Title of Invention

MICROGRANULES BASED ON ACTIVE PRINCIPLE AND METHOD FOR MAKING SAME

Abstract A method for making the micro-granule consisting of a core coated with at least one coating layer, said coated core comprising at least one active principle, the core and said coating layer each contain between 80 and 95% by weight of active principle, the balance for 100% consisting of at least one binder, and in that the coated core has substantially spherical shape, whose median size is less then 500 urn, said method comprising: in a first step, spraying onto the individualized particles of active principle maintained in suspension in a fluidized bed a granulation solution comprising at least one binder in a solvent until a core is obtained; and then in a second step, coating the core formed by spraying a coating suspension or solution based on particles of active principle and binder the coated core obtained then having a substantially spherical shape.
Full Text The invention relates to a microgranule consisting of a coated core comprising at least one active principle. It also relates to a method for making said microgranule and to the pharmaceutical compositions containing a plurality of said microgranule.
The document WO 95/22319 describes a method for making by extrusion/spheronization fine particles based on an active principle. The fine particles obtained have a size of between 50 urn and 1 mm. In particular, the examples describe particles having a size equal to 300 urn, comprising up to 72% of active principle in the presence of at least three excipients including in particular an extrusion agent. In addition, these same examples and in particular formula 1 c shows that this method does not make it possible to obtain fine particles of this order of size with a high concentration of active principle, .equal to 95%. Finally, the fine particles obtained at the end of the method have a surface which is too irregulator to allow subsequent satisfactory treatment, the coating designed to mask the taste of the active principle requiring, for example, a high level of coating.
The document EP-A-443572 describes a coating composition which can be applied in various forms and in particular microgranules designated here by the expression "fine granules'. It is indicated that at least 75% of the population of microgranules have a size of between 1 and 500 µm. No information is given relating to the concentration of active principle in the microgranule.
The document FR-A-2 419 722 describes microgranules of active principle and in particular of ferritin and their method of preparation. These microgranules consist of a core comprising a first coating obtained by spraying an aqueous suspension of active principle, the cohesion of said first coating with the core being brought about by uniform dispersion, between each spraying step, of small quantities of talc (see in particular page 7, example 3) . The core thus coated has, in addition, a second coating, whose nature depends on the characteristics of release of the desired active principle. In practice, the core itself can have two different forms. Thus, in a first embodiment, the core consists exclusively of inert material, for example of the sucrose type. In a second embodiment, (example 3), the core exists in the form of a granule based on a binder (for example starch) and an active principle in ratios of 50/50.
The method of manufacture and the microgranule thus obtained exhibit a number of disadvantages. As regards first of all the method of manufacture, it requires at least four steps, which are the manufacture of the core, and then, alternatively, the application of the first coating, and of the talc dispersion and finally the application of the second coating. Such a method is particularly long and cannot be performed continuously. In addition, the cohesion of the first coating onto the core is not always homogeneous, leading to coated ceres having an irregular surface and thereby increasing the quality of material necessary for the second coating. As regards the microgranule as such, it is indicated that the core before coating has a size of between C.3 and 0.5 millimeters (see examples) for a concentration of active principle representing only 50% of the mass of the core.
Accordingly, the first problem which the invention proposes to solve is to provide microgranules whose core, before coating of the functional layer(s) conferring on the microgranule the desired characteristics of release of the active principle and/or of masking the taste, is as concentrated as possible in active principle.
The second problem which the invention proposes to solve is to provide a microgranule whose nucleus, before coating the functional layer(s), is appreciably spherical so as to reduce its specific surface and thus reduce the quantity of material necessary for subsequent coating.
The third problem which the invention proposes to solve is to provide a microgranule whose nucleus, before coating the functional layer(s), has a size which is as small as possible, advantageously a median size of less than 5 00 urn.
The subject of the invention is therefore a microgranule consisting of a core coated with at least one coating layer, said coated core comprising at least one active principle.
This microgranule is characterized in that the core and said coating layer each contain between 80 and 95% by weight of active principle, the balance for 100% consisting of at least one binder, and in that the coated core has a substantially spherical shape.
Below an active principle concentration of 80%, the microgranule titer is not sufficient and the proportion of binder is too high, leading to the size of the microgranule being increased. For a concentration greater than 95%, the cohesion between the particles of active principle is not satisfactory because of the extremely low proportion of binder.
In a preferred embodiment, the core and the coating layer each contain 85 and 93%, advantageously 90% by weight of active principle.
In an advantageous embodiment, the balance for 10 0% by weight of the core and of the coating layer consists exclusively of a binder.
The choice of "binder' will be determined as a function not only of its capacity to bind the particles of active principle to each other in the coated core, but also of the desired functional characteristics of the .coated core, whether in the presence or in the absence of subsequent functional coating. The expression "functional characteristics" denotes in particular, but without limitation, the properties of masking of taste and/or of release (modified or otherwise) of the active principle.
These characteristics depend:
• on the one hand, on the physicochemical characteristics of the binder used (solubility, permeability, glass transition temperature, and the like);
• and on the other hand, on the nature of the active principle (solubility, bitterness, and the like).
In .other words, before any subsequent functional coating, the microgranule of the invention already has specific characteristics thus making it possible to reduce the thickness of the subsequent coating and therefore the size of the final microgranule.
In practice, the binder is chosen from the group comprising ethyl cellulose, hydroxypropyl cellulose (HPC) , carboxymethyl cellulose (CMC), hydroxypropyl methyl cellulose (HPMC), acrylic polymers, methacrylic polymers, amonio-methacrylate copolymer, polyacrylate, methacrylic acid copolymer and polyvinylpyrrolidone.
According to another characteristic, the binder contained in the coating layer and that contained in the core may be identical or different.
As already stated, another objective of the invention is to reduce the size of the coated microgranule before coating the optional subsequent functional layer. The high titer of the microgranules of the invention makes it possible to partially fulfill this objective. To further reduce the size of the microgranules, the size of the particles of active principle varies between 10 and 3 0 µ .
In practice, the size of the coated microgranules of the invention before optional subsequent coating is less than 500 µm, advantageously between 200 and 3 00 µm.
Of course and as already stated, the coated core constituting the microgranule of the invention may comprise an additional functional coating, in general of polymeric origin, whose nature will depend on the desired characteristics of the final formulation and in particular of masking taste and/or of modified or unmodified release of active principle.
Because of the specific method of production which will be described later, the microgranules of the invention have, in addition, the advantage of being substantially spherical, thus having a reduced specific surface area which makes it possible to coat a subsequent layer of raw material in reduced quantities compared with the known microgranules of the prior art. This subsequent layer preferably comprises a polymer whose application to the microgranules will make it possible to obtain the desired final characteristics.
Moreover, the microgranules of the invention may be used in various galenic forms such as in particular sachets, gelatin capsules, liquid suspensions, suspensions intended for reconstitution immediately before use. They can also enter into the composition of tablets which are orodispersible or not. In this regard, the reduced size of the microgranules of the invention makes it possible to reduce the proportion of compression excipients (for example the diluents) necessary for producing a homogeneous mixture before compression, which makes it possible to have a final form of smaller size and weight compared with known tablets of the same size and to also reduce the compression forces.
In this regard, the invention relates more particularly to fast disintegrating multiparticulate type tablets such as those described by the applicant in the document FR-A-2 679 451, and fast dispersible type tablets comprising the microgranules described above.
The subject of the invention is also the method for making the microgranules described above according to which:
♦ in a first step, a granulation solution comprising at least one binder in a solvent is sprayed onto the individualized particles of active principle maintained in suspension in a fluidized bed until a core is obtained;
♦ and then, in a second step, the core formed is coated by spraying a coating suspension or solution based on particles of active principle and binder, the coated core obtained then having a substantially spherical shape.
In an advantageous embodiment, a step for drying the cores obtained is intercalated between the first and the second step.
According to another characteristic, the method may be performed continuously or batchwise.
Of course, the solvent in which the binder is dissolved will be determined as a function of the actual nature of the binder and will be chosen from aqueous or organic solvents, alone or in combination.
To solve the problem posed of obtaining coated cores whose size is as small as possible, in any case below 50 0 micrometers, preferably below 350 micrometers, the size of the particles of active principle used in the first step is between 10 and 30 micrometers, advantageously 25 micrometers, while the size of the particles of active principle used in the second step is between 10 and 20 micrometers, advantageously below 15 micrometers.
Of course, such sizes of particles of active principle may be obtained by any methods known to persons skilled in the art, in particular micronization or grinding.
In an advantageous embodiment, the size of the particles of active principle used in the first step is identical to the size of those used in the second step.
To check, during the method of manufacture, the size of the microgranules as a function of the titer of active principle, the active principle/binder ratio is constant during the first and second steps, advantageously equal to 90/10. Consequently, the second step may be stopped as soon as the desired size of the microgranule, below 500 µm, has been reached.
According to another characteristic, in a third step, at least one additional coating solution is sprayed, whose composition is chosen as a function of the characteristics of masking of taste and/or of release of active principle desired.
As already stated, the method of the invention is formed in a fluidized bed, advantageously by a bottom spray technique. The parameters of the fluidized bed (pressure, spraying rate, and the like) do not exhibit particular characteristics and will be adjusted in the customary manner by persons skilled in the art.
The invention and the advantages resulting therefrom will emerge more clearly from the following exemplary embodiments given by way of illustration and without limitation.
Example 1 ; Manufacture of microgranules of ibuprofen
a) Composition of the coated core
- ibuprofen 1 600 g
- HPMC 606* 160 g
* manufactured by SHIN-ETSU
b) Preparation of the granulating solutions and
coating suspension
- Granulating solution
40 g' of HPMC 606 are introduced into 360 g of purified water, with stirring until complete dissolution of the hydroxymethyl propyl cellulose is obtained.
- Coating suspension
i 200 g of micronized ibuprofen (25 µ) and 120 g of HPMC 606 in 3 080 g of purified water are mixed together, with constant stirring .until complete dissolution of the hydroxypropyl methyl cellulose is obtained.
c) Manufacture of the coated core
400 g of ibuprofen having a particle size equal to 25 micrometers are introduced into a fluidized bed apparatus of the GLATT GPCG 1 type equipped with a Bottom Spray tank, while the active principle is kept at a temperature sufficient to avoid sticking together while the mass is kept moist.
The granulating solution prepared above is then sprayed until a core having a median particle size of about 100 micrometers is obtained.
After drying the core thus formed, the active principle-based coating suspension is continuously sprayed until a granule is obtained which has a median particle size of between 250 and 300 micrometers.
d) Functional coating
A polymeric dispersion of ethyl cellulose and HPMC and syloid is applied to the coated core in order to mask the taste of the active principle.
EXAMPLE 2 : Manufacture of microgranules of tinidazole
a) Composition of the coated core
- tinidazole 1 600 g
- Eudragit® E 100 160 g
b) Manufacture of the coated core
Example 1 is repeated, replacing HPMC with Eudragit® E 100 and purified water with ethanol.
The Eudragit® is chosen as binder, but also for its function as agent masking the taste' of the active principle, while allowing its immediate release. This
thereby makes it possible to improve the masking of the taste from the granulation step, before the optional functional coating step.
EXAMPLE 3 : Manufacture of microgranules of doxycyclin
a) Composition of the coated core
- doxycyclin 15 kg
- PVP K90 1.5 kg
b) Preparation of the granulating solutions and
coating suspension
- Granulating solution
Preparation of a granulating solution of PVP K90 at 5% (w/w) in ethanol.
- Coating suspension
25 kg of the solution of PVP K90 at 5% in ethanol obtained above are collected and 10 kg of doxycyclin (10 u) in 23.75 kg of ethanol are added thereto.
' c) Manufacture of the coated core
5 kg of doxycyclin (10 µ) are introduced into a fluidized bed apparatus of the GLATT GPCG5 type equipped with a bottom spray tank and a 12" nozzle.
The granulating solution obtained above is then sprayed. After drying the core thus formed, the active principle-based coating suspension is sprayed continuously until a granule having a median particle size of about 257 urn is obtained.
d) Functional coating
A polymeric solution of Eudragit® El00 (manufactured by Rohm) at 12.5% (w/w) in ethanol is sprayed on the coated cores. The equivalent of 10% (w/w calculated as
dry polymer) of the mass of the coated cores is applied
for masking taste.
The invention and the advantages resulting therefrom are clearly evident from the description.
The possibility of making coated microgranules whose coated core has a very small size, below 300 micrometers, facilitating the functional coating and subsequent forming, will be noted in particular.






We claim:
1. A method for making the micro-granule consisting of a core coated with
at least one coating layer, said coated core comprising at least one
active principle, the core and said coating layer each contain between
80 and 95% by weight of active principle, the balance for 100% consisting
of at least one binder, and in that the coated core has substantially
spherical shape, whose median size is less then 500 urn, said method
comprising:
• in a first step, spraying onto the individualized particles of active principle maintained in suspension in a fluidized bed a granulation solution comprising at least one binder in a solvent until a core is obtained;
• and then in a second step, coating the core formed by spraying a coating suspension or solution based on particles of active principle and binder the coated core obtained then having a substantially spherical shape.

2. The method as claimed in claim 1 wherein a step for drying the cores obtained is intercalated between the first step and the second step.
3. The method as claimed in claim 2, wherein the size of the particles of active principle used in the first step is between 10 and 30 micrometers, advantageously 25 micrometers while the size of the particles of active principle used in the second step is between 10 and 20 micrometers, advantageously below 15 micrometers.
4. The method as claimed in claim 3, wherein the size of the particles of active principle used in the first step is identical to that of the particles used in the second step.
5. The method as claimed in claim 4, wherein the active principle/binder ratio is constant throughout and first and second steps.
6. The method as claimed in claim 5, wherein the second step is performed until the desired size of the coated microgranule is obtained.
7. The method as claimed in claim 6, wherein in a third step, at least one additional coating solution is sprayed whose composition is chosen as a function of the characteristics of masking of taste and /or of release of active principle desired.
8. The method as claimed in claim 1, wherein the balance for 100% by weight of the core and of the coating layer consisting exclusively of binder.

9. The method as claimed in claim 1, wherein the binder contained in the core and the binder contained in said coating layer are identical.
10. The method as claimed in claim 1, wherein the binder contained in the core and the binder contained in said coating layer are different.
11. The method as claimed in claim 1, wherein the binder is chosen from the group comprising ethyl cellulose, hydroxypropyl cellulose (HPC), carboxymethyl cellulose (CMC), hydroxypropyl methyl cellulose (HPMC), acrylic polymers, methacrylic polymers, amonio-methacrylate copolymer, polyacrylate, methacrylic acid copolymer and polyvinylpyrrolidone.
12.The method as claimed in claim 1, wherein the size of the particles of active principle varies between 10 and 30 urn.
13.The method as claimed in claim 1, wherein the coated core comprises an additional functional layer whose composition is chosen according to the characteristics of masking taste and /or of release of active principle desired.
14. The method as claimed in claim 1 as and when used in fast disintegrating multiparticulate tablet fast dispersible tablet, suspension in dry or liquid forms and gelatin capsules.
15.A microgranule consisting of a core coated with at least one coating layer substantially as and when prepared by the method as claimed in any preceding claim
16. A method for making the microgranule substantially as herein described with reference to the foregoing examples.

Documents:

704-delnp-2003-abstract.pdf

704-delnp-2003-assignment.pdf

704-delnp-2003-claims.pdf

704-delnp-2003-correspondence-others.pdf

704-delnp-2003-correspondence-po.pdf

704-delnp-2003-description (complete).pdf

704-delnp-2003-form-1.pdf

704-delnp-2003-form-18.pdf

704-delnp-2003-form-2.pdf

704-delnp-2003-form-3.pdf

704-delnp-2003-form-5.pdf

704-delnp-2003-gpa.pdf

704-delnp-2003-pct-210.pdf

704-delnp-2003-petition-137.pdf

704-delnp-2003-petition-138.pdf


Patent Number 246093
Indian Patent Application Number 704/DELNP/2003
PG Journal Number 07/2011
Publication Date 18-Feb-2011
Grant Date 14-Feb-2011
Date of Filing 05-May-2003
Name of Patentee ETHYPHARM
Applicant Address 21 RUE SAINT MATHIEU, F-78550, HOUDAN, FRANCE
Inventors:
# Inventor's Name Inventor's Address
1 BRUNA ETIENNE 13 RUE DES PARIGAUDES, F-28300 JOUY, FRANCE
2 GENDROT EDOUARD 24 RUE DE DREUX, F-28500 GARNAY, FRANCE
3 COUSIN GERARD 1 RUE DU GUE, LE MESNIL PONCEAU, F-28210 VILLEMEUX, FRANCE
PCT International Classification Number A61K 9/16
PCT International Application Number PCT/FR01/03584
PCT International Filing date 2001-11-15
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 00.14803 2000-11-16 France