according to the present invention a preferred improved solid oral dosage form of dabigatran etexilate , in particular dabigatran etexilate methanesulfonate , is produced by suspension / solution layering of tartaric acid onto spherical cores , such as neutral cores comprised of sucrose , microcrystalline cellulose and starch , or tartaric acid pellets , followed by an isolating layer and the layer comprising the active pharmaceutical ingredient . optionally , an overcoat can be applied . it has surprisingly been found out that dabigatran etexilate , in particular dabigatran etexilate methanesulfonate pellets can also be prepared according to a much simplified and technologically less demanding process than powder layering of tartaric acid crystals with tartaric acid dust and with an aqueous solution of tartaric acid and acacia acting as glue . a commercially available neutral pellet , comprised of sucrose , microcrystalline cellulose or starch , or a commercially available tartaric acid pellet may simply be coated with a solution of tartaric acid , the solution optionally also comprising a binder , such as e . g . acacia , povidone , hydroxypropylcellulose or hydroxypropylmethylcellulose , and talc . the dried coated pellets ( i . e . starter pellets ) obtained by such a process are round , smooth and of narrow size distribution . their surface is smooth and the tartaric acid coating as well as the isolating layer applied to them are firm . no satellites protrude into the isolating layer and the layer comprising the active pharmaceutical ingredient thus leading to a stable and bioequivalent pharmaceutical product . the formulation according to the present invention preferably contains pellets presented in fig1 . the pellets comprise a neutral core comprised of sucrose , microcrystalline cellulose or starch , or a commercially available tartaric acid pellet ; the tartaric acid layer , the isolating layer , the active pharmaceutical ingredient layer and , optionally , an overcoat . the neutral core comprised of sucrose , microcrystalline cellulose or starch , or a commercially available tartaric acid pellet will be referred to as the & gt ;& gt ; core & lt ;& lt ; in the following . the core comprising the tartaric acid layer will be referred to as the & gt ;& gt ; starter pellet & lt ;& lt ; in the following . the pellet comprising the core , the tartaric acid layer and the isolating layer will be referred to as the & gt ;& gt ; isolated pellet & lt ;& lt ; in the following . the pellet comprising the core , the tartaric acid layer , the isolating layer as well as the active pharmaceutical ingredient layer , and optionally an overcoat , will be referred to as the & gt ;& gt ; final pellet & lt ;& lt ; in the following . the cores are preferably of round shape and of narrow size distribution . they are selected from but not limited to the group of sugar spheres of different size classes , mcc ( microcrystalline cellulose ) pellets , tartaric acid pellets etc . preferably the cores are sugar spheres . most preferably the cores are sugar spheres of the size 425 - 500 μm . the starter pellets are in particular prepared from the cores with particle size in the range from 0 . 2 to 0 . 8 mm , preferably 0 . 3 to 0 . 7 mm and most preferably 0 . 4 to 0 . 6 mm as determined by sieving , onto which a solution of tartaric acid and optionally binder is sprayed . the solution is preferably prepared according to the following method : tartaric acid is dissolved in the solvent optionally together with one or more suitable binders , preferably acacia , hydroxypropylmethyl cellulose , and / or povidone at room or elevated temperature , preferably at a temperature between 20 ° c . and 80 ° c . for example , a clear solution of acacia is prepared , then the tartaric acid is added at a constant temperature and under continuous stirring . the mixture is then stirred additionally for at least half an hour , preferably between 1 and 8 , particularly preferably 4 to 6 hours . the tartaric acid / binder solution prepared by the method described hereinbefore is then sprayed onto the cores kept moving by rotation . the equipment used is known to the person skilled in the art . in one of the preferred embodiments , a clear solution of tartaric acid without the presence of a binder is prepared in a mixture of ethanol and water . spraying is preferably carried out at a defined spray rate and at constant temperature , preferably between 20 ° c . and 80 ° c . by the spray rate is meant the amount of tartaric acid / binder solution that is sprayed onto the rotating pellet bed per hour . the spray rate depends on the batch size in the process according to the invention . after spraying is accomplished the starter pellets are dried until a product temperature of about 30 ° c . to 50 ° c . the first layer ( the tartaric acid layer ) comprises tartaric acid and is produced by suspension or solution layering of the cores without powder layering with tartaric acid dust in order to minimize , most preferably avoid the formation of the satellites . different solvents can be applied for the layering process , such as water or organic solvents , selected but not limited to the group of alcohols ( ethyl alcohol , methyl alcohol , 2 - propanol , dimethylformamide etc . ), acetone and other pharmaceutically acceptable organic solvents . preferably , alcohols , water and mixtures thereof are used . most preferably a mixture of ethanol and water is used in the process . optionally , other excipients can be added to the solution , such as for example binders , antifoaming agents , or anti - sticking agents . the content of tartaric acid in the first layer is preferably not lower than 50 %, more preferably not lower than 80 % and most preferably not lower than 90 % w / w . the function of the tartaric acid lies in providing an acidic micro environment when the solid oral dosage form disintegrates to facilitate the dissolving of dabigatran etexilate , preferably dabigatran etexilate methanesulphonate . the content of tartaric acid in the formulation ( capsule content ) is usually less than 80 %, preferably less than 60 % and most preferably less than 45 %. surprisingly it was also found that decreased tartaric acid contents in the final pellet may be applied , which can optionally also be lower than 20 % ( w / w ) without impairing the stability and dissolution of the final pellet . the second layer is an isolating layer , which is preferably based on a water soluble pharmaceutically acceptable polymer , which can be selected but not limited to the group of cellulose esters ( such as hydroxypropyl cellulose , hydroxypropyl methylcellulose , methylcellulose , carboxymethyl cellulose etc . ), povidone , acacia , etc . and whose function is to separate the acid sensitive pharmaceutically active ingredient from the tartaric acid layer . additionally , plasticizers , anticaking agents and coloring agents can be added to the isolating layer . polyethylene glycols , triethylcitrate , tributylcitrate , triacetine , dibutylsebacate etc . can be used as plasticizers . talc and silicon dioxide are examples for anticaking agents , preferably talc is used . optionally dimethylpolysiloxane ( dimeticone ) or other antifoaming agents can be used to prevent foaming of the solution or suspension . titanium dioxide , iron oxides and other coloring agents can also be applied . the isolated pellets are preferably prepared by spraying an isolating suspension / solution onto the starter pellets obtained by the process described hereinabove . to prepare the isolating suspension the selected polymer ( s ) are in particular dissolved or suspended in the solvent such as water or organic solvents , selected but not limited to the group of alcohols ( ethyl alcohol , methyl alcohol , 2 - propanol , dimethylformamide etc . ), acetone and other pharmaceutically acceptable organic solvents . preferably , alcohols , water , and mixtures thereof are used . to the solution or suspension of the polymer in the solvent optionally plasticizers , anticaking agents , antifoaming agents and coloring agents are added and the solution or suspension is sprayed onto the starter pellets . during this continuous process the cores are dried continuously with a supply of air at up to 70 ° c ., preferably from 15 ° c .- 70 ° c . the isolated pellets have a uniform and spherical geometry and practically no defects in the isolation caused by satellites . the so - called satellites are small particles adhering to the outside of the otherwise rounded pellets and detracting from the otherwise spherical geometry of the pellets . the final pellets comprising the pharmaceutically active ingredient are preferably prepared by spraying an active substance suspension onto the isolated pellets . the active substance suspension is prepared using dabigatran etexilate or a pharmaceutically acceptable salt thereof , preferably dabigatran etexilate methanesulfonate in the form of its polymorph i . the polymorph i is characterized inter alia by a melting point of tmp .= 180 +− 3 ° c . ( as determined by dsc ; evaluated using peak maximum ; heating rate : 10 ° c ./ min ) and may e . g . be prepared as disclosed in wo 03 / 074056 , example 3 . the targeted production of polymorph i is possible for example using the method described in wo 2005 / 028468 ( particularly example 1 ). in order to prepare the active substance suspension comprising dabigatran etexilate form i in a preferred embodiment for instance isopropyl alcohol ( 2 - proh ) is adjusted to a temperature range of 10 ° c .- 30 ° c . under a nitrogen atmosphere . isopropanol is preferably used in anhydrous or almost anhydrous form ( 99 . 5 % w / w ). if the suspension or solution of dabigatran etexilate methanesulfonate form i is produced or even stored ( aged ) at too high a temperature , this may lead to a change in the polymorphic form of the active substance . particularly preferably the temperature of the manufacturing process is in the range from 0 ° c . to 30 ° c ., particularly preferably between 5 ° c . and 30 ° c . if another polymorphic form of dabigatran etexilate methanesulfonate or if another salt of dabigatran etexilate is to be used , the solvents to be used are chosen from the group of water or organic solvents , selected but not limited to the group of alcohols ( ethyl alcohol , methyl alcohol , 2 - propanol , dimethylformamide etc . ), acetone and other pharmaceutically acceptable organic solvents and the temperature adapted to that specific salt and / or its polymorphic form . to the conditioned solvent hydroxypropylcellulose , hydroxypropylmethylcellulose , or another cellulose derivative is preferably added and stirred until dissolved or suspended . preferably hydroxypropyl cellulose is used . then the active substance is added and stirring is continued for 15 - 90 minutes , after which optionally one or more anticaking agent , plasticizing agent , antifoaming agent and coloring agent is added . preferably , talc is added at a constant stirring rate . stirring is continued after the addition of the last agent for about 15 to 90 minutes . to prepare the final pellet the active substance suspension thus obtained is sprayed onto the isolated pellets as prepared hereinabove . the final pellets as well as the isolated and / or starter pellets may be prepared by the fluidized bed method comprising the following steps : i .) preheating of the cores or pellets , ii .) spraying phase solution or suspension to the cores or pellets , and iii .) drying of the pellets . by a fluidized method is meant that the product to be coated has a fluid , preferably air , flowing through it . the material put in is set in motion and kept in motion by this fluid , the nature of the movement being controlled by different equipment - specific inserts . examples of suitable fluidized bed apparatus are gpcg (= glatt particle coater granulator ), precision coater ( aeromatic ), kugelcoater ( within ) or carried out using the aircoater ( innojet ) or wurster coater . optionally , an overcoat can be applied to the final pellets to increase their abrasion resistance . it is very important for the stability of the final dosage form , in particular pellets , that the moisture content is kept at a minimum . preferably , the loss on drying value of the final dosage form should not exceed 2 %, more preferably 1 . 5 % and most preferably the loss on drying should be less than 1 % ( measured on mettler moisture analyzer , 80 ° c ., 20 min ). additionally , the loss on drying also of the starter and isolated pellets should be minimal . preferably the loss on drying value of the starter and isolated pellets should not exceed 2 %, more preferably 1 . 5 % and most preferably the loss on drying should be less than 1 % ( measured on mettler moisture analyzer , 80 ° c ., 20 min ). the final pellets are usually packed into commercially obtainable capsules such as gelatine or hpmc capsules , or sachets . alternatively , the simple mixture of isolated pellets and dabigatran is filled into capsules or sachets . the capsules may be packed into primary packaging having decreased permeability for water vapor such as high density polyethylene ( hdpe ) containers with closure , such as polypropylene ( pp ) closure and with or without a desiccant ; aluminium foil blisters or polychlorotrifluoroethylene ( aclar ®) blisters or any other suitable water vapor low - permeable packaging such as blisters made of multilayer polymeric foil where different polymeric materials are combined into a single foil . the present invention also relates to a stabilized pharmaceutical product comprising a package and packaging method that utilizes an adsorbent material , such as a molecular sieve , that adsorbs or absorbs moisture in the inner local environment of an impermeable package , so as to prevent hydrolysis and subsequent oxidation products . the adsorbent material can be located in a variety of places . for example , the adsorbent material can be a part of blister foil or can be placed within a porous sachet that , in turn , is located within the sealed package . naturally , numerous adsorbent materials have applications in a stable pharmaceutical product or a method of the present invention , including a molecular sieve , an activated clay , charcoal , an activated alumina , silica , a zeolite , a bauxite , or any mixture of these materials , to name only a few . an effective amount of the adsorbent material used in a stable pharmaceutical product or in a method of the present invention is that amount sufficient to reduce or eliminate the formation of degradation products . one of ordinary skill can readily determine this amount for a particular embodiment of the present invention using routine laboratory techniques . moreover , a sealed package of a stable pharmaceutical product or a method of the present invention can be produced from a variety of materials , e . g . metal , glass , plastic , etc . similarly , the shape of a sealed package can vary . examples of such shapes include , but certainly are not limited to bottle , a bag , a drum box , and an irregularly shaped container . the sealing of a package of a stable pharmaceutical product or a method of the present invention can be accomplished in a variety of ways . more specifically , heat - sealing , gluing , welding , brazing , mechanical closures , mechanical clamps , or compression can hermetically seal a sealed package of a stable pharmaceutical product of the present invention . during the packaging and / or storing controlled conditions with low humidity can be used . additionally inert gases such as nitrogen , argon or helium ; or vacuum can be used during the manufacturing of the solid oral dosage forms , the manufacturing of starter , isolated and final pellets as well as during their packaging to assure inert atmosphere around the solid oral dosage form , such as pellet or capsule , in the sealed primary packaging . inert atmosphere according to present invention means that the concentration of oxygen in the atmosphere around the solid dosage form packed in the primary packaging is less than 10 vol %, preferably less than 5 vol % and most preferably less than 2 vol %. the concentration of oxygen in the atmosphere surrounding the pellets , sachets or capsules can be determined by gas chromatography . 1 .) a process for the preparation of starter pellets , characterized in that a neutral core , chosen from the group of sucrose , microcrystalline cellulose , starch , or a tartaric acid core is coated with a solution of tartaric acid and optionally a binder and / or further inert pharmaceutical excipients without powder layering with tartaric acid . 2 .) a process according to item 1 characterized in that the binder used is acacia , hydroxypropylmethylcellulose , hydroxypropylcellulose or povidone . 3 .) a process according to items 1 or 2 characterized in that the solvent used for the tartaric acid solution is water , ethanol , 2 - propanol or mixtures of ethanol or 2 - propanol with water . 4 .) a process according to items 1 or 2 characterized in that the tartaric acid solution further comprises talc . 5 .) a process according to any of items 1 to 4 , characterized in that the solvent used for the tartaric acid solution is water , ethanol , 2 - propanol or mixtures of ethanol or 2 - propanol with water . 6 .) a starter pellet obtainable by a process according to items 1 to 5 . 7 .) a starter pellet according to item 6 , characterized in that the content of tartaric acid in the first layer is not lower than 50 %, more preferably not lower than 80 % and most preferably not lower than 90 % w / w . 8 .) a process for the preparation of isolated pellets , characterized in that starter pellets as prepared according to any of items 1 to 5 are coated by spraying an isolating suspension comprising a water soluble pharmaceutically acceptable polymer and optionally plasticizers , anticaking agents , antifoaming and / or coloring agents . 9 .) a process according to item 8 , characterized in that the water soluble pharmaceutically acceptable polymer is chosen from hydroxypropyl cellulose , hydroxypropyl methylcellulose , povidone and / or acacia . 10 .) a process according to any of items 8 or 9 , characterized in that the isolation suspension further comprises talc and / or dimethylpolysiloxane . 11 .) an isolated pellet obtainable by a process according to items 8 to 10 . 12 .) a process for the preparation of final dabigatran pellets , characterized in that isolated pellets as prepared according to any of items 1 to 10 are coated by spraying an active substance suspension onto the isolated pellets . 13 .) a process according to item 12 , characterized in that the active substance suspension is prepared using dabigatran etexilate methanesulfonate in the form of its polymorph i . 14 .) a process according to any of items 12 or 13 , characterized in that 2 - propanol is used for the preparation of the active substance suspension . 15 .) a process according to any of items 12 to 14 , characterized in that the active substance suspension comprises hydroxypropylcellulose . 16 .) a final pellet obtainable by a process according to items 12 to 15 . 17 .) a final pellet according to item 16 , characterized in that it also comprises an overcoat . 18 .) a final pellet according to any of items 16 or 17 , characterized in that it comprises less than 20 % w / w tartaric acid . 19 .) a final pellet according to any of items 16 to 18 , characterized in that it is packed into a gas and moisture impervious packaging . 20 .) a final pellet according to item 19 , characterized in that the sealed primary packaging is flushed with nitrogen prior to sealing . the present invention is further illustrated by the following non - limiting examples . preparation of a1 - 7 : the binder and tartaric acid are dissolved in a first part of purified water . talc is suspended in the second part of purified water and added to the obtained solution . the resulting coating suspension is sprayed onto the sugar cores and the obtained starter pellets are dried until the desired lod ( loss on drying ) is achieved . preparation of a8 - 13 : tartaric acid is dissolved in a suitable quantity of purified water and the same quantity of ethanol is added . the resulting solution is sprayed onto starter beads and the obtained pellets are dried until the desired lod is achieved . preparation of a14 - 15 : tartaric acid is dissolved in a suitable quantity of purified water . 2 - propanol is added in an amount sufficient to reduce tackiness of the solution . the obtained solution is sprayed onto cores and the obtained starter pellets are dried until the desired lod is achieved . the binder and tartaric acid are dissolved in a first part of purified water . talc is suspended in the second part of purified water and added to the obtained tartaric acid solution . the resulting coating suspension is sprayed onto the sugar cores to give starter pellets which are dried until desired lod is achieved . preparation of b1 - 2 : hpmc is added to ethanol and stirred . when dissolved , dimeticone is added . talc is suspended in a part of ethanol with ultraturax and added to the hpmc solution . the obtained suspension is sprayed onto the starter pellets . preparation of b3 : acacia is dissolved in purified water , then dimeticone is added . talc is suspended in part of purified water and added to the obtained solution . the resulting suspension is sprayed onto the starter pellets . preparation of b4 : acacia is dissolved in purified water . talc is suspended in part of purified water and added to the obtained solution . the resulting suspension is sprayed onto the starter pellets . hpmc pharmacoat 606 is added to ethanol and stirred . when dissolved , dimeticone is added . talc is suspended in a part of ethanol with ultraturax and added to the hpmc solution . the suspension is sprayed onto the starter pellets . hydroxypropyl cellulose is added to part of 2 - propanol and stirred . when dissolved , dabigatran etexilate methanesulphonateis dissolved . talc is suspended in part of 2 - propanol with ultraturax and the suspension is added to the hpc solution ). the obtained suspension is sprayed onto isolated pellets b1 and the obtained pellets are dried until appropriate lod is achieved . hydroxypropyl cellulose klucel ef is added to part of 2 - propanol and stirred . when dissolved , milled dabigatran etexilate methanesulphonate methanesulphonate having a d50 particle size of 6 . 7 μm and a d90 particle size of 15 . 7 μm is added . talc is suspended in part of 2 - propanol with ultraturax and the suspension is added to the klucel solution . the obtained suspension is sprayed onto isolated pellets b1 and the obtained pellets are dried until appropriate lod is obtained . preparation of d1 - 2 : hpmc or povidone is added to part of ethanol and mixed . talc and titanium dioxide are suspended in part of ethanol with ultraturax and mixed to hpmc or povidone solution . the obtained mixture is sprayed onto pellets , which are then dried until the required lod is achieved .
the invention relates to pharmaceutical oral dosage forms of the active substance ethyl 3 -- phenylamino ]- methyl }- 1 - methyl - 1h - benzimidazole - 5 - carbonyl )- pyridin - 2 - yl - amino ]- propionate and the pharmacologically acceptable salts thereof , in particular dabigatran etexilate methanesulfonate .