Abstract: The present invention relates to fexofenadine granules, to a composition containing them and to a process for the hot melt coating of fexofenadine. The process for the hot melt coating of fexofenadine allows efficient masking of its bitter taste without, however unacceptably slowing down its dissolution.
FEXOFENADINE-BASED COMPOSITION AND PREPARATION PROCESS
THEREFOR
FIELD OF THE INVENTION
The present invention relates to fexofenadine granules, to a composition containing
them and to a fexofenadine hot melt coating process. The invention also relates to a
formulation comprising a fexofenadine composition.
PRIOR ART AND TECHNICAL PROBLEM
Fexofenadine is characterized by organoleptic or physicochemical properties, in
particular its strong bitterness that it is desirable to mask. The process of hot-melt coating
of fexofenadine thus allows efficient masking of its bitter taste without, however,
unacceptably slowing down its dissolution.
In the field of masking the taste of active principles that have an unacceptable taste,
many tests, using conventional technologies, have been performed: granulation, coating
in a fluidized air bed, etc. The excipients tested were composed of polymers: mainly
cellulose derivatives (HPC, HPMC, EC) and methacrylic acid derivatives (Eudragit range)
and polyvinyl acetate derivatives. These tests often came up against insufficient taste
masking.
In this respect, patent EP 1458387 describes orodispersible tablets comprising
fexofenadine granules comprising a mixture of particular excipients. The described
granules are coated granules containing fexofenadine microcrystals and binders. These
granules are obtained by simple granulation of the active principle with binders, such as
methacrylic acid derivatives.
Patent US 6113942 describes tablets comprising fexofenadine in the form of
granules. The granules are obtained by mixing various components, followed by simple
granulation.
Moreover, more innovative technologies have also been used in the context of taste
masking, such as microencapsulation via a process in supercritical C0 2 phase or via a
simple or complex coacervation method. The same masking polymers, mentioned above,
are thus found, along with less conventional excipients such as chitosan, alginates and
gelatin. The major drawbacks encountered in these technologies are the industrial
implementation and feasibility.
In the same approach, spray-drying and spray-cooling processes were tested.
This latter technique, of "spray-cooling", described in WO 2004/058 137 consists in
melting a fatty matrix and in incorporating the active principle therein. This active principle
is either dissolved or dispersed in the fatty phase, composed of fatty acids, a mixture or
esters of fatty acids, of fatty alcohols or of waxes.
The molten mixture is then conveyed, via a peristaltic pump, to a two-fluid nozzle
where it is sprayed as more or less fine droplets (depending on the applied parameters).
The droplets are finally cooled with a stream of cold air in the spraying chamber and
converted into solid granules containing the active principle dispersed throughout the fatty
matrix.
Although this spray-cooling process makes it possible to obtain pharmaceutical
compositions with satisfactory taste masking, while at the same time ensuring dissolution
of the active principle that is not slowed down in acidic medium, there nevertheless
remains an unsolved problem of physical heat stability of the product obtained. Similarly,
this process remains incompatible with active principles that are by nature heat-sensitive.
Furthermore, in the context of this spray-cooling process, the concentration of
active principle in the composition is limited by the viscosity of the solution or suspension
to be sprayed, which greatly reduces the active principle content of the final composition.
Only compositions with a low dose of active principle can be obtained, i.e. compositions
comprising an amount of active principle not exceeding 30% by weight in the final
composition.
Moreover, the use of a hot-melt coating process was described in WO 02/07706.
The said document describes the use of this technology for coating heat-sensitive active
principles in the form of solid particles that are not granulated beforehand. The targeted
coating amounts are low and do not allow satisfactory masking of the taste of very
unpleasant active principles.
As a result, the use of the hot-melt coating process described in the said document
is not suitable for obtaining sufficiently effective masking of the taste and odour of an
active principle characterized by strong bitterness and a strong odour, especially masking
that is sufficient to permit ingestion of the medicament by a child.
The Applicant has now found a novel improved process for solving these
drawbacks and in particular for obtaining a fexofenadine composition in the form of
coated granules that mask the bitter taste of fexofenadine.
SUMMARY OF THE INVENTION
The aim of the invention is to propose a fexofenadine composition in the form of
coated granules and a process for preparing the said composition, which solve at least
the drawbacks mentioned above.
The problem solved by this manufacturing method, which comprises formulation
with the aid of fatty matrices, is that of masking of the taste of fexofenadine, while at the
same time obtaining relatively rapid in vitro release of fexofenadine (for example a
minimum release of 70% of the active principle in 60 minutes).
Furthermore, the maximum concentration of active principle that may be used in
this process is not limited, the product thus obtained may be highly dosed, i.e.
compositions that may comprise an amount of active principle exceeding 30% by weight
in the final composition may be obtained. This makes it possible to appreciably reduce
the doses of products to be administered to the patient, in particular to young children or
to the elderly.
According to a first aspect, the invention relates to a fexofenadine composition
comprising (a) a granule centre formed from fexofenadine grains aggregated in the
presence of a binder and optionally of a diluent or lubricant, and (b) a layer for coating the
said granule centre formed from a fatty matrix, in which composition:
• the fexofenadine represents at least 10%, preferably 15% or even 20% by
weight relative to the weight of the composition; the fexofenadine represents
not more than 90%, preferably not more than 60% or 50% by weight relative to
the weight of the composition, or even less than 40% by weight relative to the
weight of the composition, preferably the fexofenadine represents from 20% to
40% relative to the weight of the composition;
• the fatty matrix represents more than 10% by weight, preferably from 50%
(inclusive) to 85% (inclusive) by weight of the composition, the fatty matrix
optionally comprising an adjuvant, preferably chosen from hydrophilic agents,
surfactants or mixtures thereof, and these adjuvants representing less than
10% by weight of the composition and preferably from 1% to 3% by weight
relative to the weight of the composition;
• the binder, preferably a hydrophilic agent chosen from hydrophilic
polymers and hot-melt agents, represents from 0.2% to 18% by weight relative
to the weight of the composition, preferably the binder represents less than
18% by weight for a hot-melt agent, or even, preferably, the binder represents
less than 10% by weight for a hydrophilic polymer relative to the weight of the
composition;
• the diluent, if necessary, as filler represents a content of from 0 to 78.8%,
preferably from 0 to 39% and preferably from 5% to 15% by weight relative to
the weight of the composition;
• the lubricant, if necessary, as flow agent represents a content of from 0 to
1.8% relative to the weight of the composition.
The weight percentage is expressed relative to the weight of the fexofenadine
composition in the form of coated granules, unless otherwise mentioned.
Preferably, the binder is a hydrophilic polymer, preferably chosen from the group of
cellulose derivatives (hydroxypropylcellulose or ethylcellulose), povidone
(polyvinylpyrrolidone or PVP), sucrose, gums, starches, gelatin, macrogols (polyethylene
glycols) and a mixture thereof.
According to another mode, the binder is a hot-melt agent chosen from Macrogols
(PEG), sucroesters or poloxamers, and represents approximately from 0.2% to 20% and
preferably from 1% to 15% by weight relative to the amount of active principle to be
granulated in step E1).
A hydrophilic polymer and in particular povidone is preferably used as binder.
According to one particular embodiment, the diluent is chosen from polyols,
celluloses, sugars, lactoses, starches, kaolin, calcium phosphates, calcium or magnesium
carbonates, or derivatives thereof. According to one particular embodiment, the diluent is
chosen from starches, for instance corn starch. This diluent represents approximately
from 0 to 39% and preferably from 5% to 15% by weight of the composition. The said
diluent may optionally act as permeabilizer, thus facilitating the dissolution of
fexofenadine.
Preferably, in the composition according to the invention, the said fatty matrix is
formed from C14 to C22 and preferably C16 to C18 long carbon-chain saturated fatty
acids, pure or as mixtures, and/or the corresponding fatty alcohols thereof, and the binder
is chosen from hydrophilic polymers.
Preferably, the fatty matrix is formed from stearic acid, palmitic acid, myristic acid,
pure or as mixtures, and/or the corresponding fatty alcohols thereof. According to one
particular aspect, the fatty matrix is formed from stearic acid.
Preferably, the said fatty matrix comprises an adjuvant chosen from the group of
surfactants (phospholipid, polysorbate, lauryl sulfate), hydrophilic excipients such as
sucrose, polyols, cellulose, lactose, silica, dicalcium phosphate, carbonates, starch,
macrogols, agents that are soluble at acidic pH (methacrylic derivatives) pure or as
mixtures, preferably phospholipids. Preferably, the adjuvant is a glycerolipid, in particular
a phospholipid. More preferentially, this phospholipid is a lecithin (phosphatidylcholine),
preferably soya lecithin.
Preferably, the adjuvant is a surfactant that represents less than 10% by weight,
preferably less than 5% by weight, preferably from 1% to 3%, or even from 1% to 2%, by
weight relative to the weight of the composition.
Preferably, in the composition according to the invention, the binder is povidone
and the diluent is chosen from starches and in particular corn starch.
Preferably, in the composition according to the invention, the fatty matrix is stearic
acid and the adjuvant is soya lecithin. A composition according to the invention in which
the binder is povidone, the diluent is chosen from starches, and in particular corn starch,
the fatty matrix is stearic acid and the adjuvant is soya lecithin is particularly preferred.
Preferably, the amount of fexofenadine represents more than 10% by weight and
ranges up to 90% by weight relative to the weight of the composition.
Preferably, the amount of fexofenadine represents more than 10% by weight of the
composition and the fatty matrix comprises an adjuvant.
Preferably, the amount of fexofenadine represents from 20% to less than 40% by
weight of the composition and the fatty matrix comprises at least one adjuvant.
Preferably, the fexofenadine composition according to the invention is obtained via
the process as described below.
According to another subject, the invention relates to a pharmaceutical composition
comprising the fexofenadine composition as described above or as may be prepared
according to the process described below.
According to one particular subject, the invention relates to a sachet for a drinkable
suspension or a sachet comprising a composition of granules to be swallowed (also
referred to as powders to be swallowed), and in particular a single-dose sachet
comprising a composition of granules to be swallowed, the said sachet comprising the
fexofenadine composition as defined above in the presence of an excipient, chosen in
particular from diluents, viscosity modifiers, sequestrants, buffers, preserving agents,
lubricants, wetting agents, effervescent agents, dyes, sweeteners, salivating agents,
flavourings, and a mixture thereof.
According to another subject, the invention relates to tablets, to be chewed,
swallowed or sucked, or orodispersible tablets with masked taste comprising the
fexofenadine composition as defined above in the presence of an excipient, in particular
chosen from diluents, binders, lubricants, salivating agents, anaesthetics, wetting agents,
preserving agents, disintegrants, effervescent agents, dyes, sweeteners, flavourings, and
a mixture thereof.
According to another subject, the invention relates to the use of the fexofenadine
composition as defined above for the preparation of sachets for a drinkable suspension,
sachets comprising a composition of granules to be swallowed, and in particular singledose
sachets comprising a composition of granules to be swallowed, tablets to be
chewed, tablets to be swallowed, tablets to be sucked, orodispersible tablets with masked
taste.
The tablets or sachets according to the invention comprise the composition
according to the invention and more specifically the coated fexofenadine granules as
defined above, and an excipient, in particular as defined above.
According to one particular embodiment, the final formulation, for example in the
form of tablets or sachets, may contain amounts of fexofenadine ranging from 20 to
200 mg (for instance 30, 60, 120 or 180 mg). The weight ratio of coated granules relative
to the weight amount of excipient in the final formulation may vary within a wide range, for
example from 0.2 to 0.8.
According to another subject, the invention relates to a process for preparing a
fexofenadine composition as defined above, the said process comprising the steps of:
E1) preparation of the granule centre by spraying an aqueous solution, an organic
solution (for example C1-C4 alcohol) or a mixture thereof (for instance an aqueousalcoholic
solution) comprising a binder or by spraying a molten binder onto the
fexofenadine alone or as a mixture with a lubricant and/or preferably a diluent ;
E2) coating by spraying onto the granules the said fatty matrix melted beforehand in
a melting vessel at a temperature from about 10 to 20°C above its melting point;
E3) cooling the composition obtained.
According to one preferred mode, the process allows the preparation of a
composition in which the fexofenadine represents at least 10% and not more than 90%
and preferably from 20% to 50%, and the fatty matrix comprising an adjuvant represents
more than 10% by weight and preferably from 50% and up to 85% by weight of the
composition.
According to one preferred embodiment, the process allows the preparation of a
composition in which the fexofenadine represents less than 40% by weight, preferably
from 20% to 40%, advantageously from 30% to 40%, relative to the weight of the
composition, and the fatty matrix represents more than 10% by weight, preferably from
50% and up to 85% by weight of the composition, advantageously from 50% to 60%
(inclusive) by weight of the composition.
Preferably, the size of the coated granules obtained after step E3) is less than
500 miti , preferably less than 350 m , preferably ranging from 50 to 350 m.
Preferably, the particle size of the final product obtained after step E3) is distributed
according to the following range:
• less than 15% by weight of the coated granules are greater than 500 mih ;
• more than 80% by weight, preferably more than 90% by weight of the
coated granules are between 350 and 50 m t i; and
• less than 20% by weight, preferably less than 5% by weight of the coated
granules are less than 50 miti .
Preferably, the aqueous or organic solution used in step E 1 comprises, as binder, a
hydrophilic polymer preferably chosen from the group of cellulose derivatives
(hydroxypropylcellulose or ethylcellulose), povidone (polyvinylpyrrolidone or PVP),
sucrose, gums, starches, gelatin, macrogols (polyethylene glycols), which represents
approximately from 15% to 45% and preferably 20% to 40% by weight of the said
solution.
Preferably, the binder used in step E1 for the granulation is a hot-melt agent chosen
from Macrogols (PEG), sucroesters or poloxamers, and represents approximately from
0.2% to 20% and preferably from 1% to 15% by weight relative to the amount of active
principle to be granulated in step E1).
A hydrophilic polymer and in particular povidone is preferably used as binder.
According to one particular embodiment, the aqueous or organic solution used in
step E 1 is sprayed onto the fexofenadine mixed with a diluent (filler). The diluents used in
granulation to increase the charge to be granulated are preferably chosen from polyols,
celluloses, sugars, lactoses, starches, kaolin, calcium phosphates, calcium or magnesium
carbonates or derivatives thereof. According to one particular embodiment, the diluent is
chosen from starches, for instance corn starch. This diluent represents approximately
from 0 to 39% and preferably from 3% to 15% by weight of the composition. The said
diluent may optionally act as permeabilizer, thus facilitating the dissolution of the
fexofenadine.
Preferably, the fatty matrix is formed from C14 to C22 and preferably C16 to C18
long-carbon-chain saturated fatty acids, pure or as mixtures, and/or the corresponding
fatty alcohols thereof.
Preferably, the fatty matrix is formed from stearic acid, palmitic acid, myristic acid,
pure or as mixtures, and/or the corresponding fatty alcohols thereof. According to one
particular aspect, the fatty matrix is formed from stearic acid.
Preferably, the adjuvant mixed with the fatty matrix is chosen from the group of
surfactants (phospholipid, polysorbate, lauryl sulfate), hydrophilic excipients such as
sucrose, polyols, cellulose, lactose, silica, dicalcium phosphate, carbonates, starch,
macrogols, agents that 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 soya lecithin.
Preferably, the weight percentage of the adjuvant added to the fatty substance in
step E2 is less than 10% by weight, preferably less than 5% by weight, preferably ranging
from 1% to 3%, or even from 1% to 2%, by weight relative to the weight of the
composition.
Preferably, the weight percentage of the binder constituting the coating for the
granule obtained in step E 1 represents from 1% to 7% (or from 1% to 5%), more
particularly from 4% to 7%, by weight relative to the weight of the composition for a
hydrophilic polymer. According to one particular embodiment, the weight percentage of
the binder constituting the coating for the granule obtained in step E 1 represents from
0.2% to 18% for a hot-melt agent.
Preferably, the process is followed by a step E4 of formulation of the coated
granules obtained in step E3 with excipients such as diluents, fillers, viscosity modifiers,
disintegrants, dyes, sweeteners, salivating agents, flavourings, preserving agents, wetting
agents, effervescent agents, lubricants, buffers or sequestrants, for the manufacture of an
oral formulation in the form of a composition of granules to be swallowed for sachets,
granules for a drinkable suspension, granules for tablets or granules for orodispersible
tablets.
DETAILED DESCRIPTION OF EMBODIMENTS OF THE INVENTION
Process for preparing the fexofenadine composition
1) Granulation step
In a first step of the process, an aqueous or organic wetting solution comprising a
binder, preferably of hydrophilic polymer type, is sprayed onto the fexofenadine in crude
form or onto a fexofenadine/diluent mixture (filler) or onto a fexofenadine/lubricant mixture
or a fexofenadine/diluent/lubricant mixture, preferably onto a fexofenadine/diluent
mixture.
Preferably, the aqueous or organic solution contains from about 10% to 45% by
weight, preferably 15% to 40% by weight and advantageously 15% of binder, preferably
of hydrophilic polymer type, in the said solution.
The parameters used for this granulation step are adapted to the properties of
fexofenadine and the equipment used.
This step makes it possible to obtain finely granulated fexofenadine by
homogenization and recentring of the particle size distribution of fexofenadine, for the
purpose of improving the quality of the second coating step.
According to one variant, calibration of the fexofenadine in the form of granules
obtained in the above step may also be performed to select the granules with a diameter
of less than 500 m.
2) Coating step via the hot-melt process
In a second step, the fexofenadine in granulated form is preferably fluidized in a
fluidized-air bed.
The fatty matrix as described above is melted, with stirring, in a melting vessel at a
temperature about 10 to 20°C above its melting point.
The melting points of the fatty substances used are in the region of about 50 to
80°C, preferentially from 55 to 65°C or preferably about 60°C. This melting range was
preferentially chosen, on the one hand for a question of physical stability of the
composition thus formulated, and on the other hand so as to finally have the fastest
possible release of fexofenadine.
According to one preferred embodiment, an adjuvant (hydrophilic excipient or
surfactant) as described above is added to the melted fatty matrix, optionally with a
preserving agent. This adjuvant promotes the generation of a rapid release profile for the
composition.
The melted mixture is then sprayed onto the fexofenadine so as to produce a
coating via the hot-melt coating process. The parameters applied during the coating
process are summarized below.
The coating process may be performed in a fluidized-air bed apparatus.
The nozzles are fed, on the one hand, with the molten mixture that circulates via a
pump in an entirely insulated circuit and traced, on the other hand, with hot compressed
air fed in via an air heater.
The main operating parameters applied, which are adapted to the equipment used
and to the batch size used, are as follows:
- T° of the molten fatty substance: from 70 to 95°C, depending on the properties
and characteristics of the fatty substance;
- T° spraying compressed air: 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 adapted according to the size of the equipment.
For apparatus with a working capacity of 3 kg, an air flow rate of 50 to
160 m /h is generally used, depending on the filling charge of the equipment;
- T° inlet air: from 25 to 50°C, according to the properties of the fatty substance
used.
After these steps and after cooling, a fexofenadine composition comprising a granule
centre formed from fexofenadine grains aggregated in the presence of binder and a
coating layer for the said granule centre, formed from fatty substance, is obtained.
Description of the fexofenadine composition
Fexofenadine
The invention relates to any type of fexofenadine in the form of solid particles
intended to be coated to mask their unsatisfactory organoleptic or physicochemical
properties, in particular its strong bitterness.
Fexofenadine (lUPAC name: (RS)-4-(1-hydroxy-4-(4-(hydroxydiphenylmethyl)-1-
piperidyl)butyl )-a,a -dimethylbenzeneacetic acid) is a metabolite of terfenadine and is an
antihistamine of rapid and prolonged action acting selectively on the peripheral H 1
receptors. In hydrochloride form, it is used in the treatment of hay fever and similar
allergic rhinites, and also in the treatment of chronic idiopathic urticaria.
Active principle granulating agents
The granulating agents used in the first step of the process are binders preferably
chosen from hydrophilic agents. They are used in a proportion of from 0.2% (or 1%) to
18% by weight relative to the weight of the composition.
These hydrophilic agents are particularly chosen from the group of cellulose
derivatives (hydroxypropylcellulose), povidone (polyvinylpyrrolidone), sucrose, gums,
starches, gelatin, macrogols, sucroesters and poloxamers. Preferably, the binder is a
hydrophilic polymer and in particular povidone.
According to one embodiment, hydrophilic polymers are especially used, preferably
PEG or PVP in aqueous solution in a proportion of about 10% to 45% by weight in the
aqueous solution.
Preferably, when the binder is a hydrophilic polymer, the weight percentage of the
binder is less than 10% by weight, preferably less than 7% (or 5%) by weight, preferably
ranging from 4% to 7% by weight relative to the weight of the composition.
According to another embodiment, hydrophilic agents chosen from hot-melt agents
(melting point < 85°C), such as macrogols (PEG), sucroesters or poloxamers are used,
especially during the use of moisture-sensitive active principles. The concentrations of
hot-melt binders used are from about 0.2% to 20% and preferably from 1% to 15% by
weight relative to the amount of active principle to be granulated.
Preferably, when the binder is a hot-melt agent, the weight percentage of the binder
is less than 18% by weight, preferably less than 13.5% by weight relative to the weight of
the composition, and preferably from 0.2% to 13.5% by weight relative to the weight of
the composition.
The diluents used in granulation to increase the charge to be granulated or to
facilitate the dissolution of the active principle are preferably chosen from polyols,
celluloses, sugars, lactoses, starches, kaolin, calcium phosphates, calcium or magnesium
carbonates, or derivatives thereof. According to one particular embodiment, the diluent is
chosen from starches, for instance corn starch. These diluents are present in a proportion
of between 0 and 80% of the weight of the granule, which represents 0 to 78.8% by
weight relative to the weight of the composition. Preferably, these diluents are present in
a proportion of between 0 and 39% and preferably from 3% to 15% by weight relative to
the weight of the composition.
The lubricants used in granulation to improve the fluidization are preferably chosen
from silicas and talc. These lubricants are present in a proportion of between 0 and 2%
by weight of the granule, which represents 0 to 1.8% by weight relative to the weight of
the final composition.
Characteristics of fexofenadine in the form of granules
The granule comprising fexofenadine, the binder and optionally the diluent,
obtained after the first granulation step has a mean particle size of less than 500 miti and
preferably on average less than 200 m.
Fatty matrix
The fatty matrices are chosen from the group of C14 to C18 and preferably C16 to
C18 long-carbon-chain saturated fatty acids, pure or as mixtures, and/or the
corresponding fatty alcohols thereof and/or the corresponding esters of fatty acids and
alcohols. Preferably, the fatty matrix is formed from stearic acid, palmitic acid, myristic
acid, pure or as mixtures, and/or the corresponding fatty alcohols thereof. According to
one aspect of the invention, the fatty matrix is formed from stearic acid.
Preferably, the fatty matrix represents more than 10% by weight, preferably more
than 15% or more than 25% by weight or alternatively 50% or 60% by weight of the
composition and up to 85% by weight of the composition.
According to one preferred embodiment, stearic acid is used as fatty matrix in a
proportion of 50% or more, such as 60%, by weight relative to the weight of the
composition, to improve the masking of the taste of the very unpleasant molecules.
Fatty-matrix adjuvants
The adjuvants are chosen from the group of surfactants such as phospholipids,
polysorbate, lauryl sulfate, hydrophilic excipients such as sucrose, polyols, cellulose,
lactose, silica, dicalcium phosphate, starch, povidones, macrogols, agents that are
soluble at acidic pH such as methacrylic derivatives; phospholipids are preferably used.
Preferably, the adjuvant used is a glycerolipid, in particular a phospholipid. More
preferentially, this phospholipid is a lecithin (phosphatidylcholine), preferably soya
lecithin.
Preferably, the weight percentage of the adjuvant added to the fatty substance 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 from 1% to 3% by weight relative to the weight of the
composition.
According to one preferred embodiment, phospholipids, preferably lecithin (in
particular soya lecithin), are preferably used as adjuvant, in a proportion of from 1% to
3%, or even from 1% to 2%, by weight relative to the weight of the composition, to
improve their dissolution profile.
Characteristics of the fexofenadine composition :
Particle size
The particle sizes of the products resulting from this process are of the order of a
few hundred microns (depending on the parameters applied and the type of equipment
used).
The particle size distribution of the product obtained follows the following profile:
o less than 15% by weight of the coated granules are greater than 500 mi ;
o more than 80% by weight and preferably more than 90% by weight of the
coated granules are between 350 and 50 m h , and
o less than 20% by weight and preferably less than 5% by weight of the coated
granules are less than 50 mih.
Preferred amounts and ratio
The composition according to the invention is formed from fexofenadine comprising
(a) a granule centre formed from fexofenadine grains aggregated in the presence of
binder and (b) a coating layer for the said granule centre formed from fatty matrix.
In this composition, the preferred amounts and ratios of the various combinations of
ingredients are represented below:
> fexofenadine represents at least 10%, preferably 15% or even 20% by weight
relative to the weight of the composition; fexofenadine represents not more than
90% by weight, preferably not more than 60% or even not more than 50% by
weight relative to the weight of the composition; according to one embodiment,
fexofenadine represents less than 40% by weight relative to the weight of the
composition, and fexofenadine preferably represents from 20% to less than
40% relative to the weight of the composition,
> the fatty matrix represents more than 10% by weight, preferably from 50% to
85% by weight of the composition, preferably from 50% to 70% by weight of the
composition,
> the adjuvant, when it is present in the fatty matrix, represents less than 10% by
weight of the composition, preferably from 1% to 3%, or even from 1% to 2%, by
weight relative to the weight of the composition,
the binder, preferably a hydrophilic polymer or a hot-melt agent, represents less
than 18% (for a hot-melt agent) or even less than 5% (for a polymer) by weight
relative to the weight of the composition,
> the diluent, if necessary, as filler represents a proportion of from 0 to 78.8% by
weight relative to the weight of the composition,
> the lubricant, if necessary, as flow agent represents a proportion of from 0 to
1.8% by weight relative to the weight of the composition.
Properties
The composition or the final formulation containing it allows efficient masking of the
taste and odours of fexofenadine, which has unpleasant organoleptic properties.
Specifically, the coating of fexofenadine allows the creation of a barrier around it so as to
mask its bitter taste.
In parallel, products that show relatively rapid in vitro release of fexofenadine (for
example a minimum release of 70% in 60 minutes) are obtained.
Moreover, by virtue of the effective masking of the taste, products with a high dose
of fexofenadine may be obtained, for example containing more than 30% of fexofenadine,
which makes it possible to appreciably reduce the doses of products to be administered
to the patient, in particular to young children or the elderly.
Evaluation of the taste masking:
The taste masking performed by this coating may be evaluated qualitatively, by
means of taste tests performed by volunteers. The test consists of an oral administration
of the product (tablets or composition of granules to be swallowed). The administration
rules are as follows: do not take the test just after a meal (wait at least one hour), perform
the test in a calm, quiet environment, drink water between each test, wait at least
2 minutes between each test, fill in an evaluation form. The evaluation consists in grading
the disintegration time in the mouth, in specifying the mouthfeel (granular, pasty, etc.) and
in specifying the perception of the bitterness and optionally in adding comments.
in vitro dissolution/release:
The dissolution profiles of the composition obtained after the process are
determined according to the following method. The dissolution is performed with paddles.
The reagents used are: 0.001 M hydrochloric acid; acetonitrile and fexofenadine
hydrochloride: reference substance.
The procedure is as follows:
> Temperature: 37°C ± 0.5°C
Paddle speed: 50 rpm
> Dissolution medium: 0.001 M hydrochloric acid
> Dissolution volume: 900 ml
1 ml samples are collected on line in an HPLC vial at 5 , 10, 15, 30, 4 5 and
60 minutes. 2.7 m fibreglass filters are used. Two controls weighing 40.1 mg of
reference substance (fexofenadine hydrochloride) are prepared in a 200 ml flask. The
active principle is dissolved with 1 ml of acetonitrile and the volume is made up to the
graduation mark with 0.001 N HCI. Analysis of the dissolution samples are performed by
HPLC chromatography. Generally, the mean obtained corresponds to a mean of six tests
performed. The dissolution samples are injected as collected in a vial.
The chromatographic conditions are as follows:
> Column: Luna C18 100 x 3.0 mm (diameter 3 m )
Flow rate: 0.3 ml/minute
> Wavelength: 220 nm
> Injection: 4 mI
Column temperature: 30°C
> Mobile phase: 70V of 10 m ammonium acetate and 30V of acetonitrile
Formulation of the outer phase
The fexofenadine composition based on granules coated with fatty matrix according
to the invention may then be incorporated into an external formulation for the
manufacture of an oral form such as compositions of granules for a sachet to be placed
directly in the mouth and to be swallowed with or without water, in particular compositions
of granules to be swallowed for a single-dose sachet, granules for suspension, tablets for
chewing, tablets for sucking, tablets for swallowing or orodispersible tablets.
In the case of formulation in sachets, the formulation of the outer phase may be
enriched with surfactants or wetting agents so as to improve the resuspension of the
granules obtained in aqueous medium.
Other excipients such as fillers or diluents, dyes, sweeteners, viscosity modifiers or
gelling agents, adsorbents, buffers or flavourings, effervescent agents or salivating
agents may also be added to the formulation for the purpose of improving the final aspect
of the product.
The examples that follow illustrate the present invention without, however, limiting
its scope. The percentages are given on a weight basis, unless otherwise mentioned.
Examples
Preparation of fexofenadine granules coated with a fatty matrix
1. Description of the hot-melt process for obtaining the compositions according to
the invention
Fexofenadine and optionally corn starch are mixed together and fluidized in a
fluidized-air bed. After a few minutes of fluidization at an average flow rate of 80 mVh,
spraying is started at an average flow rate of 20 g/min. The granulation solution is
composed of water in which is dispersed povidone.
The inlet temperature is set at 65°C with an average flow rate of 20 g/min. Spraying
lasts for about 1 hour. The grain is then dried in a fluidized-air bed with an inlet air flow
rate of 80-100 m3/h and an inlet temperature of 65°C and an outlet temperature of about
45°C. The grain obtained is finely granulated and has a particle size predominantly less
than 200 m h . Stirring is continued throughout the spraying.
The fatty matrix formed from stearic acid is melted at 80°C. After homogenization of
the fatty substance, the phospholipid adjuvant is added to the molten fatty matrix to a
proportion of 1% to 5% depending on the formulation, until homogenization of the mass is
complete.
A few hundred grams of granulate are fluidized in the fluidized-air bed with an air
flow rate of 70 to 90 m /h (this flow rate is adapted as a function of the progress of the
step, i.e. as a function of the charge and of the density, acquired gradually by the grain).
The inlet air temperature during coating is set at between 30° and 40°C. The molten
mixture is then sprayed at a flow rate of 17 g/min on average. Once set, this flow rate
remains constant throughout the spraying. The spraying pressures used are also kept
constant and are between 0.5 and 0.9 bar. The spraying air used is heated to a target
temperature of 90°C. Depending on the formula, the spraying time varies. Once the
spraying is complete, the granule is cooled and then discharged.
2. Description of compositions according to the invention and results
Fexofenadine is granulated with 15% of PVP and coated with a proportion of 50%
to 60% of stearic acid. Corn starch is added to certain formulae and the proportion of
soya lecithin is also modified.
Formula 1: The proportion of soya lecithin is 5% in the coating solution. There is no
addition of starch, and the proportion of stearic acid coating is 50%.
Formula 2: Starch is added to 5% in the coating solution (which corresponds to 10% of
the amount of stearic acid). The proportion of soya lecithin is 1.5% and the proportion of
stearic acid coating is 50%.
Formula 3: The proportion of soya lecithin is increased to 5% in the coating solution and
the starch is at 5% in the coating solution (which corresponds to 10% of the amount of
stearic acid). The proportion of stearic acid coating is 50%.
Formula 4: Starch is added to 10% in the coating solution (which corresponds to 20% of
the amount of stearic acid). The proportion of soya lecithin is 1.5% and the proportion of
stearic acid coating is 50%.
Formula 5: The proportion of starch is added to 5% to the fexofenadine for the
granulation. The proportion of soya lecithin is 1.5% and the proportion of stearic acid
coating is 50%.
Formula 6: The proportion of starch is added to 5% to the fexofenadine for the
granulation. The proportion of soya lecithin is 1.5% and the proportion of stearic acid
coating is 60%.
Table 1 collates formulae 1-4 and Table 2 presents formulae 5 and 6.
Table 1
Table 2
3. Pharmaceutical compositions according to the invention
The percentages indicated below are expressed as total weight of the composition.
a) Preparation of granules or of a powder to be swallowed in a sachet:
PRODUCT 1
COMPONENTS % 30 mg 60 mg 120 mg 180 mg FUNCTION
Unit formula Unit formula Unit formula Unit
% Formula (mg) (mg) (mg) formula (mg)
Coated
fexofenadine 54 Coated active 8 1 162 324 486
granules principle
(formula 5)
Mannitol 17 25.5 5 1 102 153 Diluent
Xylitol 17 25.5 5 1 102 153 Diluent
Sweetener 2 3 6 12 18
Effervescent 7 10.5 2 1 42 63
agents
Flavourings 2 3 6 12 18
1 1.5 3 6 9
Flow agent
TOTAL 100.0 150.0 300.0 600.0 900.0
PRODUCT 2
COMPONENTS % 30 mg 60 mg 120 mg 180 mg FUNCTION
Percentage Unit formula Unit formula Unit formula Unit
formula (%) (mg) formula (mg) (mg)
(mg)
Coated
fexofenadine 68 102 204 408 Coated active 6 12
granules principle
(formula 6)
Mannitol 10.5 15.75 3 1.5 63 94.5 Diluent
Xylitol 10.5 15.75 3 1.5 63 94.5 Diluent
Sweetener 2 3 6 12 18
Effervescent 6.5 9.75 19.5 39 58.5
agents
Flavourings 1.5 2.25 4.5 9 13.5
Flow agent 1 1.5 3 6 9
TOTAL 100.0 150.00 300.0 600.0 900.0
The formulation of the external phase may vary especially in the following manner:
- Diluents: from 5% to 90%
- Flow agents: from 0 to 3%
- Viscosity modifiers: from 0 to 10%
- Effervescent agents: from 1% to 16%
- Sweeteners: from 0.5% to 5%
- Flavourings: from 0 to 5%
- Dyes: from 0 to 3%
- Buffers: from 0 to 3%
- Sequestrants: from 0 to 10%
The external phase is added to the coated granules manufactured according to the
invention to a proportion of 20% to 80%.
All the excipients of the external phase, with the exception of the lubricants, are mixed
with the coated granules. A lubrication phase is then optionally prepared before placing in
the sachet.
b) Preparation of tablets for chewing, swallowing or sucking:
The formulation of the external phase is as follows:
- Diluents: from 5% to 90%
- Lubricants: from 0.25% to 5%
- Sweeteners: from 0.2% to 5%
- Flavourings: from 0 to 5%
- Dyes: from 0 to 3%
The external phase is added to the coated granules manufactured according to the
invention to a proportion of 20% to 80%.
All the excipients of the external phase are mixed with the coated granules. The whole is
then tableted.
c) Preparation of orodispersible tablets:
The formulation of the external phase is as follows:
- Diluents: from 5% to 90%
- Disintegrants: from 2% to 20%
- Salivating agents: from 0 to 5%
- Lubricants or flow agents: from 0.25% to 5%
- Sweeteners: from 0.2% to 5%
- Flavourings: from 0 to 5%
- Dyes: from 0 to 3%
The external phase is added to the coated granules manufactured according to the
invention to a proportion of 20% to 80%.
All the excipients of the external phase are mixed with the coated granules. The whole is
then tableted.
d) Example of formulae of orodispersible fexofenadine tablets:
COMPONENTS Percentage formula (%)
Coated fexofenadine granule (formula 5) 54
Mannitol 28
Crospovidone (Kollidon CL) 5
Sweetener 1.5
Effervescent agents 5
Microcrystalline cellulose 5.0
Lubricant 1.50
TOTAL 100.00
COMPONENTS Percentage formula (%)
Coated fexofenadine granule (formula 5) 54
Mannitol 28
Crospovidone (Kollidon CL) 5
Sweetener 1.5
Effervescent agents 5
Flavourings 0.5
Microcrystalline cellulose 4.5
Lubricant 1.5
TOTAL 100.0
For these three formulae, all the excipients of the external phase are mixed with the
coated granules. The whole is then tableted.
4. Results of the tests performed
The protocols used for obtaining the results below are as described previously.
* : Variable taste perception according to the type of flavourings used
- Dissolution profiles of products 1, 2 and tablets Telfast® (Allegra®) 180 mg are collated
in the following tables.
Product 2
Time (min) Mean CV
0 0 0
5 43 18.5
10 58 11.6
15 65 9.5
30 74 6.1
45 78 4.7
60 80 4.5
Telfast (or Allegra) ® 180 mg
"CV": represents the Coefficient of Variation, which is the ratio of the standard deviation
to the mean obtained.
Conclusions
It may be noted that the addition of an adjuvant to the formulation in the fatty
matrix, such as phospholipid (lecithin) added to a proportion of a few per cent, for
instance from 1% to 3%, makes it possible to accelerate the dissolution.
In the absence of lecithin, a slowed dissolution profile is observed, the presence of
1.5% makes it possible to improve the dissolution kinetics and increasing the proportion
to 5% does not afford any improvement. The optimum proportion in the specific example
studied is of the order of .5%.
It may also be noted that the addition of a diluent also acting as permeabilizer to
the formulation during granulation (step E1), added to a proportion of a few per cent, for
instance from 3% to 10%, makes it possible to accelerate the dissolution. The addition of
corn starch as diluent or permeabilizer thus improves the dissolution kinetics. The
addition of 10% starch does not afford a better result than at 5%. The addition of this
agent is preferable during step E 1 (granulation) compared with the introduction of this
adjuvant to the coating solution.
CLAIMS
1. Fexofenadine composition comprising (a) a granule centre formed
from active principle grains aggregated in the presence of a binder and optionally of
a lubricant or preferably of a diluent, and (b) a layer for coating the said granule
centre formed from a fatty matrix, in which composition
• the fexofenadine represents at least 10%, preferably 15% or even 20% by
weight relative to the weight of the composition; the active principle
represents not more than 90%, preferably not more than 60% or 50% by
weight relative to the weight of the composition, or even less than 40% by
weight relative to the weight of the composition, preferably the active
principle represents from 20% to 40% relative to the weight of the
composition;
• the fatty matrix represents more than 10% by weight, preferably from 50% to
85% by weight of the composition, the fatty matrix optionally comprising an
adjuvant, preferably chosen from hydrophilic agents, surfactants or mixtures
thereof, and these adjuvants representing less than 10% by weight of the
composition and preferably from 1% to 3% by weight relative to the weight of
the composition;
• the binder, preferably a hydrophilic agent chosen from hydrophilic polymers
and hot-melt agents, represents from 0.2% to 18% by weight relative to the
weight of the composition, preferably the binder represents less than 18% by
weight for a hot-melt agent, or even, preferably, the binder represents less
than 10% by weight for a hydrophilic polymer relative to the weight of the
composition;
• the diluent, if necessary, as filler represents a content of from 0 to 78.8%,
preferably from 0 to 39% and preferably from 5% to 15% by weight relative to
the weight of the composition;
• the lubricant, if necessary, as flow agent represents a content of from 0 to
1.8% relative to the weight of the composition.
2. Fexofenadine composition according to Claim 1, in which the said fatty matrix is
formed from C14 to C22 and preferably C16 to C18 long-carbon-chain saturated
fatty acids, pure or as mixtures, and/or the corresponding fatty alcohols thereof,
and the binder is chosen from hydrophilic polymers.
3. Fexofenadine composition according to Claim 2, in which the said fatty matrix is
formed from stearic acid.
4. Fexofenadine composition according to one of Claims 1, 2 and 3, in which the said
fatty matrix comprises an adjuvant chosen from the group of surfactants
(phospholipid, polysorbate, lauryl sulfate), hydrophilic excipients such as sucrose,
polyols, cellulose, lactose, silica, dicalcium phosphate, carbonates, starch,
macrogols, agents that are soluble at acidic pH (methacrylic derivatives), pure or
as mixtures, preferably phospholipids.
5. Fexofenadine composition according to Claim 4, in which the adjuvant is soya
lecithin.
6. Fexofenadine composition according to one of Claims 1 to 5, in which the adjuvant
is a surfactant that represents less than 10% by weight, preferably less than 5% by
weight, preferably from 1% to 3%, or even from 1% to 2%, by weight relative to the
weight of the composition.
7. Fexofenadine composition according to one of Claims 1 to 6, in which the binder is
povidone and the diluent is corn starch.
8. Fexofenadine composition according to one of Claims 1 to 7, in which the amount
of fexofenadine represents more than 10% by weight and ranges up to 90% by
weight relative to the weight of the composition.
9. Fexofenadine composition according to one of Claims 1 to 8, in which the amount
of fexofenadine represents more than 10% by weight of the composition and the
fatty matrix comprises an adjuvant.
10. Process for preparing a fexofenadine composition as defined according to one of
Claims 1 to 9, the said process comprising the steps of:
E1) preparation of the granule centre by spraying an aqueous solution, an organic
solution or a mixture thereof comprising a binder or by spraying a molten binder
onto the fexofenadine alone or as a mixture with a lubricant and/or preferably a
diluent;
E2) coating by spraying onto the granules a fatty matrix melted beforehand in a
melting vessel at a temperature from about 10 to 20°C above its melting point;
E3) cooling of the composition obtained.
11. Process for preparing a composition according to Claim 10, in which:
• fexofenadine represents at least 10% and not more than 90%, preferably
from 20% to 50%, and
• the fatty matrix comprising an adjuvant represents more than 10% by
weight, preferably 50% and up to 85% by weight of the composition.
12. Process for preparing a composition according to Claim 10, in which:
• fexofenadine represents less than 40% by weight, preferably from 20%
to 40% and advantageously from 30% to 40% relative to the weight of
the composition, and
· the fatty matrix represents more than 10% by weight, preferably 50%
and up to 85% by weight of the composition, advantageously from 50%
to 60% by weight of the composition.
13. Process according to one of Claims 10 to 12, in which the size of the coated
granules obtained after step E3) is less than 500 pm, preferably less than 350 pm,
preferably ranging from 50 to 350 pm.
14. Process according to one of Claims 10 to 13, in which the particle size of the final
product obtained at step E3) is distributed according to the following range:
• less than 15% by weight of the coated granules are greater than 500 pm;
more than 80% by weight, preferably more than 90% by weight, of the coated
granules are between 350 and 50 m, and;
• less than 20% by weight, preferably less than 5% by weight, of the coated
granules are less than 50 pm.
5. Process according to one of Claims 10 to 14, in which the aqueous or organic
solution used in step E 1 comprises, as binder, a hydrophilic polymer, preferably
chosen from the group of cellulose derivatives (hydroxypropylcellulose or
ethylcellulose), povidone (polyvinylpyrrolidone), sucrose, gums, starches, gelatin,
macrogols (polyethylene glycols), which represent approximately from 15% to 45%
and preferably 20% to 40% by weight of the said solution.
16. Process according to one of Claims 10 to 15, in which the aqueous or organic
solution used in step E1 sprayed onto the fexofenadine is mixed with corn starch.
17. Process according to one of Claims 10 to 16, in which the weight percentage of the
binder constituting the coating of the granule obtained in step E1 represents from
1% to 7% by weight relative to the weight of the composition for a hydrophilic
polymer.
18. Process according to one of Claims 10 to 17, followed by a step E4 of formulation
of the coated granules obtained in step E3 with excipients such as diluents, fillers,
viscosity modifiers, disintegrants, dyes, sweeteners, salivating agents, flavourings,
preserving agents, wetting agents, effervescent agents, lubricants, buffers and
sequestrants for the manufacture of an oral formulation in the form of a
composition of granules to be swallowed for sachets, granules for a drinkable
suspension, granules for tablets or granules for orodispersible tablets.
19. Fexofenadine composition that may be obtained according to the process
described in one of Claims 10 to 18.
20. Pharmaceutical composition comprising the fexofenadine composition as
described in one of Claims 1 to 9 or as may be prepared according to the process
as described in one of Claims 10 to 18.
2 . Composition according to Claim 20, characterized in that it is in the form of a
sachet comprising a composition of granules to be swallowed or a sachet for a
drinkable suspension and characterized in that it contains one or more excipients,
preferably chosen from diluents, viscosity modifiers, sequestrants, buffers,
preserving agents, lubricants, wetting agents, effervescent agents, dyes,
sweeteners, salivating agents and flavourings, and mixtures thereof.
22. Composition according to Claim 20, characterized in that it is in the form of tablets,
to be chewed, swallowed or sucked, or orodispersible tablets with masked taste,
and characterized in that it contains one or more excipients, preferably chosen
from diluents, binders, lubricants, salivating agents, anaesthetics, wetting agents,
preserving agents, disintegrants, dyes, sweeteners, flavourings, and mixtures
thereof.
23. Sachet or tablet according to Claim 2 1 or 22, characterized in that the weight ratio
of the fexofenadine composition as defined according to one of Claims 1 to 9
relative to the weight amount of excipient in the sachet or tablet ranges from 0.2 to
0.8.
24. Use of a fexofenadine composition as defined in one of Claims 1 to 9 or prepared
according to the process of any one of Claims 10 to 18, for the preparation of a
pharmaceutical composition that is in the form of sachets comprising a composition
of granules to be swallowed or for a drinkable suspension, tablets to be chewed,
tablets to be swallowed, tablets to be sucked, or orodispersible tablets with
masked taste.
| # | Name | Date |
|---|---|---|
| 1 | 3077-Kolnp-2012-(11-10-2012)GPA.pdf | 2012-10-11 |
| 1 | 3077-KOLNP-2012-AbandonedLetter.pdf | 2019-01-03 |
| 2 | 3077-KOLNP-2012-FER.pdf | 2018-04-16 |
| 2 | 3077-Kolnp-2012-(11-10-2012)FORM-5.pdf | 2012-10-11 |
| 3 | 3077-KOLNP-2012-FORM-18.pdf | 2014-05-21 |
| 3 | 3077-Kolnp-2012-(11-10-2012)FORM-3.pdf | 2012-10-11 |
| 4 | 3077-KOLNP-2012-(01-04-2013)-ASSIGNMENT.pdf | 2013-04-01 |
| 4 | 3077-Kolnp-2012-(11-10-2012)FORM-2.pdf | 2012-10-11 |
| 5 | 3077-Kolnp-2012-(11-10-2012)FORM-1.pdf | 2012-10-11 |
| 5 | 3077-KOLNP-2012-(01-04-2013)-CORRESPONDENCE.pdf | 2013-04-01 |
| 6 | 3077-Kolnp-2012-(11-10-2012)CORRESPONDENCE.pdf | 2012-10-11 |
| 6 | 3077-KOLNP-2012-(01-04-2013)-FORM 3.pdf | 2013-04-01 |
| 7 | 3077-KOLNP-2012.pdf | 2012-11-06 |
| 7 | 3077-KOLNP-2012-(01-04-2013)-OTHERS.pdf | 2013-04-01 |
| 8 | 3077-KOLNP-2012.pdf | 2012-11-06 |
| 8 | 3077-KOLNP-2012-(01-04-2013)-OTHERS.pdf | 2013-04-01 |
| 9 | 3077-Kolnp-2012-(11-10-2012)CORRESPONDENCE.pdf | 2012-10-11 |
| 9 | 3077-KOLNP-2012-(01-04-2013)-FORM 3.pdf | 2013-04-01 |
| 10 | 3077-KOLNP-2012-(01-04-2013)-CORRESPONDENCE.pdf | 2013-04-01 |
| 10 | 3077-Kolnp-2012-(11-10-2012)FORM-1.pdf | 2012-10-11 |
| 11 | 3077-KOLNP-2012-(01-04-2013)-ASSIGNMENT.pdf | 2013-04-01 |
| 11 | 3077-Kolnp-2012-(11-10-2012)FORM-2.pdf | 2012-10-11 |
| 12 | 3077-KOLNP-2012-FORM-18.pdf | 2014-05-21 |
| 12 | 3077-Kolnp-2012-(11-10-2012)FORM-3.pdf | 2012-10-11 |
| 13 | 3077-KOLNP-2012-FER.pdf | 2018-04-16 |
| 13 | 3077-Kolnp-2012-(11-10-2012)FORM-5.pdf | 2012-10-11 |
| 14 | 3077-KOLNP-2012-AbandonedLetter.pdf | 2019-01-03 |
| 14 | 3077-Kolnp-2012-(11-10-2012)GPA.pdf | 2012-10-11 |
| 1 | 3077abc_04-04-2018.pdf |