PROCESS FOR PREPARING ETOFIBRATE OR SIMILAR COMPOUNDS CONTAINING SUSTAINED RELEASE MICROGRANULES AND PRODUCTS THUS OBTAINED

Abstract: The present invention relates to the pharmaceutical field and particularly to the manufacturing of a pharmaceutical product named etofibrate in the form of sustained release microgranules, wherein each microgranule consists entirely of an etofibrate composition and polyethylene glycol 4000, said microgranules being placed in capsules that, size of known capsules being equal, display an higher concentration of the active ingredient, the process for preparing the above microgranules comprising mainly the manufacturing of a compound consisting of etofibrate and solvent, wherein said compound is obtained in rotatory pan, then submitting this compound to a first sieving, placing it again in rotatory pan, drying the product thus obtained and sieving it once more, separating the microgranules which are replaced in the rotatory pan and then coated in rotatory pan with further etofibrate added with a suitable amount of polyethylene glycol 4000 to give, after a last sieving, the desired microgra­ nules whose size corresponds to the requested size and is normally comprised between 400 and 2000 microns.

Description: The present invention relates to a new composition of etofibrate microgranules which are differently formulated and differently manufactured in comparison to the already available product. Etofibrate is in fact a known compound having the following pharmacological properties: it reduces hyperlipidemia, hypertriglyceridemia and hypercholesterolemia. Said etofibrate is a compound corresponding to the chemical name 2-(p-chlorophenoxy) - 2 - methylpropionic acid [2-(nicotinoyloxy)-ethyl] - ester . This product is on the market since many years and is available in form of hard "00" type gelatine capsules containing 500 mg of etofibrate as sustained release microgranules. These capsules, with a capacity of 0.95 ml, are able to contain the above microgranules which are composed of an inert material inner core coated with a spheroidal layer of active ingredient comprising etofibrate and polyethylene glycol 4000, also known on the market as polyglycol 4000. This result, that has been achieved by means of particular per se known processes, entails each microgranule to have a concentration ranging from 67 to 75% of active ingredient, as even each microgranule consists also of an inert material inner core with a diameter of 850-500 microns comprising from 65 to 90% of sucrose and from 10 to 35% of corn starch. The presence in each microgranule of an inner core binds evidently to use the above "00" type capsules, being only these capsules able to contain the mentioned dosage of 500 mg per capsule. Aim of the present invention was to obtain an higher concentration of etofibrate, so that the 500 mg standard dosage might be placed in smaller gelatine capsules. In each capsule an higher dosage of 750 mg of active ingredient may also be included. It is therefore possible to have the 500 mg standard dosage placed not in the "00" type capsules but rather in a "0" type capsule (0.68 ml), thus evidently facilitating its deglutition. Because of components percentage and of its particular constitution, this composition allows a sustained release of the drug and eliminates the well-known flash, characteristic side-effect of etofibrate. Further aim of the present invention was to prepare spherical microgranules by means of simple procedures, said microgranules having a diameter ranging from 400 to 2000 µm (microns) and an etofibrate concentration of 88-98%, in other words spherical microgranules without inert core and, therefore, with an higher concentration of active ingredient. This and other aims have been achieved with the present invention, characterized in that the provided process comprises the following manufacturing features: preparation in rotatory pan of a compound consisting of etofibrate and solvent, said compound being then submitted to a first sieving and replaced in rotatory pan, the product being subsequently dried and resieved, the microgranules being separated and then introduced in rotatory pan, wherein the microgranules thus obtained are coated with further etofibrate added with a suitable percentage of polyethylene glycol 4000 to give, after a last sieving, the ultimate microgranules having a size corresponding to the requested size and which is normally comprised between 400 and 2000 µm. The product obtained with the above process consists at contrary of a "O" type (0.68 ml), or "O" extended type (0.80 ml) or of a "00" type capsule (0.95 ml) containing respectively 500, 600 or 750 mg of active ingredient, wherein said active ingredient consists of several microgranules having a diameter between 400 and 2000 µm, each microgranule comprising an etofibrate inner core and an outer coat of etofibrate added with polyethylene glycol 4000, wherein the total percentage of etofibrate is comprised between 89 and 98%, whereas the total percentage of polyethylene glycol 4000 ranges from 11 and 2% respectively. In WO-A- 8 303 353 an ingestible granulated psyllium composition is described consisting essentially of granules of psyllium powder, wherein the psyllium is rendered substantially instantly and uniformly dispersible in water by the presence on the surface of the psyllium particles of a coating of an amount from up to about 10% by weight of a non-toxic, normally solid, alcohol soluble, water dispersible polyethylene glycol, polyvinylpyrrolidone or mixture thereof. DE-1 492 128 teaches the synthesis of pharmaceutical oral controlled release compositions, wherein a crystalline, spherical active ingredient is moistened in a rotating pan with a binding agent solution, the moistened crystalline drug is coated with further powdered active ingredient thus obtaining smooth, spherical pellets, the pellets are dried and subdivided in a plurality of groups, at least one of said pellet groups is coated with a pharmaceutically compatible, in stomach-intestine tract slowly dispersible lipoid, and the mentioned groups are then mixed. From what stated above, it may be clearly argued that, in comparison to the prior art, each capsule is filled with many microgranules, all being lacking in inert core and, therefore, at high concentration of active ingredient, and having particular percentages of the active ingredient compositions which confer the mentioned advantages. Further features and advantages of the invention will be made clear in the following detailed description that is given only for illustrative purposes. The process used to obtain the product of the present invention provides the following procedures, each being only given as exemplificatory. Generally, the process comprises the following steps: a) powdered etofibrate (or a substance having similar properties) was placed in a rotating pan, then acetone was added in an amount of from 10 to 40% by weight, and the mixture was worked in the same pan; b) the compound was submitted to a first sieving on a 0.8-1.4 mm (14-20 mesh) sieve and the first microgranules thus obtained were reworked in the pan that was being rotated for a while; c) the product comprising these first microgranules was dried until the solvent was evaporated off, then it was sieved again thus separating other microgranules or cores having a 0,3-1 mm diameter, which however is lower than the diameter of the first microgranules; d) said second microgranules or cores were replaced in the rotating pan and, by means of suitable pumps or by spraying, they were coated with further fused or dissolved etofibrate to which polyethylene glycol 4000 in an amount of from 3 to 12% or 2 to 11%, respectively, has been added; e) a last sieving was carried out to separate only these third microgranules, whose size corresponds to the requested size and is comprised between 400 and 2000 µm (microns); f) said third microgranules were then placed in suitable capsules. A detailed example of the process described above is reported here below. Referring to an amount of 50 kg of etofibrate, this powder was placed in a pan having a steel basket rotating at 10-20 rpm; 10 kg of acetone were added and the pan was being rotated for 10-25 minutes. The product was discharged and placed in a net granulator of 0.8-1.4 mm (14-20 mesh). The granulate thus obtained (or first microgranules) was replaced in the pan, rotating for 10/25 minutes. The product was dried for 10/20 minutes at 30°C in a thermostatic drier, i.e. until all the acetone was evaporated off. The dried granulate was then resieved, thus selecting the fraction comprised between 300 and 1000 µm (microns) and consisting of the second microgranules or cores. Said fraction was placed in the rotating par and by spraying with high pressure pumps the cores were coated with previously fused etofibrate to which polyethylene glycol 4000 was added. As to the sprayed etofibrate, the amount of polyethylene glycol 4000 is comprised between 3 and 12%. These (third) microgranules thus obtained were sieved for a last time and they were showing a diameter comprised between 400 and 2000 µm (microns). A further procedure could be fully identical to the procedure described above, with the sole exception that the etofibrate applied on the previously formed cores was not melted in advance. For coating these nuclei with etofibrate, the product was brought into solution with a solvent (acetone) by preparing a cold saturated solution or, if a lower concentration is desired, the solution etofibrate-acetone was heated between 35° and 45°C. In both cases, to the etofibrate solution the 3-12% of polyethylene glycol 4000, based on the etofibrate, was added. The microgranules obtained with the procedures and methods described above were then placed into capsules that are well known in the art as hard gelatine capsules and that can be of several sizes, that is of "0" type, containing 0.68 ml, or of extended "0" type (0.80 ml) or of "00" type (0.95 ml). The product obtained with the above process consists therefore of one of said capsules containing respectively 500, 600 or 750 mg of active ingredient. Said active ingredient comprises all the (third) microgranules having a diameter ranging from 400 to 2000 µm (microns). Each of these microgranules consists therefore of an etofibrate inner core and of an outer layer of etofibrate added with polyethylene glycol 4000, according to the above process, the whole having amounts of etofibrate ranging from 89 and 98% and amounts of polyethylene glycol 4000 comprised between 11 and 2% respectively. Evidently each microgranule consists mainly and entirely of active ingredient, even though it comprises an inner core of etofibrate alone. Logically each microgranule consists entirely of active ingredient with a very high amount of etofibrate, and therefore all the microgranules corresponding to a standard dosage of pharmaceutical product will take up less room and less volume, so that on one hand the therapeutic activity of the capsules can be increased, size of known capsules being equal, and on the other hand their size may be decreased, amount of active ingredient being equal.

Claims: A process for preparing capsules containing increased dosage sustained release microgranules of etofibrate or a substance having similar properties, characterized in that it comprises the following manufacturing steps: a) powdered active ingredient is placed in a rotating pan, acetone is added in an amount of from 10 to 40% by weight, based on the active ingredient weight, and the mixture is worked in said pan; b) the compound is submitted to a first sieving on a 14-20 mesh sieve (0.8-1.4 mm openings) and the microgranules not retained are reworked in the pan which is being rotated; c) the product comprising these first microgranules is dried until the solvent is evaporated off, and then it is sieved again thus obtaining microgranules having a diameter ranging from 0.3 to 1 mm which is lower than the diameter of the first microgranules; d) said second microgranules or cores, obtained as described under c), are replaced in the rotating pan and by means of suitable pumps they are coated with further fused or dissolved active ingredient to which polyethylene glycol 4000 in an amount of from 3 to 12% or 2 to 11%, respectively is added, based on the added active ingredient; e) a last sieving is carried out in order to separate only the third microgranules whose size corresponds to the requested size of from 0.4 to 2 mm diameter, and f) said third microgranules are placed in capsules. A process according to claim 1, characterized in that: in -step (a) the pan is rotated at a speed comprised between 10 and 20 rotations per minute and for a time ranging between 10 and 25 minutes; in step (b) the first microgranules thus obtained are being rotated in the pan for a time of 10-25 minutes; in step (c) the product consisting of the first microgranules is dried for 10-20 hours at about 30°C; and in step (d) said second microgranules are coated with previously melted active ingredients added with said polyethylene glycol 4000 by means of high pressure pumps. A process according to claim 1, characterized in that in step (d) the active ingredient, to which polyethylene glycol is to be added and that is to be applied on the second microgranules, is brought into solution with a solvent, creating a cold saturated solution, and then polyethylene glycol is added. A process according to claim 1, characterized in that in step (d) the active ingredient to be added with polyethylene glycol 4000 and to be applied on the second microgranules or cores is brought in solution with a solvent, then suitably heated and added with polyethylene glycol 4000. A capsule containing an active ingredient in the form of active ingredient-coated granules of said active ingredient, charcaterized in that it comprises a "0" type (0.68 ml) or an extended "0" type (0.80 ml) or a "00" type (0.95 ml) capsules, containing respectively 500 mg, 600 mg or 750 mg of active ingredient, this latter comprising microgranules obtainable according to any one of the preceding claims.

Inventors: VALDUCCI, ROBERTO
Applicants: VALDUCCI, ROBERTO
Application year: 1985
Main classification: A61K31
IPC codes: C07D213, A61K31, A61K9