In case a glidant was used too, it was added to the clear solution and shortly stirred to get a homogeneous suspension. The final suspension was dried completely in a vacuum oven at 50° C. for 24 h. The dried film was milled to get a powder of ca 0.5 mm particle diameter. The powder was tested accordingly to examples 1 to 22.
Coating Suspension Preparation:
A coating composition was prepared mixing the formulation of example 1 with talc (50% w/w ref. to polymer) and dispersing the powder compound in purified water by gentle stirring. The coating suspension had a content of dry solid of 18% w/w. Stirring is continued through the entire coating process.
Coating Process:
1800 g Quinidine sulphate tablets were loaded in a side vented coating pan Hi Coater LHC 30, Loedige) and coated with the coating suspension under appropriate conditions, i.e. a spray rate of approximately 7 g/min coating suspension per kg cores and a bed temperature of approximately 30-35° C. Dry polymer weight gain was adjusted to 2 mg/cm2 tablet surface. After coating the tablets were dried in the coater for 5 min at 45° C. and for 2 hours on trays on an oven at 40° C.
Results:
All tablets provided neutral taste over more than 10 minutes.
Coating Suspension Preparation:
A coating composition was prepared mixing the formulation of example 1 with talc (50% w/w ref. to polymer) and dispersing the powder compound in purified water by gentle stirring. The coating suspension had a content of dry solid of 18% w/w. Stirring is continued through the entire coating process.
Coating Process:
1800 g Quinidine sulphate tablets were loaded in a side vented coating pan Hi Coater LHC 30, Loedige) and coated with the coating suspension under appropriate conditions, i.e. a spray rate of approximately 7 g/min coating suspension per kg cores and a bed temperature of approximately 30-35 ° C. Dry polymer weight gain was adjusted to 10 mg/cm2 tablet surface. After coating the tablets were dried in the coater for 5 min at 45° C. and for 2 hours on trays on an oven at 40° C.
Results:
All tablets were tested for drug release in dissolution medium 1 and 2 and provided more than 90% drug release in 15 min in both media. The same tablets tested in purified water provided a drug release of less than 5% after 60 min.
Coating Suspension Preparation:
A coating composition was prepared mixing the formulation of example 11 with talc (100% w/w ref. to polymer) and dispersing the powder compound in purified water by gentle stirring. The coating suspension had a content of dry solid of 18% w/w. Stirring is continued through the entire coating process.
Coating Process:
1800 g Quinidine sulphate tablets were loaded in a side vented coating pan Hi Coater LHC 30, Loedige) and coated with the coating suspension under appropriate conditions, i.e. a spray rate of approximately 7 g/min coating suspension per kg cores and a bed temperature of approximately 30-35° C. Dry polymer weight gain was adjusted to 2 mg/cm2 tablet surface. After coating the tablets were dried in the coater for 5 min at 45° C. and for 2 hours on trays on an oven at 40° C.
Results:
All tablets provided an neutral taste over more than 10 minutes.
Coating Suspension Preparation:
A coating composition was prepared mixing the formulation of example 11 with talc (100% w/w ref. to polymer) and dispersing the powder compound in purified water by gentle stirring. The coating suspension had a content of dry solid of 18% w/w. Stirring is continued through the entire coating process.
Coating Process:
1800 g Quinidine sulphate tablets were loaded in a side vented coating pan Hi Coater LHC 30, Loedige) and coated with the coating suspension under appropriate conditions, i.e. a spray rate of approximately 7 g/min coating suspension per kg cores and a bed temperature of approximately 30-35° C. Dry polymer weight gain was adjusted to 10 mg/cm2 tablet surface. After coating the tablets were dried in the coater for 5 min at 45° C. and for 2 hours on trays on an oven at 40° C.
Results:
All tablets disintegrated in medium 1 in 2-5 min and in purified water in 30-60 min All tablets were tested in dissolution medium 1 and 2 and provided more than 90% drug release in 15 min. The same tablets tested in purified water provided a drug release of less than 5% after 60 min.
Coating Suspension Preparation:
A coating composition was prepared mixing the formulation of example 1 with talc (50% w/w ref. to polymer) and dispersing the powder compound in purified water by gentle stirring. The coating suspension had a content of dry solid of 18% w/w. Stirring is continued through the entire coating process.
Coating Process:
1800 g Silicagel tablets sulphate tablets were loaded in a side vented coating pan Hi Coater LHC 30, Loedige) and coated with the coating suspension under appropriate conditions, i.e. a spray rate of approximately 7 g/min coating suspension per kg cores and a bed temperature of approximately 30-35° C. Dry polymer weight gain was adjusted to 10 mg/cm2 tablet surface. After coating the tablets were dried in the coater for 5 min at 45° C. and for 2 hours on trays on an oven at 40° C.
Results:
Coated and uncoated tablets were stored in open containers at 40° C. and 75% rel. humidity. After 8 hours of testing the moistures uptake of the coated tablets was less than 15% compared to the uncoated tablets set as 100%.
Coating Suspension Preparation:
A coating composition was prepared mixing the formulation of example 11 with talc (100% w/w ref. to polymer) and dispersing the powder compound in purified water by gentle stirring. The coating suspension had a content of dry solid of 18% w/w. Stirring is continued through the entire coating process.
Coating Process:
1800 g Silicagel tablets sulphate tablets were loaded in a side vented coating pan Hi Coater LHC 30, Loedige) and coated with the coating suspension under appropriate conditions, i.e. a spray rate of approximately 7 g/min coating suspension per kg cores and a bed temperature of approximately 30-35° C. Dray polymer weight gain was adjusted to 10 mg/cm2 tablet surface. After coating the tablets were dried in the coater for 5 min at 50° C. and for 2 hours on trays on an oven at 40° C.
Results:
Coated and uncoated tablets were stored in open containers at 40° C. and 75% rel. humidity. After 8 hours of testing the moistures uptake of the coated tablets was less than 15% compared to the uncoated tablets set as 100%.
| Number | Date | Country | Kind |
|---|---|---|---|
| PCT/EP2009/059861 | Jul 2009 | EP | regional |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP10/53447 | 3/17/2010 | WO | 00 | 12/6/2011 |
