Title of Invention

"PELLETS CONTAINING VENLAFAXINE HYDROCHLORIDE"

Abstract

The present invention relates to pellets and process of pelletization thereof. Pellets of the present invention are nearly spherical shape comprising pharmaceutically active venlafaxine hydrochloride, whereby said pellets contain (related to the total weight) at most 80% by weight of venlafaxine hydrochloride, 10 to 60% by weight of sodium chloride and/or potassium chloride, 10 to 60% by weight of microcrystalline cellulose and optionally other pharmaceutically acceptable excipients and/or pelletization promoting additives.

Full Text

Field of the invention The invention relates to pellets containing venlafaxine hydrochloride and a process for the preparation thereof. Technical background of the invention Venlafaxine (1-[2-(dimethylamino)-1-(4-methoxy-phenyl) ethyl] cyclohexanol) is a highly important antidepressant belonging to the antipsychotics possessing serotonin/noradrenalin uptake inhibiting effect (SNRI). A drawback of immediate release pharmaceuticals in therapeutic application resides in the fact that the quick release of the active agent results in a high plasma concentration, which causes unpleasant side-effects, such as nausea or vomiting in a considerable part of the patients. In order to avoid high plasma concentration following administration in case of venlafaxine as active ingredient the administration of sustained release pharmaceutical dosage forms is very advantageous, because the slow release of the active ingredient results in a lower and even blood level and thus the side-effects can be decreased. The most advantageous forms of sustained release pharmaceutical dosage forms are pharmaceuticals containing drug-loaded pellets. Pellets are spherical agglomerates 0,2-2 mm in diameter, which may be coated with one or more layer (s) regulating the release of the active agent and filled into hard gelatine capsules or tabletted When administering these compositions to patients, in the stomach the capsules or tablets are disintegrated or distributed into individual pellets, which are then thoroughly mixed with the content of the stomach, and the discharge of the pellets from the stomach becomes more uniform. In this way" a high active agent concentration cannot develop during the release of the active ingredient from the pellets, thus the plasma concentration becomes more even. The therapeutic activity of the composition becomes more favourable and the likelihood of the occurrence of side-effects considerably decreases. The first peliet-based pharmaceutical compositions were put on the market in the early 1950s. However, they could not become more wide¬spread until the 1970s due to their cumbersome preparation technology, which was based on the layering of the active ingredient and solid auxiliary agents, such as various types of starch, onto sugar crystals, in coating drums, and in this way the pellet preparation rook several days. From the beginning of the 1970s a special equipment is available for the preparation of pellets. This equipment serves basically for the purpose of extrusion-spheronization, centrifugal granulation, fluidization rotogranulation and high-shear mixing processes. By applying said equipment pellets can be produced directly, within only a few hours from a suitable powder mixture. Recently especially the application of fluidization rotary granulators and high-shear pelletizing machines combined with vacuo or microwave drying has become frequent, because by using such an equipment the production of pellets can be performed in a single apparatus (Isaac Ghebre-Sellassie: Pharmaceutical Pelletization Technology, Marcel Dekker, Inc., New York, Basel, 1989). Pellets can be prepared according to a number of methods, which all can be based on the following tree principles: 1 . layering 2 . extrusion-spherofonization 3. build-up granulation By the layering method a mixture of the particles of the active ingredient and/or the auxiliary agents of small particle size is applied in layers onto a nearly isodiamstric seed material having larger particle size than that of the said active ingredient and/or auxiliary agents. The application can be performed in a conventional coating drum, in a centrifugal granulating equipment or in a fluidization spraying' apparatus. In certain cases in the fluidization machines the active ingredient can be sprayed onto the surface of the inert granules from a solution. However, according to Hungarian patent specification No. 199,677 the high solubility (exceeding 600 mg/ml) of the active ingredient is disadvantageous from the viewpoint of the layering pelletization. In case of the extrusion-spheronization process the active ingredient is mixed with the auxiliary agents and a liquid, the wet mass is fed into an extruder having holes of about I mm in diameter, and the extrudate is formed into uniform, nearly spherical particles in a rotary spheronization machine. According to the build-up granulation process a mixture of the active ingredient and the auxiliary agents is mixed in a mixer or in a centrifugal or fluidization granulator, while a liquid is fed into the machine. During this process the particles of the powder mixture adhere to each other and become spherical upon the effect of shear forces and abrasive forces . The last step of all pelletization 'processes is drying of the particles and separation of the fraction having a particle size suitable for further processing,. The quality of the pelletization technology can be characterized by the product fraction, that is by the ratio of the mass of the pellets having the desired particle size to the total mass of the pellets. The pellets of unsuitable size are namely recycled to the manufacturing process and processed repeatedly, which results in an increase of the production time, costs of material and energy and the intensity of the labour involved in the procedure. In case of pellets filled into capsules the preferable particle size varies between 0.5 mm and 1.0 mm, in case of pellets compressed into tablets between 0.3 mm and 0.6 mm. In case of active ingredients readily soluble in water it is expedient to use pellets of bigger particle size, such as 0.8 - 1.6 mm or 1.0 - 2.0 mm, in order to decrease the amount of the coating material necessary for the coating modifying the release of the active ingredient. In addition to the active ingredient pharmaceutically acceptable excipients are also applied for the pelletization, which promote the formation of pellets of appropriate shape and surface. Such excipients may be fillers, lubricants, antiadhesives, disintegrants or drug release promoting additives, buffers, sur¬factants, surface-active substances, pelletiz- ation promoting additives or glidants (Isaac Ghebre-Sellassie: Pharmaceutical Pelletization Technology, Marcel Dekker, Inc., New fork, Basel, 1989). As fillers which can be used for the pelletiz-ation e.g. calcium sulfate, calcium hydro-phosphate, lactose, mannitol, szaccharose, starch and microcrystalline cellulose are mentioned. Suitable binders are e.g. gelatine, hydroxy-propyl cellulose, hydroxypropyl-methyl cellulose, methylcellulose, polyvinyl pyrrolidone, szaccharose and starch. As lubricant calcium stearate, hydrogenated vegetable oil, magnesium stearate, mineral oil, polyethylene glycol, glycerine and propylene glycol may be applied. The pellets may also contain antiadhesives, such as kaolin, talk or silicon dioxide, furthermore disintegrants or drug release promoting agents, e.g. alginates, sodium carboxymethyl cellulose, crospovidon, starch, pre-gelatinized starch, sodium carboxymethyl starch, or e.g. ethyl-cellulose, carnauba vax, shellac. Buffers (such as citrate, phosphate, carbonate and hydro-carbonate salts), surface-active additives (such as polysorbate, sodium laurylsulfate) and spheronization promoting substances (e.g. micro-crystalline cellulose or a mixture of micro-crystalline cellulose and sodium carboxymethyl cellulose) may also be used for the pellets. Glidants applied during pelletization include e.g. colloidal silicon dioxide, magnesium stearate, talc and starch. In the conventional pelletization methods the ratio of the product fraction is about 60% by weigh. That is why every technical solution resulting in an increase in the product fraction in addition to the maintenance of other important characteristics of the pellets - such as a nearly spherical shape and a suitable quality of the surface - is of high importance. Several methods aiming at increasing the product fraction have been published. According to European patent specification No. 288,732 during the extrusion-spheronization process organic acids (such as citric, tartaric, maleic, fumaric, succinic acid) applied in the composition in an amount of 5 to 50% by weight improve the plasticity of the wet mass and thus enable the preparation of harder pellets with particles of a narrow size range. At the same time this method cannot be used for the formulation of acid-sensitive active ingredients. According to a publication of G.A. Hileman et al. (Drug Dev. and Ind. Pharmacy, 19(4) , 4 83-491, 1993) in case of the preparation of pellets with high active agent content the application of microcrystalline cellulose containing a slight amount of sodium carboxyroethyl cellulose promote the formation of high-quality pellets. In the process disclosed in International patent application No. WO 94/08567 0.03% by weight of polysorbate is applied in order to increase the ratio of product fraction. According to the process disclosed in Hungarian patent specification No. 198,396 a coating powder containing 5 to 98% by weight of low-substituted hydroxypropyl cellulose (containing 4 to 20% of hydroxypropyl group) is applied during the pelletization. On the basis of the above facts it can be established that peiletization is a complicated pharmaceutical operation requiring a special equipment and intensive labour. For the persons skilled in the manufacture of pharmaceutical compositions it is known that by using the excipients known from the prior art it is particularly difficult - in certain cases impossible - to produce pellets in suitable quality (which are approximately spherical in shape) and in high yield (with a high ratio of the product fraction), especially in case of active ingredients soluble or readily soluble in water. Venlafaxine hydrochloride belongs to the group of the active ingredients readily soluble in water (0.57 g/ml). According to Hungarian patent specification No. 196,677 pellets cannot be prepared from methoprolol salts readily soluble in water, that is from salts having a water-solubility higher than 500 mg/ml . What is more, even in case of methoprolol salts having a water solubility lower than 600 mg/ml the application of a special technology is necessary. During this technology the active ingredient is applied onto water-insoluble quartz or glass granules from a solution of methoprolol fumarate or succinate in ethanol-dichloromethane by a layering process. This technology requires an expensive equipment from the viewpoint of solvent recovery and regeneration, its productivity is poor, and it has unfavourable characteristics considering environmental, health and fire protection. Hungarian patent application No. P9700589 suggests that in case of venlafaxine hydro¬chloride having a solubility higher than 500 mg/ml pelletization can be performed only by the application of microcrystalline cellulose combined with hydroxypropyl-methyl cellulose. According to Hungarian patent application No. P0004287 pellets containing venlafaxine can also be prepared without the application of hydroxy-propyl-methyl cellulose if the ratio of the weight of venlafaxine is decreased in the pellets. However, this solution is unfavourable,-because in case of identical doses a decrease in the weight ratio of venlafaxine constitutes a higher pellet weight and consequently a medicine of bigger size. Thus it is more difficult to swallow the composition and the manufacture is more expensive. Data of the technical literature show that in case of the readily water-soluble venlafaxine hydrochloride experts have so far failed to elaborate a composition of the excxpients enabling the preparation of pellets having a high active ingredient content and a suitable quality (being approximately spherical in shape) and providing an advantageous product fraction. The aim of the invention was to elaborate a composition and process which are suitable for the preparation of pellets in up-to-date fluidization and rotogranulation machines providing the preparation of the product fraction (that is the ratio of pellets used for further processing) in a high yield, that is in a yield of at least 75%, preferably more that 80%, and in a suitable quality. Summary of the invention The invention is based on the surprising recognition that if 10 to 60% by weight of sodium chloride and/or potassium chloride are added to the powder mixture to be pelletized in addition to at most 80% by weight of active agent and 10 to 60% by weight of microcrystalline cellulose, pellets with high active ingredient content and very advantageous in shape (approximately spherical) can be produced from the otherwise unpelletizable active agents as well. Besides, the particle size of the said pellets is highly suitable for pharmaceutical purposes, and the yield of the product fraction exceeds 75%. Details of the invention According to an aspect of the present invention there are provided nearly spherical pellets comprising the pharmaceutical ingredient venlafaxine hydrochloride in admixture with 10 to 60% by weight of sodium chloride and/or potassium chloride and* 10 to 60% by weight of microcrystalline cellulose and optionally other, pharmaceutically acceptable excipipents and/or additives promoting the pelletization. According to another aspect of the present invention there is provided a process for the preparation of nearly spherical pellets containing the pharmaceutical ingredient venlafaxine, which comprises admixing at most 80% of the active ingredient with 10 to 60% by weight of microcrystalline cellulose, 10 to 60% by weight of sodium chloride and/or potassium chloride and optionally other, pharmaceutically acceptable excipients and/or additives promoting the pelletization, converting the thus-obtained mixture into pellets by high-shear mixing, rotofluidization or extrusion-spheronization method, preferably by rotofluidization by spraying water or preferably an aqueous dimethyl polysiloxane emulsion and/or an aqueous solution of xanthane gum, drying the pellets, separating the desired product fraction and optionally coating the pellets with a layer to modify the drug release. In order to improve efficiency of the pelletization dimethyl polysiloxane is emulged in the pelietizmg liquid. In this way the particle size of the thus-obtained pellets can be controlled much better, the size or the pellets is more uniform and the product fracrion may exceed even 90%. Similar results can be achieved when xanthane gum is dissolved in the pelletezing liquid, or when the pelietizing liquid contains both dimethyl polysiloxane and xanthane gum. The exact mechanism of the effect of sodium chloride and/or potassium chloride, dimethyl polysiloxane and xanthane gum is not known at the moment, but it can be supposed that the formation of a more uniform particle size may be the result of a decrease in the solubility of the active ingredient upon the effect of the ionic filler materials, an increase in the plasticity of the powder mixture to be pelletized and some advantageous changes of the cohesion between the particles. The pharmaceutical compositions containing pelletized active ingredient are usually prepared in dosage unit forms. During the pelletization process the concentration of the active ingredient is determined by the single dose of the active agent finished in a dose unit so that the weight of the pellets containing a single dose of the active ingredient should vary between 50 to 1500 mg, preferably between 100 to 700 mg. In the knowledge of the weight of the pellets containing a single dose of the active ingredient the sodium chloride and/or potassium chloride and microcrystalline cellulose content of the pellet can be determined. The premix used for the preparation of pellets according to the invention possessing advantageous properties should contain a total amount of at least 10% by weight of both excipients. If the active ingredient content of the pellets is lower than 80% by weight as a consequence of a lower dose, the sodium chloride and/or potassium chloride and microcrystalline cellulose content may be increased. The two types of excipients can be used in nearly identical amounts. As to the quality of the microcrystalline cellulose used for the preparation of pellets according to the invention, there are no restrictions. Various types of microcrystalline cellulose of different particle size and of¬different density may freely be applied. Even the application of microcrystalline cellulose with a low moisture content is not required, since during pelletization the substance mixture is moistened with water or contacted with an aqueous solution or dispersion. In addition tc the so-called pure or monocomponent microcrystalline cellulose varieties mixtures of various types of microcrystalline cellulose formed with colloidal silicon dioxide can alsc be used, which contain about 98% by weight of microcrystalline cellulose and about 2% by weight of colloidal silicon dioxide. From the viewpoint of pelletization both sodium chloride and potassium chloride can be used to advantage, but due to their different physiological effects it is preferable to chose their concentrations on the basis of the extra¬cellular physiological concentration. This constitutes a weight ratio of sodium chloride to potassium chloride of about 20:1. Thus, choosing e.g. 10% by weight as sodium chloride/potassium chloride concentration, preferably 9.5% by weight of sodium chloride and 0.5% by weight of potassium chloride can be applied. ft Furthermore, by applying excipients in the compositions of the pellets according to the invention, the quality of the pellets and the quantity of the amount of pellets falling into the preferable particle size region can be improved. For this purpose xanthane gum or dimethyl polysiloxane may be used. These auxiliary agents are dissolved or disperged either individually or together in water used for the pelletization, and added to the premix to be pelletized in the beginning of the pelletization procedure. Xanthane gum used in the compositions according to the invention is a natural polysaccharide produced by the microorganism Xantomonas campestris. The skeleton of xanthane gum, such as that of cellulose,- consints of 1,4-gluco-pyranose units, while the side-chains contain mannose, acetate and glucuronic acid. The average molecular weight is a few million Dalton. In the pharmaceutical industry xanthane gum is mostly applied for increasing the stability of suspensions used for coating of medicines or films (e.g. Hungarian patent specification No. 202120) or as a viscosity-increasing agent (the United States Pharmacopoeia, ed. 26., 2003, United States Pharmacopoeial Convention, Inc, Rockwille, USA) or as a matrix building material for extended release tablets. When used for pelletization, xanthane gum increases the stability of the peilets. This advantageous effect of this substance has not so far been mentioned in the literature and could not be aforeseen. Xanthane gum can be used in the pelletization liquid in an amount of not exceeding 2% by weight related to the final weight of the pellet. Dimethyl polysiloxane used in the compositions according to the invention is a liquid substance, a completely methylated polymeric siloxane having a viscosity value between 100 and 1000 centi -stokes. The aqueous dimethyl polysiloxane dispersions are commercially available products, which are used for surface treatments, as skin softening additives for pharmaceutical and cosmetic compositions, as antifriction agents for tabletting or as antiadhesives for film-coating (Hungarian patent specification No. 190,693). The United States Pharmacopoeia (USP 26) classifies dimethyl polysiloxane into the, group of antifoarn additives. A surprising - and so far fully unknown - property of dimethyl polysiloxane is that in the course of pelletization, when. emulged in an amount of not exceeding 5% by weight: into water or an aqueous colloidal solution of xanthane gum used for the pelletitation, it improves the spherical shape of the pellets and augments the ratio of the product fraction. The pellets according to the invention can be prepared by build-up (high-shear or roto-fluidization) or by extrusion-spheronization methods known from the literature. In the course of the pelletization process venlafaxine hydrochloride is mixed with sodium chloride and/or potassium chloride and microcrystalline cellulose The mixture is homogenized and the thus-obtained powdered premix is moistened with water or with an aqueous solution of the binder(s) and/or other, pharmaceutically acceptable excipients. The mixture is converted into pellets of the desired particle size by using an appropriate equipment (extruder-spheronizator-drier, high-shear granulator-drier, rotofluidization apparatus). Then the product fraction having the desired particle size is isolated by size, e.g. by sieving. The pellet fraction having an unsuitable particle size is transferred back to the pelletization process after grinding. The advantageous effect of sodium chloride and potassium chloride on the pelletization manifests itself in the simplification of the manufacturing technology.-increase in its reliability and the advantageous formation of the product fraction. Another advantage of the application of the above-mentioned alkali salts is that their price is low even in case of a pharmaceutical quality, so their application results in a reduction of the manufacturing costs. The pellets containing venlafaxine hydrochloride according to the invention are particularly suitable for further coating operations. In the course of coating water-soluble (e.g. hydroxy-propyl-methyl cellulose, polyvinyl alcohol), water-insoluble (e.g. ethyl cellulose, ethyl acrylate - methyl methacrylate copolymer, poly¬vinyl acetate) or film-forming substances having a sulubility depending on the pH of the aqueous medium (e.g. cellulose acetate phtalate, hydroxypropyl-methyl cellulose acetate succinate, ethyl-acrylate-methacrylic acid copolymer) can equally be used. Coating can be carried out with an aqueous or organic solution or an aqueous dispersion of the film-forming substances. Depending on the solubility characteristics of the film coating immediate release (water-soluble coating), extended release (water-insoluble coating) or delayed release (the solubility of the coating depends on the pH of the releasing medium) compositions can be prepared. The quality and quantity of the coating substance are to be determined on the basis of the dissolution profile, that is the desired dependence of the release on time. The pellets containing venlafaxine hydrochloride according to the invention and preparation thereof are illustrated- by the following examples without limiting the scope of protection to said examples. Example 1 Preparation of pellets containing venlafaxine hydrochloride 450 g of venlafaxine hydrochloride, 396 g of microcrystallme cellulose, 6 g of colloidal silicon dioxide, 342 g of sodium chloride and 18 g of potassium chloride were mixed in an acid-resistant vessel. The mixture was transferred to a fluidization rotogranulator (Glatt GPCG1), and a mixture of 20 g of 35% dimethyl polysiloxane emulsion and 1000 ml of ion-exchanged water was sprayed onto it. Spraying speed of the pelletiz-mg liquid was set at 50 ml/rnin, pressure of the spraying air was 2.5 bar. The speed of the rotor was set at 450 rev/min in the first 15 minutes of the pelletization and later kept at 600 rev/min. Speed by volume of the fluidization air was kept at 60 m3/hour in the first 15 minutes of the pelletization and later at 90 m3/hour. The temperature of the fluidization air was set at 25 °C in the first part of the pelletization and to 40 °C for the drying procedure. The dried pellets were passed through sieves having hole widths of 0,8 mm and 1,6 mm, respectively and divided into 3 fractions . The product fraction, that is the amount of the granules in the range between 0.8 mm and 1.6 mm, amounts to 96% by weight. For the preparation of a sustained release composition a fluidization apparatus of Glatt GPCG1 type was equipped' with a bottom spraying Wurster insert, and 500 g of the product fraction were fed into the container. As coating liquid 200.0 g of an aqueous polymeric dispersion containing 30% of polyvinyl acetate (trademark name: Kollicoat SR) were applied. To the said dispersion 8.4 g of propylene glycol dissolved in 240 g of water were added. Coating was carried out under the following conditions: - temperature of the fluidization air: 60 °C - rate of feed: 8 ml/min - pressure of spraying: 2 bar Example 2 Preparation of pellets containing venlafaxme hydrochloride 4 50 g of venlafaxine hydrochloride, 396 g of microcrystalline cellulose, 6 g of colloidal silicon dioxide, 342 g of sodium chloride and 18 g of potassium chloride were mixed in an acid-proof vessel. The mixture was transferred to a fluidization rotogranulator (Glatt GPCG1), and a solution of 2 g of xanthane gum in 300 ml of ion-exchanged water and further 1080 ml of ion-exchanged water were sprayed onto it. Spraying speed of the pelletizing liquid was set at 50 ml/mm, pressure of spraying air was 2.5 bar. The speed of the rotor was set at 450 rev/mm in the first" 15 minutes of the pelletization and later kept at 600 rev/min. Speed by volume of the fluidization air was kept at 60 m3/hour in the first 15 minutes of the pelletization and later at 90 m3/hour. The temperature of the fluidization air was set at 25 °C in the first part of the pelletization and to 40 °C for the drying procedure. The dried pellets were passed through sieves having hole widths of 1.6 mm and 0.8 mm, respectively and divided into three fractions. The product fraction, that is the amount of the pellets in the range between 0.8 mm and 1.6 mm, amounts to 90% by weight. Example 3 Preparation of pellets containing venlafaxine hydrochloride 4 50 g of venlafaxine hydrochloride, 396 g of microcrystalline cellulos, 6 g of colloidal silicon dioxide, 342 g of sodium chloride and 18 g of potassium chloride were mixed in an acid-proof vessel. The mixture was transferred to a fluidization rotogranulator (Glatt GPCG1), and a mixture of a solution of 2 g of xanthane gum in 250 ml of ion-exchanged -water and 50 g of 35% dimethyl polysiloxane and a mixture of further 60 g of 35% dimethyl polysiloxane and 1000 ml of ion-exchanged water were sprayed onto it. Spraying speed of the pelletizing liquid was set at 50 ml/min, pressure of spraying air was 2.5 bar. The speed of the rotor was set at 4 50 rev/min in the first 15 minutes of the pelletization and later kept at 600 rev/min. Speed by volume of the fluidization air was kept at 60 m3/hour in the first 15 minutes of the pelletization and later at 90 m3/hour. The temperature of the fluidization air was set at 25 °C in the first part of the pelletization and to 4 0 °C for the drying procedure. The dried pellets were passed through sieves, having hole widths of 1.6 mm and 0.8 mm, respectively and divided into 3 fractions. The product fraction, that is the amount of the granules in the range between 0.8 mm and 1.6 mm, amounts to 88.3% by weight. For the preparation of sustained-release compositions a fluidization apparatus of Glatt GPCG1 type is equipped with a bottom spraying Wurster insert, and 500 g of the above product fraction were fed into the container. As coating liquid a solution of 60.0 g of ethylcellulose (viscosity. 10 centipoise) and 6.0 g of copovidone (vinylpyrrolidone acetate (60/4 0) co- polymer) in 550.0 g of 96% by volume ethanol were used, in which 18.0 g of talc had been suspended as antiadhesive. Coating was carried out under the following conditions: - temperature of the fluidization air: 40 °C - rate of feed: 8 ml/min - pressure of spraying: 2 bar Example 4 Preparation of pellets containing venlafaxine hydrochloride 450 g of venlafaxine hydrochloride, 396 g of microcrystalline cellulose, 6 g of colloidal silicon dioxide, 342 g of sodium chloride and 18,. g of potassium chloride were mixed in an acid-proof vessel. The mixture was transferred to a fluidization rotogranulator (Glatt GPCG1) , and 1500 ml of ion-exchanged water were sprayed onto it. Spraying speed of the pelletizing liquid was set at 50 ml/min, pressure of spraying air was 2.5 bar. The speed of the rotor was set at 4 50 rev/min in the first 15 minutes of the pelletization and later kept at 600 rev/rain. Speed by volume of the fluidization air was kept at 60 m3/hour in the first 15 minutes of the pelletization and later at 90 m3/hour. The temperature of the fluidization air was set at 25 °C in the first part of the pelletization and at 40 °C for the drying procedure. The dried pellets were passed through sieves having hole widths of 1.6 mm and 0.8 mm, respectively, and divided into 3 fractions. The product fraction, that is the amount of the granules in the range between 0.8 mm and 1.6 mm, amounts to 75.3% by weight. Example 5 Preparation of pellets containing veniafaxine hydrochloride 11.0 kg of veniafaxine hydrochloride, 7.26 kg of microcrystalline cellulose, 0.13 kg of colloidal silicon dioxide, 5.97 kg of sodium chloride and 0.32 kg of potassium chloride were homogenized in a high-shear granulator of Diosna V-100 type. The homogenizate was moistened with a mixture of a solution of 0.04 kg of xanthane gum in 6.5 kg of ion-exchanged water and 1.0 kg of 39% dimethyl polysiloxane. The wet substance was sieved with the aid of an oscillation apparatus of Diaf GS-140 type using a sieve having hole widths of 1,0 mm. The sieved substance was transferred to a fluidization rotogranulator of Glatt GPCG15 type, about 20 kg of ion-exchanged water were sprayed onto it and converted into pellets having a particle size mostly in the range between 0.-8 mm and 1.6 mm. Spraying speed of the pelletizing liquid was set at 250 ml/mm, pressure of spraying air was 3.5 bar. The speed ' of the rotor was kept at 300 rev/min during the pelletization and at 500 rev/min during drying of the pellets. Speed by volume of the fluidization air was varied between 350 and 750 m3/Vhour depending on the motion of the material .. The temperature of the fluidization air was kept at 25 °C during the pelletization and at 40 °C in the course of the drying. For the preparation of sustained-release compositions a fluidization apparatus of Glatt GPCG1 type was equipped with a bottom spraying Wurster insert, and 20 kg of the above product fraction were fed into the container. As coating liquid a solution of 3.30 kg g of ethylcellulose (viscosity: 10 centipoise) and 0.33 kg of copovidone (vinylpyrrolldone/vinylacetate (60/40) copolymer) in 30 kg of 96% by volume ethanol was used, in which as antiadhesive 0.99 kg of talc and as colouring agent 0.02 kg of iron oxide pigment had been suspended. Coating was carried out under the following conditions: - temperature of the fluidization air: 60 °C - rate of feed: 90 ml/min - pressure of spraying: 3.5 bar We Claim: 1. Pellets in nearly spherical shape comprising pharmaceutically active venlafaxine hydrochloride, whereby said pellets contain (related to the total weight) at most 80% by weight of venlafaxine hydrochloride, 10 to 60% by weight of sodium chloride and/or potassium chloride, 10 to 60% by weight of microcrystalline cellulose and optionally other pharmaceutically acceptable excipients and/or pelletization promoting additives. 2. Pellets as claimed in claim 1, wherein the pellet has a particle size in the range between 0.2 mm and 2 mm, preferably between 0.5 mm and 1.6 mm. 3. Pellets as claimed in claim 2 comprising 0.4 to 60% by weight of active ingredient, 20 to 60% by weight of sodium chloride and/or potassium chloride, 20 to 60% by weight of microcrystalline cellulose, 0.5 to 3.0% by weight of dimethyl polysiloxane and/or 0.1 to 1.0% by weight of xanthane gum and, if desired, 0.1 to 0.6% by weight of colloidal silicon dioxide. 4. Pellets as claimed in claim 3, wherein the total amount of the potassium chloride and sodium chloride is 20 to 60% by weight. 5. Pellets as claimed in claim 4, wherein the weight ratio of the sodium chloride: potassium chloride is about 20:1. 6. Pellets as claimed in any of claims 1 to 5 comprising venlafaxine hydrochloride in the polymorphic form I. 7. Pellets as claimed in any of claims 1 to 5 comprising venlafaxine hydrochloride in the polymorphic form II. 8. Pellets as claimed in any of claims 1 to 5 comprising venlafaxine hydrochloride in the polymorphic form III. 9. Pellets as claimed in claim 8 optionally supplied with a coating to modify the drug release and having a particle size between 0.8 mm and 1.6 mm, which comprise 35 to 45% by weight of venlafaxine hydrochloride in admixture with 25 to 35% by weight of microcrystalline cellulose, 1.0 to 1.6% by weight of potassium chloride, 23.8 to 30% by weight of sodium chloride, 0.5 to 1.6% by weight of dimethyl polysiloxane and/or 0.1 to 0.2% by weight of xanthane gum and 0.4 to 0.6% by weight of colloidal silicon dioxide. 10. Solid pharmaceutical compositions comprising as active ingredient venlafaxine hydrochloride formulated with the aid of pellets as claimed in any of claims 1 to 9. 11. A process for the preparation of pellets as claimed in any of claims 1 to 9, which comprises admixing at most 80% of the active ingredient with 10 to 60% by weight of micro-crystalline cellulose, 10 to 60% by weight of sodium chloride and/or potassium chloride and optionally other, pharmaceutically acceptable excipients and/or pelletization promoting additives, converting the thus-obtained mixture into pellets by high-shear blending, rotofluidization or extrusion-spheronization method, preferably by rotofluidization by spraying water or preferably an aqueous dimethyl polysiloxane emulsion and/or an aqueous solution of xanthane gum, drying the pellets, separating the desired product fraction and optionally coating the pellets with a layer to modify the drug release.

Documents:

2041-DELNP-2006-Abstract-(27-12-2011).pdf

2041-delnp-2006-abstract.pdf

2041-DELNP-2006-Claims-(27-12-2011).pdf

2041-delnp-2006-claims.pdf

2041-DELNP-2006-Correspondence Others-(11-10-2011).pdf

2041-delnp-2006-Correspondence Others-(12-07-2012).pdf

2041-DELNP-2006-Correspondence Others-(27-12-2011).pdf

2041-DELNP-2006-Correspondence Others-(30-09-2011).pdf

2041-delnp-2006-correspondence- other.pdf

2041-delnp-2006-correspondence-others-1.pdf

2041-delnp-2006-correspondence-others-2.pdf

2041-DELNP-2006-Description (Complete)-(27-12-2011).pdf

2041-delnp-2006-description (complete).pdf

2041-DELNP-2006-Form-1-(27-12-2011).pdf

2041-delnp-2006-form-1.pdf

2041-delnp-2006-form-18-1.pdf

2041-delnp-2006-form-18.pdf

2041-delnp-2006-form-2.pdf

2041-DELNP-2006-Form-3-(27-12-2011).pdf

2041-DELNP-2006-Form-3-(30-09-2011).pdf

2041-delnp-2006-form-3.pdf

2041-delnp-2006-form-5.pdf

2041-delnp-2006-gpa.pdf

2041-delnp-2006-pct-101.pdf

2041-delnp-2006-pct-210.pdf

2041-delnp-2006-pct-304.pdf

2041-delnp-2006-pct-401.pdf

2041-delnp-2006-pct-409.pdf