Abstract: The present invention relates to a method for "hot melt coating" of pharmaceutical active ingredients characterized by organoleptic or physicochemical properties that it is desirable to mask. The invention also relates to the resulting medicinal active ingredients with masked organoleptic orphysicochemical properties and the compositions comprising same.
Method for preparing pharmaceutical compositions intended for oral
administration comprising one or more active ingredients and the compositions
comprising same
FIELD OF THE INVENTION
The present invention relates to a method for hot melt coating of pharmaceutical
active ingredients. These active ingredients are characterized by organoleptic or
physicochemical properties that it is desirable to mask. Thus, the pharmaceutical active
ingredients may have unacceptable organoleptic properties (taste, odour, colour,
appearance), in particular their strong bitterness. These pharmaceutical active
ingredients may be sensitive to moisture and/or to temperature. This method therefore
allows effective masking of unsatisfactory organoleptic and/or physicochemical
properties of pharmaceutical active ingredients, without however slowing down the
dissolution of said active ingredient. The invention also relates to the resulting medicinal
active ingredients with masked organoleptic or physicochemical properties and to the
compositions comprising same.
PRIOR ART AND TECHNICAL PROBLEM
In the context of the masking of the taste of active ingredients which have an
unacceptable taste, many tests, using conventional technologies, have been carried out:
granulation, coating in a fluidized air bed, etc. The excipients tested were composed of
polymers: mainly cellulose derivatives (HPC, HPMC, EC) and derivatives of methacrylic
acid (Eudragit range) and of polyvinyl acetate. These tests often came up against
insufficient taste masking.
Moreover, more innovative technologies have also been used, such as
microencapsulation by means of a supercritical C0 2-phase process or by means of a
simple or complex coacervation method. The same masking polymers, mentioned above,
are found, as are other less conventional excipients such as chitosan, alginates or
gelatin. The major drawbacks encountered in these technologies are implementation and
industrial feasibility.
In the same approach, spray-drying and spray-cooling processes have been tested.
The latter "spray-cooling" technology described in WO/2004/058137 consists in
melting a fatty matrix and incorporating the active ingredient therein. The latter is either
dissolved or dispersed in the fatty phase, composed of fatty acids, of a mixture or of
esters of fatty acids, of fatty alcohol or of waxes.
The molten mixture is then conveyed, via a peristaltic pump, to a two-fluid nozzle
where it is atomized into more or less fine droplets (according to the parameters applied).
The droplets are finally cooled by a stream of cold air within the atomization chamber and
converted into solid granules containing the active ingredient dispersed throughout the
fatty matrix.
Although this spray-cooling method makes it possible to obtain pharmaceutical
compositions with correct taste masking while at the same time providing dissolution of
the active ingredient which is not slowed down in an acidic medium, there remains,
however, an unsolved problem of physical heat-stability of the product obtained.
Likewise, this method remains incompatible with active ingredients which are heatsensitive
by nature.
Furthermore, in the context of this "spray-cooling" method, the concentration of the
active ingredient of the composition is limited by the viscosity of the solution or
suspension to be sprayed, which greatly reduces the active ingredient content of the
composition of the coated granule. It is possible to obtain only compositions with low
doses of active ingredient, i.e. compositions comprising an amount of active ingredient
not exceeding 30% by weight in the composition of the coated granule.
Moreover, the use of the hot melt coating method has been described in
WO02/07706. That document describes the use of this technology for coating heatsensitive
active ingredients in the form of solid particles which have not been
pregranulated. The amounts of coating targeted are low and do not make it possible to
satisfactorily mask the taste of very unpleasant active ingredients.
Likewise, W09718798 describes prompt-release pharmaceutical compositions
suitable in particular for oral administration, comprising microcrystals or microgranules of
active agents, a lipid coating obtained by means of a hot melt coating method and a
vehicle comprising excipients. The concentration of fatty matrix of the coating is between
1% and 25%, preferably between 5% and 20%. That document specifies that, in order to
mask the unpleasant taste of an active ingredient while at the same time allowing
satisfactory release of the active agent, it is necessary to work with sufficiently low levels
of fatty matrix. This condition is necessary so as not to modify the dimensions of the
coating layer, which would then influence the release of the active ingredient. However,
the amounts of lipid coating proposed are low and do not make it possible to satisfactorily
mask the taste of very unpleasant active ingredients.
As a result, the use of the hot melt coating method described in these documents is
not suitable for obtaining sufficiently effective masking of the taste and of the odour of an
active ingredient characterized by a strong bitterness and a strong odour, in particular
masking sufficient to allow ingestion of the medicament by a child.
The applicant has now found a novel improved method which makes it possible to
solve these drawbacks.
SUMMARY OF THE INVENTION
The objective of the invention is to propose a novel method which solves at least
the drawbacks mentioned above.
The problem solved by this method of production which comprises formulation
using fatty matrices, is that of the masking of the taste of certain active ingredients while
at the same time obtaining a relatively rapid release of the active ingredient in vitro (for
example a minimum release of 70% of active ingredient in 60 minutes).
Furthermore, the maximum concentration of active ingredient that can be used in
this method is not limited; the resulting product can contain a high dose, i.e. it is possible
to obtain compositions that can comprise an amount of active ingredient exceeding 30%
by weight in the composition of the coated granule. This makes it possible to notably
reduce the doses of products to be administered to the patient, in particular to young
children or to the elderly.
According to an additional advantage, this method makes it possible to obtain a
high dosage of the active ingredient even when the latter is heat-sensitive. Furthermore, it
is observed that the final products obtained exhibit satsifactory physical stability, in
particular under storage conditions subjected to heat (at 30°C/65% RH).
Moreover and surprisingly, this method makes it possible to provide certain
sensitive active ingredients with protection against moisture. This is because the
presence of this lipid coating appears to make it possible to establish a barrier against
moisture.
According to another additional advantage, this method makes it possible, by virtue
of the quality of the coating, to inhibit the anaesthetic and unpleasant effect of certain
active molecules generally felt in the oral cavity.
The invention therefore proposes a method for preparing a composition of
medicinal active ingredient comprising (a) a granular centre consisting of grains of active
ingredient, agglomerated in the presence of binder, and (b) a layer of coating of said
granular centre consisting of fatty matrix, in which composition:
the active ingredient represents a minimum of 10%, preferably 20% or else
30% by weight, relative to the weight of the composition of the coated granule; the
active ingredient represents a maximum of 48%, preferably a maximum of 40%, the
active ingredient preferably represents from 20% to less than 40%, relative to the
weight of the composition of the coated granule, more preferentially the active
ingredient represents from 30% to 40%, relative to the weight of the composition of
the coated granule;
· the fatty matrix represents more than 50% and up to 85% by weight of the
composition of the coated granule, preferably from 51% to 65%, the fatty matrix
optionally comprising an adjuvant, preferably chosen from hydrophilic agents,
surfactants or mixtures thereof, and the latter representing less than 10%, preferably
from 1% to 3% by weight, relative to the weight of the composition of the coated
granule;
the binder, preferably a hydrophilic agent chosen from hydrophilic polymers or
hot-melt agents, represents from 0.2% to 18% by weight, relative to the weight of the
composition of the coated granule, preferably the binder represents less than 18% by
weight for a hot-melt agent or else preferably the binder represents less than 10% by
weight for a hydrophilic polymer;
the diluent, if necessary, as filler, represents a content of 0 to 39%, relative to
the weight of the composition of the coated granule;
the lubricant, if necessary, as flow agent, represents a content of 0 to 1.8%,
relative to the weight of the composition of the coated granule;
the method comprising the steps of:
E 1) preparing the granular centre by spraying an aqueous solution comprising
the binder or by spraying the binder in the molten state onto the active
ingredient alone or as a mixture with a diluent and/or a lubricant;
E2) coating by spraying, onto the granules, said fatty matrix pre-melted in a
melting kettle at a temperature approximately 10 to 20°C above its melting
point;
E3) cooling the composition obtained.
According to one preferred embodiment, the method makes it possible to prepare a
composition in which:
· the active ingredient represents a minimum of 10% and a maximum of
48%, preferably from 20% to less than 40% by weight of the composition of the
coated granule, and
• the fatty matrix comprising an adjuvant represents more than 50% and up
to 85% by weight of the composition of the coated granule.
According to another preferred embodiment, the method makes it possible to
prepare a composition in which:
• the active ingredient represents from 30% to 40%, relative to the weight of
the composition of the coated granule, and
• the fatty matrix represents from 51% up to 65% by weight of the
composition of the coated granule.
Preferably, the granular centre of active ingredient is coated only with a single layer
of coating.
Preferably, the size of the coated granules obtained at the end of step E3) is less
than 500 m h , preferably less than 355 m h , preferably ranging from 100 to 300 m h .
Preferably, the particle size of the final product obtained at the end of step E3) is
distributed according to the following range:
• less than 15% by weight of the coated granules are greater than 500 m h ;
• more than 80% by weight, preferably more than 90% by weight, of the
coated granules are between 355 and 90 mhi ; and
• less than 20% by weight, preferably less than 5% by weight, of the coated
granules are less than 90 m h .
Preferably, the aqueous solution used in step E 1 comprises, as binder, a
hydrophilic polymer preferably chosen from the group of cellulosic derivatives
(hydroxypropylcellulose), povidone (polyvinylpyrrolidone), sucrose, gums, starches,
gelatin and macrogols (polyethylene glycols), which represents approximately from 15%
to 45%, preferably 20% to 40% by weight of said aqueous solution.
Preferably, the binder used in step E 1 for the granulation is a hot-melt agent chosen
from macrogols (PEGs), sucroesters or else poloxamers, and represents approximately
from 0.2% to 20%, preferably from 1% to 15% by weight, relative to the amount of active
ingredient to be granulated in step E 1) .
According to one particular embodiment, the aqueous solution used in step E 1 is
sprayed onto the active ingredient mixed with a diluent (filler). The diluents used in
granulation for increasing the load to be granulated are preferably chosen from polyols,
celluloses, sugars, lactoses, starches, kaolin, calcium phosphates, calcium carbonates or
magnesium carbonates, or derivatives thereof. This diluent represents approximately
from 0 to 39%, preferably 5% to 15% by weight of the composition of the coated granule.
Said diluent may optionally act as a permeabilizing agent thus facilitating dissolution of
the active ingredient.
Preferably, the fatty matrix consists of saturated fatty acids with long C14 to C22,
preferably C16 to C18, carbon-based chains, pure or as mixtures, and/or their
corresponding fatty alcohols.
Preferably, the fatty matrix consists of stearic acid, palmitic acid, myristic acid, pure
or as mixtures, and/or their corresponding fatty alcohols. More preferentially, the fatty
matrix consists only of stearic acid, which is a C18 saturated fatty acid.
Preferably, the adjuvant as a mixture with the fatty matrix is chosen from the group
of surfactants (phospholipid, polysorbate, lauryl sulphate), hydrophilic excipients such as
sucrose, polyols, cellulose, lactose, silica, dicalcium phosphate, carbonates, starch,
macrogols and agents which are soluble at acidic pH (methacrylic derivatives), pure or as
mixtures. Preferably, the adjuvant used is a glycerolipid, in particular a phospholipid.
More preferentially, this phospholipid is a lecithin (phosphatidylcholine), preferably
soybean lecithin.
Said fatty matrix coating the granular centre preferably consists of stearic acid and
the adjuvant as a mixture with the fatty matrix is soybean lecithin.
Preferably, the percentage by weight of the adjuvant added to the fat in step E2 is
less than 10% by weight, preferably less than 5% by weight, preferably ranging from 1%
to 3% by weight, relative to the weight of the composition of the coated granule.
Preferably, the percentage by weight of the binder constituting the coating of the
granule obtained in step E 1 represents from 1% to 5% by weight, relative to the weight of
the composition of the coated granule, for a hydrophilic polymer and from 0.2% to 18%
for a hot-melt agent.
Preferably, the active ingredient is chosen from the group consisting of antibiotics
such as cephalosporins and macrolides, advantageously chosen from: pristinamycin,
cefpodoxime, roxithromycin, spiramycin, rovamycin and levofloxacin, or the group
consisting of corticoids such as prednisolone or methylprednisolone, or else the group
consisting of NSAIDs such as tiaprofenic acid, ketoprofen, ketoprofen lysinate or
ibuprofen, or the group consisting of analgesics such as paracetamol, or else the group
consisting of zopiclone, riluzole, Zolpidem, clobazam, thiocolchicoside, drotaverine
hydrochloride or base, amodiaquine hydrochloride, diltiazem, levocetirizin, mizolastine,
dronedarone, celivarone, dramamine, ramipril, irbesartan, clopidogrel, leflunomide,
nicorandil, lysine acetyl salicylate, magnesium citrate, levothyroxine, sodium valproate,
rifampicin, artesunate and omeprazole.
Preferably, the method is followed by a step E4 of formulating the coated granules
obtained in step E3 with excipients such as diluents, fillers, viscosity modifiers,
disintegrating agents, effervescent agents, colourants, sweeteners, salivating agents,
flavourings, buffers and sequestering agents, flow agents and lubricants for producing an
oral form in the form of granules for sachets, granules for oral suspension, or granules for
conventional tablets or for orodispersible tablets.
According to another subject, the invention relates to a composition of medicinal
active ingredient comprising (a) a granular centre consisting of grains of active ingredient
agglomerated in the presence of binder and, optionally, of diluent or of lubricant, and (b) a
layer of coating of said granular centre consisting of a fatty matrix, in which composition:
· the active ingredient represents a minimum of 10%, preferably 20% or else
30% by weight, relative to the weight of the composition of the coated granule; the
active ingredient represents a maximum of 48%, preferably a maximum of 40%, the
active ingredient preferably represents from 20% to less than 40%, relative to the
weight of the composition of the coated granule, more preferentially the active
ingredient represents from 30% to 40%, relative to the weight of the composition of
the coated granule;
the fatty matrix represents more than 50% and up to 85% by weight of the
composition of the coated granule, preferably from 51% to 65%, the fatty matrix
optionally comprising an adjuvant, preferably chosen from hydrophilic agents,
surfactants or mixtures thereof, and the latter representing less than 10%, preferably
from 1% to 3% by weight, relative to the weight of the composition of the coated
granule;
the binder, preferably a hydrophilic agent chosen from hydrophilic polymers or
hot-melt agents, represents from 0.2% to 18% by weight, relative to the weight of the
composition of the coated granule, preferably the binder represents less than 18% by
weight for a hot-melt agent or else preferably the binder represents less than 10% by
weight for a hydrophilic polymer;
the diluent, if necessary, as filler, represents a content of 0 to 39%, relative to
the weight of the composition of the coated granule;
· the lubricant, if necessary, as flow agent, represents a content of 0 to 1.8%,
relative to the weight of the composition of the coated granule.
Preferably, in the composition of medicinal active ingredient according to the
invention, said fatty matrix consists of saturated fatty acids with long C14 to C22,
preferably C16 to C18, carbon-based chains, pure or as mixtures, and/or their
corresponding fatty alcohols, and the binder is chosen from hydrophilic polymers. More
preferentially, the fatty matrix consists only of stearic acid, which is a C18 saturated fatty
acid.
Preferably, said fatty matrix comprises an adjuvant chosen from the group of
surfactants (phospholipid, polysorbate, lauryl sulphate), hydrophilic excipients such as
sucrose, polyols, cellulose, lactose, silica, dicalcium phosphate, carbonates, starch,
macrogols and agents which are soluble at acidic pH (methacrylic derivatives), pure or as
mixtures, preferably phospholipids. Preferably, the adjuvant used is a glycerolipid, in
particular a phospholipid. More preferentially, this phospholipid is a lecithin
(phosphatidylcholine), preferably soybean lecithin.
Preferably, said fatty matrix coating the granular centre consists of stearic acid and
the adjuvant as a mixture with the fatty matrix is soybean lecithin.
Preferably, the adjuvant is a surfactant which represents less than 10% by weight,
preferably less than 5% by weight, preferably from 1% to 3% by weight, relative to the
weight of the composition of the coated granule.
Preferably, the active ingredient is chosen from the group consisting of antibiotics
such as cephalosporins and macrolides, advantageously chosen from: pristinamycin,
cefpodoxime, roxithromycin, spiramycin, rovamycin and levofloxacin, or the group
consisting of corticoids such as prednisolone or methylprednisolone, or else the group
consisting of NSAIDs such as tiaprofenic acid, ketoprofen, ketoprofen lysinate or
ibuprofen, or the group consisting of analgesics such as paracetamol, or else the group
consisting of zopiclone, riluzole, Zolpidem, clobazam, thiocolchicoside, drotaverine
hydrochloride or base, amodiaquine hydrochloride, diltiazem, levocetirizin, mizolastine,
dronedarone, celivarone, dramamine, ramipril, irbesartan, clopidogrel, leflunomide,
nicorandil, lysine acetyl salicylate, magnesium citrate, levothyroxine, sodium valproate,
rifampicin, artesunate and omeprazole.
Preferably, the amount of active ingredient represents more than 10% by weight
and ranges up to 48% by weight, relative to the weight of the composition of the coated
granule.
Preferably, the amount of active ingredient represents more than 10% by weight of
the composition of the coated granule and the fatty matrix comprises an adjuvant.
Preferably, the amount of active ingredient represents from 20% to less than 40%
by weight of the composition of the coated granule.
Preferably, the composition of the active ingredient according to the invention is
obtained by means of the method as described above.
According to another subject, the invention relates to a pharmaceutical composition
comprising the composition of medicinal active ingredient as described above or else
which can be prepared according to the method described above.
According to another subject, the invention relates to a sachet for an oral
suspension comprising the composition of active ingredient as defined above in the
presence of an excipient chosen from diluents, viscosity modifiers, disintegrating agents,
sequestering agents, buffers, preservatives, lubricants, wetting agents, effervescent
agents, colourants, sweeteners, salivating agents or flavourings.
According to another subject, the invention relates to tablets to be chewed,
swallowed or sucked, or orodispersible or water-dispersible tablets with a masked taste,
comprising the composition of active ingredient as defined above in the presence of an
excipient chosen from diluents, binders, lubricants, salivating agents, anaesthetic agents,
wetting agents, preservatives, flow agents, disintegrating agents, colourants, sweeteners
or flavourings.
According to another subject, the invention relates to a powder to be swallowed,
with masked taste, comprising the composition of active ingredient as defined above in
the presence of an excipient chosen from diluents, salivating agents, effervescent agents,
flow agents, preservatives, colourants, sweeteners or flavourings.
According to another subject, the invention relates to the use of a composition of
medicinal active ingredient as defined above or prepared according to the method
described above, for preparing pharmaceutical compositions in the form of sachets for an
oral suspension, powders to be swallowed, tablets to be chewed, tablets to be swallowed,
tablets to be sucked, orodispersible tablets or water-dispersible tablets, and having a
masked taste.
DETAILED DESCRIPTION OF EMBODIMENTS OF THE INVENTION
Method for preparing the composition of medicinal active ingredient
1) Granulation step
In a first step of the method, an aqueous wetting solution comprising a binder of
hydrophilic polymer type is sprayed onto the active ingredient in the crude state or onto
an active ingredient/diluent (filler) mixture or onto an active ingredient/lubricant mixture or
an active ingredient/diluent/lubricant mixture.
Preferably, the aqueous solution contains approximately 10% to 45% by weight,
preferably 15% to 40% by weight, of binder of hydrophilic polymer type in the aqueous
solution.
The parameters used for this granulation step are suitable for the properties of the
active ingredient and for the equipment used.
The aqueous wetting solution used can be replaced, when moisture-sensitive active
ingredients are used, with a hot-melt binder (of macrogol type).
This step makes it possible to obtain an active ingredient which is finely granulated
by homogenization and recentring of the particle size distribution of the active ingredient,
with the aim of improving the quality of the second, coating step.
According to one variant, it is also possible to carry out a calibration of the granular
active ingredient obtained in the step above, in order to select the granules having a
diameter of less than 500 m h .
2) Hot-melt coating step
In a second step, the active ingredient in the granular state is preferably fluidized in
a fluidized air bed.
The fatty matrix is brought to melting, with stirring, in a melting kettle at a
temperature of approximately 10 to 20°C above its melting point.
The melting points of the fatty substances used are in the region of from 50 to 80°C,
preferentially from 55 to 65°C or else preferably around 60°C. This melting range was
preferably chosen, firstly, for reasons of physical stability of the composition thus
formulated and, secondly, in order to have, in the end, as prompt a release of active
ingredient as possible.
According to one preferred embodiment, an adjuvant (surfactant or hydrophilic
excipient) is added to the melted fatty matrix with, optionally, a preservative. This
adjuvant makes it possible to promote the obtaining of a prompt release profile of the
composition.
The molten mixture is then sprayed onto the active ingredient in order to produce a
coating by the "hot-melt coating" method. The parameters applied during the coating
method are summarized below.
The coating method can be carried out in a fluidized air bed apparatus. The nozzles
are fed, on the one hand, with the molten mixture which circulates via a pump in an
entirely thermally-insulated and completed circuit, and secondly, with hot compressed air
fed via an air heater.
The main operating parameters applied, which are suitable for the equipment used
and the batch size used, are the following:
- T° of the fatty substance melted: from 70 to 95°C, according to the properties
and characteristics of the fatty matrix;
T° compressed air for spraying: from 80 to 120°C;
Compressed air pressure: from 0.5 to 1.5 bar;
- T° of the feed circuits: between 80 and 100°C;
- Liquid flow rate: from 5 to 30 g/min;
Air flow rate: this is usually adjusted according to the size of the equipment.
For an apparatus with a working capacity of 3 kg, an air flow rate of 50 to
160 m /h is generally used, according to the equipment filling load;
T° air inlet: from 25 to 50°C, according to the properties of the fatty matrix
used.
At the end of these steps and after cooling, a composition of medicinal active ingredient
comprising a granular centre consisting of grains of active ingredient agglomerated in the
presence of binder, and a layer of coating of said granular centre consisting of fatty
matrix, is obtained.
Preferably, the granular centre of active ingredient is coated only with a single layer of
coating.
Description of the composition of medicinal active ingredient
1. Active ingredient
The invention relates to any type of active ingredient in the form of solid particles
intended to be coated in order to mask their unsatisfactory organoleptic or
physicochemical properties.
The active ingredient used in the invention in particular has unpleasant organoleptic
properties (taste, odour, appearance), an unacceptable taste and/or an unacceptable
odour, or else it can have an anaesthetic, hot, irritant or astringent effect when it passes
through the oral cavity. In addition, the active ingredient used in the invention may also be
heat-sensitive or else moisture-unstable.
It is preferably chosen from the group consisting of antibiotics such as
cephalosporins and macrolides, advantageously chosen from: pristinamycin,
cefpodoxime, roxithromycin, spiramycin, rovamycin and levofloxacin, or the group
consisting of corticoids such as prednisolone or methylprednisolone, or else the group
consisting of NSAIDs such as tiaprofenic acid, ketoprofen, ketoprofen lysinate or
ibuprofen, or the group consisting of analgesics such as paracetamol, or else the group
consisting of zopiclone, riluzole, Zolpidem, clobazam, thiocolchicoside, drotaverine
hydrochloride or base, amodiaquine hydrochloride, diltiazem, levocetirizin, mizolastine,
dronedarone, celivarone, dramamine, ramipril, irbesartan and clopidogrel.
Among the moisture-sensitive active ingredients, mention may be made of:
leflunomide, nicorandil, lysine acetyl salicylate, ramipril, magnesium citrate, levothyroxine,
sodium valproate, rifampicin, artesunate, clopidogrel and omeprazole.
Amisulpride is excluded from the list of active ingredients used in the invention.
According to one preferred embodiment, the active ingredient used in the invention
is chosen from the group consisting of drotaverine hydrochloride or base, clobazam,
paracetamol, riluzole, ketoprofen, ketoprofen lysinate, clopidogrel, irbesartan, zopiclone,
Zolpidem and pristinamycin.
2. Active ingredient granulating agents
The granulating agents used in the first step of the method are binders preferably
chosen from hydrophilic agents. They are used in a proportion of from 0.2% to 18% by
weight, relative to the weight of the composition of the coated granule.
These hydrophilic agents are particularly chosen from the group of cellulosic
derivatives (hydroxypropylcellulose), povidone (polyvinylpyrrolidone), sucrose, gums,
starches, gelatin, macrogols, sucroesters and poloxamers.
According to one embodiment, use is in particular made of hydrophilic polymers,
preferably PEG or PVP in an aqueous solution in a proportion of from approximately 10%
to 45% by weight in the aqueous solution.
Preferably, when the binder is a hydrophilic polymer, the percentage by weight of
the binder is less than 10% by weight, preferably less than 5% by weight, preferably
ranging from 1% to 5% by weight, relative to the weight of the composition of the coated
granule.
According to another embodiment, use is made of hydrophilic agents chosen from
hot-melt agents (melting point < 85°C) such as macrogols (PEG), sucroesters or else
poloxamers, in particular when moisture-sensitive active ingredients are used. The
concentrations of hot-melt binders used are about from 0.2% to 20%, preferably from 1%
to 15% by weight, relative to the amount of active ingredient to be granulated .
Preferably, when the binder is a hot-melt agent, the percentage by weight of the
binder is less than 18% by weight, preferably less than 13.5% by weight, relative to the
weight of the composition of the coated granule, and preferably from 0.2% to 13.5% by
weight, relative to the weight of the composition of the coated granule.
The diluents used in granulation in order to increase the load to be granulated or
else in order to facilitate the dissolution of the active ingredient are preferably chosen
from polyols, celluloses, sugars, lactoses, starches, kaolin, calcium phosphates, calcium
carbonates or magnesium carbonates, or mixtures thereof. These diluents are present in
a content of between 0 and 80% of the weight of the granule, which represents 0 to 39%
by weight of the weight of the composition of the coated granule.
The lubricants used in granulation in order to improve the fluidization are preferably
chosen from silicas and talc. These lubricants are present in a content of between 0 and
2% of the weight of the granule, which represents 0 to 1.8% by weight of the weight of the
composition of the coated granule.
3. Characteristics of the granular active ingredient
The granule comprising the active ingredient and the binder, obtained at the end of
the first granulation step, has a particle size of less than 500 m h , preferably on average
4. Fatty matrix
The fatty matrices are chosen from the group of saturated fatty acids with long C 14
to C 18, preferably C 16 to C 18, carbon-based chains, pure or as mixtures, and/or their
corresponding fatty alcohols and/or the corresponding esters of fatty acids and alcohols.
Preferably, the fatty matrix consists of stearic acid , palmitic acid , myristic acid, pure or as
mixtures, and/or their corresponding fatty alcohols. More preferentially, the fatty matrix
consists only of stearic acid , which is a C 18 saturated fatty acid .
Preferably, the fatty matrix represents more than 50% by weight of the composition
and up to 85% by weight of the composition ; more preferentially from 5 1% to 65% by
weight of the composition of the coated granule.
According to one preferred embodiment, use is made, as fatty matrix, of stearic acid
in a proportion of more then 50% by weight, relative to the weight of the composition of
the coated granule, preferably from 5 1% to 65% in order to improve the masking of the
taste of very unpleasant molecules.
5. Fatty matrix adjuvants
The adjuvants are chosen from the group of surfactants such as phospholipids,
polysorbate or lauryl sulphate, hydrophilic excipients such as sucrose, polyols, cellulose,
lactose, silica, dicalcium phosphate, starch, povidones or macrogols, and agents which
are soluble at acidic pH, such as methacrylic derivatives; preferably, phospholipids are
used. Preferably, the adjuvant used is a glycerolipid, in particular a phospholipid. More
preferentially, this phospholipid is a lecithin (phosphatidylcholine), preferably soybean
lecithin.
Preferably, the percentage by weight of the adjuvant added to the fat in the coating
step is less than 10% by weight, preferably less than 5% by weight, preferably ranging
from 0.5% to 3.5% or else from 1% to 3% by weight, relative to the weight of the
composition of the coated granule.
According to one preferred embodiment, phospholipids are used as adjuvant,
preferentially soybean lecithin, in a proportion of from 1% to 3% by weight, relative to the
weight of the composition of the coated granule, in order to improve the dissolution
profile.
Characteristics of the composition of medicinal active ingredient :
Particle size
The particle sizes of the products resulting from this method are about a few
hundred microns (according to the parameters applied and the type of equipment used).
The particle size distribution of the product obtained is distributed according to the
following range:
o less than 15% by weight of the coated granules are greater than 500 m h ;
o more than 80% by weight, preferably more than 90% by weight, of the coated
granules are between 355 and 90 m h ; and
o less than 20% by weight, preferably less than 5% by weight, of the coated
granules are less than 90 m h .
Preferred amounts and ratio
The composition according to the invention consists of medicinal active ingredient
comprising (a) a granular centre consisting of grains of active ingredient agglomerated in
the presence of binder, and (b) a layer of coating of said granular centre consisting of
fatty matrix.
In this composition, the preferred amounts and ratios of the various combinations of
ingredients are represented below:
• the active ingredient represents a minimum of 30% by weight relative to the
weight of the composition of the coated granule; the active ingredient
represents a maximum of 48%, preferably a maximum of 40%, the active
ingredient preferably represents from 30% to 40%, relative to the weight of the
composition of the coated granule;
• the fatty matrix represents more than 50% and up to 85% by weight of the
composition of the coated granule, preferably from 51% to 65%, the fatty
matrix optionally comprising an adjuvant, preferably chosen from hydrophilic
agents, surfactants or mixtures thereof, and the latter representing less than
10% by weight of the composition, preferably from 1% to 3% by weight,
relative to the weight of the composition of the coated granule;
• the adjuvant, when it is present in the fatty matrix, represents less than 10%
by weight of the composition, preferably from 1% to 3% by weight, relative to
the weight of the composition of the coated granule;
· the binder, preferably a hydrophilic polymer or a hot-melt agent, represents
less than 18% (for a hot-melt agent) or else less than 10% (for a polymer) by
weight, relative to the weight of the composition of the coated granule;
• the diluent, if necessary, as filler, represents a content of from 0 to 39% by
weight, relative to the weight of the composition of the coated granule;
· the lubricant, if necessary as flow agent, represents a content of from 0 to
1.8% by weight, relative to the weight of the composition of the coated
granule.
Properties
The formulation of the coated granule according to the invention allows effective
masking of the taste and of the odours of active ingredients with unpleasant organoleptic
properties. This is because the coating of the active ingredient allows the creation of a
barrier around said active ingredient so as to mask its taste, its odour and, potentially, its
colour.
In parallel, products having a relatively prompt release of the active ingredient in
vitro are obtained (for example a minimum release of 70% in 60 min).
Moreover, by virtue of the effective taste masking, it is possible to obtain products
with a high dose of active ingredient, for instance containing more than 30% of active
ingredient, which makes it possible to notably reduce the doses of products to be
administered to the patient, in particular to young children or to the elderly.
According to another advantage, this method makes it possible to combine a high
dosage of the active ingredient with heat-sensitive or moisture-sensitive active
ingredients.
In addition, it is observed that the physical appearance of the final products
obtained remains stable during heat-stability tests (30°C/65%RH).
Furthermore, it is observed that the composition of the coated granule exhibits good
stability with respect to moisture.
According to another additional advantage, this method makes it possible, by virtue
of the quality of its coating, to inhibit the anaesthetic, irritant, astringent and unpleasant
effect in the mouth of certain active molecules.
Evaluation of the taste masking:
The taste masking produced by this coating can be evaluated:
qualitatively, by means of tasting tests carried out by volunteers;
quantitatively, using analytical methods such as the "glass of water test" in
which the amount of active ingredient released at a given time is assayed and
a comparison is made with a given bitterness threshold.
The method of the glass of water test, making it possible to replace the tasting test,
is described below for the example of pristinamycin:
Calculation of the concentration in the glass of water:
The concentration of pristinamycin dissolved at time "t" (C gra nuie) is calculated
according to the measurement of absorbance at 252 nm in the glass of water AgranU e and
of the pristinamycin control (Apyo control) at the concentration C COntroi :
Cgranuie ( ) (^granule C Control) / A y0 control
The bitterness threshold for pristinamycin is set at 400 mg/L released in
15 minutes.
In vitro dissolution/release:
The dissolution profiles for the composition obtained at the end of the method are
determined according to the method of the European Pharmacopoeia 2.9.3.
Physical stability
The appearance of the product after 3 months at 30°C and 65%RH is examined.
When the product is nonagglomerated, the result is denoted satisfactory (++) or
when the product is agglomerated, the result is denoted unsatisfactory (- -).
Moisture-stability
The appearance of the granule coated in accordance with the method according to
the invention is examined when said granule is placed under accelerated degradation
conditions, i.e. in a controlled chamber at 40°C and 75% relative humidity (RH).
The stability of the active agent is measured by assaying the degradation impurities
produced from said active agent.
The behaviour with respect to moisture, of the product resulting from the method of
the invention, is compared at various coating contents.
Anaesthetic effect test:
A taste test is carried out by volunteers. The test tablets are broken in half and then
placed in the mouth. The anaesthetic effect in the oral cavity is assessed after several
minutes following administration of the half-tablet.
When the anaesthetic effect is no longer felt, the result is denoted satisfactory (++)
or when the anaesthetic effect persists, the result is denoted unsatisfactory (- -).
The molecules which have an anaesthetic effect and which are exemplified in the
compositions tested are drotaverine and riluzole.
Formulation of the external phase
The granule coated with fatty matrix, obtained according to the method of the
invention, may subsequently be integrated into an external formulation for the
manufacture of an oral form, such as granules for a sachet, granules for suspension,
tablets to be chewed, tablets to be sucked, tablets to be swallowed or else orodispersible
tablets or granules.
In the case of the formulation of sachets, the formulation of the external phase can
be enriched with surfactants or wetting agents in order to improve the resuspension of the
granules obtained in an aqueous medium.
Other excipients, such as fillers or diluents, colourants, sweeteners, viscosity
modifiers or gelling agents, adsorbents, buffers or flavourings may also be added to the
formulation for the purpose of improving the final appearance of the product.
Examples
The following examples illustrate the present invention without, however, limiting
the scope thereof.
A. Preparation of the granular medicinal active ingredients coated with a fatty
matrix
Various active ingredients characterized by their strong unpleasant odour and/or
their very pronounced bitterness or else having an anaesthetic, hot, irritant or astringent
effect were used in the tests.
1. Description of the hot melt method for obtaining the compositions
according to the invention
Three kilos of pristinamycin in the crude state are fluidized in a fluidized air bed.
Over the course of a few minutes of fluidization at an average flow rate of 90 m /h,
spraying is initiated at an average flow rate of 30 g/min.
The granulation solution is composed of 1.4 kg of water in which 600 g of PEG
6000 fine powder are dispersed, i.e. a concentration of 30% of binder.
The inlet temperature is set at 75°C for a product and outlet temperature equal to
40°C. The spraying lasts approximately 1 hour. The grain obtained is finely granulated
and has a particle size predominantly less than 200 m h .
In the case of moisture-sensitive active ingredients, the granulation can be carried
out directly with PEG 6000 alone in the molten state.
The fatty matrix consisting of stearic acid is melted at 80°C. After homogenization of
the fatty substance, the phospholipid adjuvant, in an amount of from 2% to 5% according
to the formulations, is added to the molten fatty matrix until complete homogenization of
the mass is obtained.
Stirring is maintained throughout the duration of spraying.
A few hundred grams of granules are fluidized in the fluidized air bed with an air
flow rate of 70 to 90 m /h (the latter is adjusted according to the progression of the step,
i.e. according to the load and the density gradually acquired by the grain).
The inlet air temperature during the coating is set between 30° and 40°C. The
molten mixture is then sprayed at a flow rate of 15 g/min on average.
Once set, this flow rate remains constant throughout the duration of the spraying.
The spray pressures used are themselves also kept constant and are between 0.5 and
0.9 bar. The air used is heated to a target temperature of 90°C.
The spraying time varies according to the formula. Once the spraying is complete,
the inlet air temperature is cut and the granule is thus cooled before being discharged.
2. Influence of the fatty matrix and of the adjuvant in a composition of active
agent according to the invention on the particle size, the masking of bitterness, the
dissolution, the physical stability and the anaesthetic effect of the active ingredient
Tables I and I I represent all the formulations tested from C 1 to C20.
Table I
Ingredients % by weight C 1 C2 C3 C4 C5 C6 C7 C8 C9 C10 C 11
Active pristinamycin 32.5 34.6 32.8 29 25.1 25.2 24.7 25 18.3 20.8 23.4
ingredient
Lubricant aerosil 200 0.3 0.4 0.3 0.3 0.3 0.3 0.3
Binder PEG 600 6.6 7 6.6 5.9 5.1 5.1 5 5 3.7 4.2 4.7
Fatty stearic acid 60 64.8 64.5 64.4 65 65 75 73 70
matrix stearyl 60.3
alcohol
palmitic acid 60.6
Adjuvant phospholipid 5 2 3 2 2
polysorbate 5
PEG 6000 5
Results
Particle size profile ++ ++ ++ ++ ++ — ++ ++ ++ ++ ++
Bitterness masking ++ ++ ++ ++ ++ ++ — ++ ++ ++ ++
Dissolution profile TO — ++ ++ — ++ — — ++ ++ ++ ++
Physical stability T 3 ++ ++ ++ / / / / ++ / / /
months
40°C/75%RH
Dissolution profile T 3 ++ / / / / / / / /
months
30°C/65%RH
Table II
Ingredients % by weight C 12 C 13 C 14 C 15 C 16 C 17 C 18 C 19 C20
Active drotaverine 30 29.5 28
ingredient clobazam 18 14 16
riluzole 43
clopidogrel 32.3
ketoprofen 35
Diluent mannitol 25 19.5 22.3
Lubricant colloidal silica 0.9
Binder PVP 4 4.5 4 2 1.5 1.7 5 .1 1.85
PEG 5.7
Fatty matrix stearic acid 65 65 65 55 65 59 5 1 60 60
Adjuvant phospholipid 1 3 1 2 2
Results
Particle size profile ++ ++ ++ ++ ++ ++ ++ ++
Taste masking ++ ++ ++ ++ ++ + ++ ++
Anaesthetic effect inhibition ++ ++ ++ N N N ++ N N
Dissolution profile TO — - ++ / ++ / ++ ++
++: Satisfactory result - : Unsatisfactory result / : Absence of result
N: Not concerned
Conclusions
1) Presence of the adjuvant:
It may be noted that the addition of an adjuvant to the formulation in the fatty matrix,
of phospholipid type added in an amount of a few percent, 2 to 5%, makes it possible to
accelerate dissolution.
2) Choice of fatty substance:
It may be noted that, according to the type of fatty substance, for the same masking
quality, the dissolution profiles and the physical heat-stability are not equivalent (cf.
Examples C 1, C2, C3). The best compromise is obtained with stearic acid, which is a
C18 saturated fatty acid.
3) Choice of adjuvant:
The comparison of several types of adjuvants showed that phospholipid makes it
possible to obtain the best bitterness masking/dissolution compromise (cf. Examples C5
to C 11) . The preferred phospholipid is soybean lecithin.
4) Choice of adjuvant content:
When a phospholipid content of more than 10% is used in the coating formula, a
technical difficulty is observed and the method cannot be carried out.
When a phospholipid content of less than 5% is used in the coating formula, it is
observed that the method can be carried out, but that a composition agglomeration
phenomenon may occur during storage.
Few differences are noted between the percentages of 1, 2 and 3% (cf. Examples
C13, C14, C17 and C19).
3. Effect of a composition of active ingredient according to the invention on
the stability of said active agent with respect to moisture
Nicorandil (N-(2-hydroxyethyl)nicotinamide nitrate) was chosen as an example of
an active molecule particularly sensitive to moisture.
It was used according to the method of the invention with, in step E 1) , granulation
using a hot-melt agent, polyethylene glycol 6000 or PEG 6000. This granule obtained is
then coated according to step E2) of the method according to the invention at various
coating contents with respect to stearic acid: 30% (comparative example), then 54% and
80% (according to the invention). Step E3) is carried out for all the batches.
The resulting coated granules are then placed under stressing temperature and
humidity conditions at 40°C/75%RH in a climatic chamber under open conditions (open
pillbox).
After 3 days, nicorandil impurity assay analyses are performed by HPLC.
The formulae of the compositions tested, corresponding to the various coating contents,
are the following (the percentages are expressed by weight relative to the composition of
the coated granule):
Components Percentage composition (%)
COMPOSITION A nicorandil 59.50
PEG 6000 10.50
stearic acid 30.00
COMPOSITION B nicorandil 38.93
PEG 6000 6.87
stearic acid 54.20
COMPOSITION C nicorandil 17.00
PEG 6000 3.00
stearic acid 80.00
The results of the nicorandil degradation impurity assay analyses are given in the table
below:
* : known major impurities of nicorandil
These results demonstrate that the coating containing stearic acid significantly improves
the stability of nicorandil placed under very high relative humidity conditions. The
percentage of major impurities is significantly reduced on compositions B (54% stearic
acid) and C (80% stearic acid) compared with composition A (30% stearic acid).
These results show the protective effect, with respect to moisture, of a coating containing
stearic acid at greater than 50% in the composition of the coated granule.
4. Effect of a composition of active ingredient according to the invention on
the inhibition of the anaesthetic effect of said active agent
Drotaverine was chosen as an example of an active molecule having a persistent
anaesthetic effect.
It was used according to the method of the invention with, in step E1), a povidone
(PVP-K30)-based aqueous-phase granulation.
The resulting granular centre is then coated, in step E2), with stearic acid at various
coating contents. Step E3) is finally carried out.
The composition of the coated granule comprises approximately 43% of
drotaverine, from 1% to 10% of povidone and various corresponding stearic acid
contents.
The introduction of an external phase into the composition of the coated granule
thus obtained allows tableting.
The tablets are tasted by volunteers.
The study made it possible to demonstrate that a coating content of less than or
equal to 50% was not sufficient to suitably mask the anaesthetic effect of drotaverine. On
the other hand, when the coating content is greater than 50%, and preferably about 65%
by weight of the composition of the coated granule, the anaesthetic effect of drotaverine
is greatly reduced, or even nonexistent.
5. Pharmaceutical compositions according to the invention
The percentages indicated below are expressed by total weight of the composition:
a) Preparation of granules or of a powder to be swallowed, in sachets:
The formulation of the external phase is the following:
- Diluents: from 5% to 90%
- Lubricants: from 0.5% to 2%
Viscosity modifiers : from 1% to 10%
Effervescent agents: from 1% to 7%
Sweeteners: from 0.5% to 5%
- Flavours: from 1% to 5%
- Colourants: from 0.1 % to 3%
Buffering agents: from 0.1% to 3%
Sequestering agents: from 0.1% to 10%.
The external phase is added to the coated granules produced according to the
invention in a proportion of from 40% to 70%.
All of the excipients of the external phase, with the exception of the lubricants, are
mixed with the coated granules. A lubrication step is then carried out before the
placing in sachets.
b) Preparation of tablets to be chewed, swallowed or sucked:
The formulation of the external phase is the following:
- Diluents: from 5% to 90%
Lubricants: from 0.5% to 5%
Sweeteners: from 0.5% to 5%
- Flavours: from 1% to 5%
- Colourants: from 0.1% to 3%.
The external phase is added to the coated granules produced according to the
invention in a proportion of from 40% to 70%.
All of the excipients of the external phase, with the exception of the lubricants, are
mixed with the coated granules. A lubrication step is then carried out and the
whole is then tableted.
c) Preparation of orodispersible or dispersible tablets:
The formulation of the external phase is the following:
- Diluents: from 5% to 90%
Disintegrating agents: from 0 to 30%
Salivating agents: from 1% to 5%
Lubricants or flow agents: from 0.5% to 5%
Sweeteners: from 0.5% to 5%
Flavours: from 1% to 5%
- Colourants: from 0.1% to 3%.
The external phase is added to the coated granules produced according to the
invention in a proportion of from 40% to 70%.
All of the excipients of the external phase, with the exception of the lubricants, are
mixed with coated granules. A lubrication step is then carried out and the whole is
then tableted.
d) Orodispersible ketoprofen tablets (25 mg):
Coated granule according to the invention:
- Ketoprofen: 7.81%
- Binder: 0.41%
- Stearic acid: 8.60%
External phase:
Disintegrating agent: 7%
- Diluents: 73.58%
- Lubricants or flow agents: 1%
Flavours and sweeteners: 1.6%.
All of the excipients of the external phase, with the exception of the lubricants, are
mixed with the coated granules. A lubrication step is then carried out and the
whole is then tableted.
CLAIMS
1. Method for preparing a composition of medicinal active ingredient comprising
(a) a granular centre consisting of grains of active ingredient, agglomerated in the
presence of binder, and (b) a layer of coating of said granular centre consisting of
fatty matrix, in which composition:
• the active ingredient represents a minimum of 10%, preferably 20% or else
30% by weight, relative to the weight of the composition of the coated granule;
the active ingredient represents a maximum of 48%, preferably a maximum of
40%, the active ingredient preferably represents from 20% to less than 40%,
relative to the weight of the composition of the coated granule, more
preferentially the active ingredient represents from 30% to 40%, relative to the
weight of the composition of the coated granule;
• the fatty matrix represents more than 50% and up to 85% by weight of the
composition of the coated granule, preferably from 51% to 65%, the fatty
matrix optionally comprising an adjuvant, preferably chosen from hydrophilic
agents, surfactants or mixtures thereof, and the latter representing less than
10%, preferably from 1% to 3% by weight, relative to the weight of the
composition of the coated granule;
• the binder, preferably a hydrophilic agent chosen from hydrophilic polymers or
hot-melt agents, represents from 0.2% to 18% by weight, relative to the weight
of the composition of the coated granule, preferably the binder represents less
than 18% by weight for a hot-melt agent or else preferably the binder
represents less than 10% by weight for a hydrophilic polymer;
• the diluent, if necessary, as filler, represents a content of 0 to 39%, relative to
the weight of the composition of the coated granule;
• the lubricant, if necessary, as flow agent, represents a content of 0 to 1.8%,
relative to the weight of the composition of the coated granule;
the method comprising the steps of:
E1) preparing the granular centre by spraying an aqueous solution comprising
the binder or by spraying the binder in the molten state onto the active
ingredient alone or as a mixture with a diluent and/or a lubricant;
E2) coating by spraying, onto the granules, said fatty matrix pre-melted in a
melting kettle at a temperature approximately 10 to 20°C above its melting
point;
E3) cooling the composition obtained.
2. Method for preparing a composition according to Claim 2, in which:
• the active ingredient represents a minimum of 10% and a maximum of 48%,
preferably from 20% to less than 40% by weight of the composition of the
coated granule, and
· the fatty matrix comprising an adjuvant represents more than 50% by weight
and up to 85% by weight of the composition of the coated granule.
Method for preparing a composition according to Claim 2, in which:
the active ingredient represents from 30% to 40%, relative to the weight of the
composition of the coated granule, and
the fatty matrix represents from 51% up to 65% by weight of the composition
of the coated granule.
4. Method according to one of Claims 1 to 3, in which the size of the coated
granules obtained at the end of step E3) is less than 500 m h , preferably less than
355 m h , preferably ranging from 100 to 300 m h .
5. Method according to one of Claims 1 to 4, in which the particle size of the final
product obtained at the end of step E3) is distributed according to the following
range:
• less than 15% by weight of the coated granules are greater than 500 m h ;
• more than 80% by weight, preferably more than 90% by weight, of the coated
granules are between 355 and 90 m h ; and
• less than 20% by weight, preferably less than 5% by weight, of the coated
granules are less than 90 m h .
6. Method according to one of Claims 1 to 5, in which the aqueous solution used
in step E 1 comprises, as binder, a hydrophilic polymer preferably chosen from the
group of cellulosic derivatives (hydroxypropylcellulose), povidone
(polyvinylpyrrolidone), sucrose, gums, starches, gelatin and macrogols (polyethylene
glycols), which represents approximately from 15% to 45%, preferably from 20% to
40% by weight of said aqueous solution.
7. Method according to one of Claims 1 to 6, in which the binder used in step E 1
for the granulation is a hot-melt agent chosen from macrogols (PEGs), sucroesters
or else poloxamers, and represents approximately from 0.2% to 20%, preferably
from 1% to 15% by weight, relative to the amount of active ingredient to be
granulated in step E 1) .
8 . Method according to one of Claims 1 to 7, in which the fatty matrix consists of
saturated fatty acids with long C 14 to C22, preferably C 16 to C 18, carbon-based
chains, pure or as mixtures, and/or their corresponding fatty alcohols.
9 . Method according to one of Claims 1 to 8, in which the fatty matrix consists of
stearic acid , palmitic acid, myristic acid , pure or as mixtures, and/or their
corresponding fatty alcohols.
10 . Method according to Claim 9, in which the fatty matrix consists of stearic acid .
11. Method according to one of Claims 1 to 10, in which the fatty matrix comprises
an adjuvant chosen from the group of surfactants (phospholipid , polysorbate, lauryl
sulphate), hydrophilic excipients such as sucrose, polyols, cellulose, lactose, silica,
dicalcium phosphate, carbonates, starch, macrogols and agents which are soluble at
acidic pH (methacrylic derivatives), pure or as mixtures.
12 . Method according to Claim 11, in which the adjuvant as a mixture with the
fatty matrix is soybean lecithin.
13 . Method according to one of Claims 1 to 8, in which said fatty matrix coating
the granular centre consists of stearic acid and in which said fatty matrix comprises
soybean lecithin as adjuvant.
14 . Method according to one of Claims 1 to 13, in which the percentage by weight
of the adjuvant added to the fat in step E2 is less than 10% by weight, preferably less
than 5% by weight, preferably ranging from 1% to 3% by weight, relative to the
weight of the final composition .
15 . Method according to one of Claims 1 to 14, in which the percentage by weight
of the binder constituting the coating of the granule obtained in step E1 represents
from 1% to 5% by weight, relative to the weight of the final composition , for a
hydrophilic polymer and from 0.2% to 18% for a hot-melt agent.
16. Method according to one of Claims 1 to 15, in which the active ingredient is
chosen from the group consisting of antibiotics such as cephalosporins and
macrolides, advantageously chosen from: pristinamycin, cefpodoxime, roxithromycin,
spiramycin, rovamycin and levofloxacin, or the group consisting of corticoids such as
prednisolone or methylprednisolone, or else the group consisting of NSAIDs such as
tiaprofenic acid, ketoprofen, ketoprofen lysinate or ibuprofen, or the group consisting
of analgesics such as paracetamol, or else the group consisting of zopiclone,
riluzole, Zolpidem, clobazam, thiocolchicoside, drotaverine hydrochloride or base,
amodiaquine hydrochloride, diltiazem, levocetirizin, mizolastine, dronedarone,
celivarone, dramamine, ramipril, irbesartan, clopidogrel, leflunomide, nicorandil,
lysine acetyl salicylate, magnesium citrate, levothyroxine, sodium valproate,
rifampicin, artesunate and omeprazole.
17. Method according to one of Claims 1 to 16, followed by a step E4 of
formulating the coated granules obtained in step E3 with excipients such as diluents,
fillers, viscosity modifiers, disintegrating agents, effervescent agents, colourants,
sweeteners, salivating agents, flavourings, buffers and sequestering agents, flow
agents and lubricants for the manufacture of an oral formulation in the form of
granules for sachets, granules for oral suspension, or granules for conventional
tablets or for orodispersible tablets.
18. Composition of medicinal active ingredient which can be obtained according
to the method described in one of Claims 1 to 17.
19. Pharmaceutical composition comprising the composition of medicinal active
ingredient as defined in Claim 18 or prepared according to the method of any one of
Claims 1 to 17.
20. Composition according to Claim 19, characterized in that it is in the form of
sachets for oral suspension; tablets to be chewed, swallowed or sucked; or
orodispersible or water-dispersible tabets; or powder to be swallowed.
21. Use of a composition of medicinal active ingredient as defined in Claim 18 or
prepared according to the method of any one of Claims 1 to 17, for preparing a
pharmaceutical composition in the form of sachets for oral suspension, powders to
be swallowed, tablets to be chewed, tablets to be swallowed, tablets to be sucked,
orodispersible tablets or water-dispersible tablets, and having a masked taste.
| # | Name | Date |
|---|---|---|
| 1 | 3078-Kolnp-2012-(11-10-2012)GPA.pdf | 2012-10-11 |
| 2 | 3078-Kolnp-2012-(11-10-2012)FORM-5.pdf | 2012-10-11 |
| 3 | 3078-Kolnp-2012-(11-10-2012)FORM-3.pdf | 2012-10-11 |
| 4 | 3078-Kolnp-2012-(11-10-2012)FORM-2.pdf | 2012-10-11 |
| 5 | 3078-Kolnp-2012-(11-10-2012)FORM-1.pdf | 2012-10-11 |
| 6 | 3078-Kolnp-2012-(11-10-2012)CORRESPONDENCE.pdf | 2012-10-11 |
| 7 | 3078-KOLNP-2012.pdf | 2012-11-06 |
| 8 | 3078-KOLNP-2012-(01-04-2013)-OTHERS.pdf | 2013-04-01 |
| 9 | 3078-KOLNP-2012-(01-04-2013)-CORRESPONDENCE.pdf | 2013-04-01 |
| 10 | 3078-KOLNP-2012-(01-04-2013)-ASSIGNMENT.pdf | 2013-04-01 |
| 11 | 3078-KOLNP-2012-FORM-18.pdf | 2014-05-21 |
| 12 | 3078-KOLNP-2012-FER.pdf | 2017-10-31 |
| 13 | 3078-KOLNP-2012-AbandonedLetter.pdf | 2018-05-18 |
| 1 | search3078_31-10-2017.pdf |