the present invention consists in a multi tablet capsule delivery system . each capsule of the said delivery system contains 1 - 6 mini tablets , containing the pharmacologically active water - soluble substance substance venlafaxine hcl . each one of the said tablets comprises of a functional core , which is partially or totally coated with an appropriate coating agent , so that the surface of the core that is initially available for drug delivery is limited . i . the drug substance , venlafaxine hcl , in a proportion that varies between 10 - 40 % by weight ii . 40 - 80 % of a gelling agent . this gelling agent can be chosen among ; hydroxypropylmethylcellulose , hydroxypropylcellulose , hydroxycellulose phthalate , poly ( ethyleneoxide ), polylactic acid , xanthan gum , alginates , sodium and calcium carboxymethylcellulose , carragheen , carbomer , carbopol ( oral use ), methylhydroxyethylcellulose , propylhydroxyethylcellulose , polyhema , methylcellulose , alginates and other swellable polymers . the swelling agent used in the formulation should preferably be of high viscosity , as the incorporated drug substance is highly soluble in water and the diffusion rate through the gelling agent should be limited , without beholding the drug substance after the desired time window . iii . 30 - 60 % of a non - swellable ( also characterized as monolithic or plastic ) agent or system comprising of one or a mixture of water insoluble , non - swelling polymers such as : ethyl cellulose , cellulose acetate propionate , cellulose acetate , poly ( ethyl acrylate , methyl metlacrylate , trimethylammonioethyl methacrylate chloride ) 1 : 2 : 0 . 1 , commerced as eudragit rs 100 , poly ( ethyl acrylate , methyl methacrylate , trimethylammonioethyl methacrylate chloride ) 1 : 2 : 0 . 2 copolymer , commercially available as eudragit rl ®, polyvinylpyrrolidone acetate , polyvinyl chloride , polyvinyl acetate , polyethylene , and others . the function of these compounds is to limit the swelling rate of the gelling agent and to reduce the penetration of water through the pores that are formed by the swelling of the gelling agent and the diffusion of the drug substance from the core . iv . a conjugation agent , a surfactant or a polymer that forms bonds between the gelling agent and the non swellable agent , or between the drug substance and the gelling or the non swellable agent , causing interactions between the constituents of the core that limit its swelling properties . surfactants that are used as conjugation agents are usually anionic , as sodium lauryl sulphate , sodium docusate , sodium cetostearyl sulphate and triethanolamine lauryl sulphate , in proportions 2 - 12 % by weight . non ionic compounds , such as polysorbates exhibit weak conduction ability , while cationic surfactants do not have such properties . polymers used as binding agents between the gelling agent and the drug substance are polyvinylpyrrolidone , polyvinyl alcohol and polyvinylpyrroliudone acetate , in proportions of 10 - 30 % by weight . v . 1 - 30 % by weight of classical excipients such as : a . lubricants and glidants , as mg , ca and zn stearate , silicon dioxide , talc and stearic acid , or any other insoluble in water lubricant or glidant . b . binders : the binders adopted for the invention should not be feely soluble in water . for example , polyvinylpyrrolidone acetate is preferred over polyvinylpyrrolidone as it obtains sustained release properties and enhances the relevant behavior of the core . c . diluents : any diluents free of disintegrating properties such as talc , dicalcium phosphate and calcium sulphate dihydrate could be adopted . the classical excipients used for the preparation of the core should exhibit low solubility in water and free of disintegrant properties . the core can be obtained by either a direct compression process , or through a wet granulation and compression process . in order to optimize the cohesiveness of the core a wet granulation process step is essential . the gelling agent ( s ), the active ingredient , the non - swelling polymers and the conjugation agent ( s ) are mixed together , comprising the internal phase to be submitted to the wet granulation step . the solvent used for the wet granulation step could be any suitable solvent for use in the manufacture of oral dosage forms . the solvent or mixture of solvents should be able to dilute or disperse the drug substance , the swellable polymers , the non - swellable polymers and the conduction agent , so that the interactions between the above compounds can be developed . such solvents are ethanol , acetone , isopropyl alcohol , water and mixtures of the said solvents . alternatively the non - swelling compound is dissolved into an appropriate co - solvent preparing a 5 - 40 % solution or uniform dispersion that is used for the wet granulation step of the rest of the constituents of the internal phase . the conduction agent may also be diluted or dispersed in the granulation fluid . any diluents or binders may be added in the internal phase . after drying , the granule mass is mixed with the excipients comprising the external phase ( glidants , lubricants and binders ) and the granular / powder mixture is compressed into tablets . the core is partially or totally coated by a coating layer or a coating film that reduces the initial rapid release of the water - soluble drug substance from the core , via two mechanisms . i . by reducing the surface of the core that is initially available for the release of the drug substance , during the initial stages of the wetting of the dosage form of the said formulation . ii . by suppressing the core and in particular the swellable gelling agents . this way the penetration of water through the core that causes the diffusion of the drug substance and its rapid release during the initial steps of the wetting of the core is limited and the “ burst ” phenomenon is restricted . the coating layer is applied on ( as described in fig1 ): i . one surface of the core with thickness that ranges between 3 - 30 % of the diameter of the core , providing a two - layer tablet . ii . two surfaces of the core with thickness that ranges between 3 - 30 % of the diameter of the core , providing a three - layer tablet . iii . one surface and the perimeter of the core with thickness . that ranges between 3 - 30 % of the diameter of the core , forming a “ cap ” that covers the larger part of the core , leaving only one flat surface for the release of the drug substance . the coating layer comprises of a polymer and a water - soluble compound . the polymer can be a swelling agent or a non - swelling agent , similar to the ones used for the core . the water soluble compound can be : i . a water soluble salt such as sodium chloride , sodium bicarbonate , or any other water soluble salt that can be used as an excipient in a solid oral pharmaceutical formulation . ii . a water soluble small organic compound like mannitol , lactose , sucrose , sorbitol , citric acid or any other water soluble , low relative molecular mass organic compound that can be used as an excipient in a solid oral pharmaceutical formulation . iii . a water - soluble polymer like polyvinylpyrrolidone , polyvinyl alcohol , low viscosity hydroxyprolylmethyl cellulose , or any other water - soluble polymer that can be used as an excipient in a solid oral pharmaceutical formulation . during the initial stages of the wetting of the coating layer the water - soluble compounds dissolve rapidly , creating pores through the drug substance can be diffused and released . the polymer reduces the diffusion of the drug substance by reducing the surface of the core that is available for the dissolution of the drug substance . the function of the coating layer is time limited with an optimal duration from 0 up to 2 - 4 hours of the drug release . the function of the coating layer is advanced and terminated through two different mechanisms , depending on the kind of polymer that is enabled : i . in the case of swellable polymers the wetting of the polymer causes the formation of moving boundaries delimiting different physical conditions inside the matrix of the coating layer ( dry coating material , swollen polymer , dissolved / undissolved polymer ). the polymer swells through a swelling front that is followed by a diffusion front , through which soluble compounds can be diffused through the mass of the polymer and be released and an eroding front through which the polymer dissolves into the surrounding fluids . the termination of the function of the coating layer consisting of swellable polymers coincides with the extension of the diffusion layer up to the surface of the core . after that stage the surface of the core that was covered by the polymer layer can be hydrated and the drug substance can be diffused through the swollen polymer . ii . in the case of non - swellable polymers the termination of the function of the coating layer is achieved by the breaking of the inelastic coating layer due to the swelling of the core as the core is hydrated through the free surfaces and the pores that are created after the soluble compound of the coating layer is dissolved . i . the composition of the coating layer and more specifically the polymer - soluble compound ratio . the polymer is usually added at a 1 : 1 to 9 : 1 ratio to the water - soluble compound . ii . the thickness of the coating layer iii . the kind of the polymer and the kind of the soluble compound iv . in the case of non - swellable polymers the resistance of the coating layer is also depended on the presence and the percentage of plasticizers . the plasticizers are used in a percentage that ranges between 0 - 10 % and increase the elasticity and consequently the endurance of the coating layer . this way the time period that the coating layer is functional can be controlled through another parameter , the percentage of the plasticizer . plasticizers used in such formulations are polyethylene glycol , triethyl citrate , glycerol , 1 , 2 propylene glycol . the coating layer is applied on the core by a compression process , after mixing the excipients that compose it . as a result the coating layer may contain classical excipients used in direct compression processes , such as glidants , lubricants , diluents and binders . in contrast with the formulation of the cores the coating layer may contain disintegrating agents ( such as microcrystalline cellulose , pregelatinized starch , sodium starch glycollate and calcium carboxymethyl cellulose ) in proportion between 0 - 5 %, as long as these agents enhance the formation of pores through the polymer mass and do not affect the continuity of the coating layer during the early stages of the drug release . the cores may also be film coated . similarly to the coating layer , the coating material is functional for a determined period of time that does not exceed the first 4 hours of the drug release from the core . the film coating usually represents from 1 . 5 to 18 %, by weight of the weight of the mini tablet . the film coating material contains a polymer at a proportion that ranges between 10 - 80 % of the dry mass of the coating material . the said polymer creates a film that covers the core , reducing the surface of the core that is initially available for the dissolution of the drug substance . the delivery of the drug substance in the initial stages of the wetting of the coated mini tablets is through pores that are created by the dissolution of water soluble compounds that the coating film contains in a proportion that usually ranges from 20 - 50 % by weight . i . swellable polymers such as those recited above with respect to the formulation of the core . ii . non - swellable such as those recited above with respect to the formulation of the core . iii . ph - dependent polymers that are insoluble in acidic environment ( like the gastric fluids ), while they dissolve in slightly acidic ( ph 4 . 5 - 5 . 5 ), neutral or slightly basic ph ( 6 . 0 - 8 . 0 ). such polymers are : a ) cellulose acetate phthalate , a polymer that dissolves at ph values over 6 . 4 . b ) poly ( butyl methacrylate , ( 2 - dimethyl aminoethyl ) methacrylate , methyl methacrylate ) 1 : 2 : 1 copolymer , commercially available as eudragit e ®, that dissolves in ph values lower than 5 . c ) poly ( ethyl acrylate , methyl methacrylate ) 2 : 1 copolymer , commercially available as eudragit 30d ®, that dissolves in ph values of about 5 . 5 . d ) poly ( methacrylic acid , methyl methacrylate ) 1 : 1 copolymer , commercially available as eudragit l ®, that dissolves in ph values of about 6 . 7 . e ) poly ( methacrylic acid , methyl methacrylate ) 1 : 2 copolymer , commercially available as eudragit s ®, that dissolves in ph values of about 6 . 7 . the water - soluble compound may be the same as the ones recited above with respect to the water - soluble compounds of the coating layer . the coating material may also contain classical excipients such as those recited above with respect to the formulation of the core , as well as plasticizers ( such as those recited above with respect to the formulation of the coating layer ), colourants ( e . g . quinoline yellow , indigotine , sunset yeloow ), opacifiers ( usually titanium dioxide ), adhesive agents ( such as low viscosity hydroxypropyl methyl cellulose , hydroxypropyl cellulose and polyvinylpyrrolidone ), at a total proportion that ranges between 10 - 50 % by weight of the total weight of the dry coating material . ethanol , acetone , water isopropyl alcohol , methylene chloride , chloroform or any other pharmaceutically suitable solvent may be used , as well mixtures of the said solvents , as long as can dissolve or uniformly disperse the constituents of tile coating mixture . the solid content of the coating solution or dispersion typically ranges between 3 - 40 % by weight . the dissolution or dispersion of the solid content of the coating material may be optimised by the use of polyethylene glycol in an amount from 0 to 10 % by weight of the coating material . in the case of the film coating the function of the coating is terminated at an optimal time period as said above . the mechanisms that cause the termination of the function of the film coating are : i . in the case of coating films consisting of swellable polymers the function of the coating is terminated when the diffusion layer reaches the surface of the core . after that stage the surface of the core that was covered by the polymer layer can be hydrated and the drug substance can be diffused through the swollen polymer , similarly to the process recited above for the coating layers . ii . in the case of coating films consisting of non - swellable polymers the function of the coating is terminated when the swelling of the core breaks the polymer layer , similarly to the process recited above for the coating layers . the diffusion of the soluble compound creates pores through the core can be hydrated and swell . iii . in the case of ph - dependent polymer films the function of the coating is terminated through two potential mechanisms : firstly the same mechanism that occurs when the non - swelling polymers are enabled and secondly the change of the ph of the aqueous environment throughout the gastrointestinal track . one preferred embodiment is a capsule containing an appropriate number of mini tablets , in a way that linearity between the strength and the total weight of the dosage form is achieved ( 1 to 6 mini tablets per capsule ). i . a functional core comprising venlafaxine hcl , one or more gelling agents , one or more non - swelling agents , one or more conjugation agents and appropriate quantities of classical excipients ii . a functional coating comprising an enteric film coating containing water - soluble compound . example 1 . 1 : a 0 or 00 size capsule containing 1 - 6 venlafaxine 25 mg coated mini - tablets example 1 . 2 : a 0 or 00 size capsule containing 1 - 4 venlafaxine 37 . 5 mg coated mini - tablets example 1 . 3 : a 0 or 00 size capsule containing 1 - 3 venlafaxine 50 mg coated mini - tablets example 1 . 4 : a 0 or 00 size capsule containing 1 - 2 venlafaxine 75 mg coated mini - tablets venlafaxine venlafaxine venlafaxine venlafaxine % in the ingredient 25 mg core 37 . 5 mg core 50 mg core 75 mg core core venlafaxine hcl ( equivelant to 28 . 30 42 . 45 56 . 60 84 . 90 26 . 87 1 : 1 . 132 venlafaxine base ) sodium lauryl sulphate 7 . 37 11 . 06 14 . 75 22 . 12 7 . 00 eudragit rs 100 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 methocel k100 m 62 . 06 93 . 09 124 . 12 186 . 18 58 . 92 magnesium stearate 0 . 53 0 . 79 1 . 05 1 . 58 0 . 50 total 105 . 33 158 . 00 210 . 67 316 . 00 100 . 00 manufacturing process : venlafaxine hcl , methocel k 100 m ®, and sls are sieved through a 30 mesh sieve and mixed for an appropriate time period until a uniform mixture is formed . this mixture comprises the internal phase of the formulation . eudragit rs 100 ® is dissolved in acetone , preparing a wet granulation fluid . the constituents of the internal phase are wet granulated using the wet granulation fluid . the granular mixture is dried to constant weight in an oven at 40 ° c . ( the total content in solvents is estimated using the loss on drying method as described in the european pharmacopoeia 3 rd edition and should be less than 1 . 5 %). the dry granule is mixed with the rest of the excipients in a drum mixer and the resulting mixture is pressed into biconvex tablets ( almost spherical in shape ) of appropriate mass relatively to the strength and hardness using a killian ® tabletting machine . for the venlafaxine 25 mg cores 5 mm punches were used , for the 37 . 5 and 50 mg cores 6 mm punches were used , while for the 75 mg cores 7 mm punches were used . the mini - tablets are placed into 00 - sized capsules . venlafaxine venlafaxine venlafaxine venlafaxine % in the ingredient 25 mg core 37 . 5 mg core 50 mg core 75 mg core core venlafaxine hcl ( equivelant to 28 . 30 42 . 45 56 . 60 84 . 90 26 . 87 1 : 1 . 132 venlafaxine base ) sodium lauryl sulphate 5 . 00 7 . 50 10 . 00 15 . 00 4 . 75 eudragit rs 100 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 methocel k100 m 57 . 36 86 . 04 114 . 72 172 . 08 54 . 46 kollidon sr 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 magnesium stearate 0 . 53 0 . 79 1 . 05 1 . 58 0 . 50 total 105 . 33 158 . 00 210 . 67 316 . 00 100 . 00 manufacturing process : the same manufacturing process as the one recited above with respect to the core of example 2 . 1 . kollidon sr ® is a commercial name for polyvinulpyrolidon acetate and it was added in the internal phase . venlafaxine venlafaxine venlafaxine venlafaxine % in the ingredient 25 mg core 37 . 5 mg core 50 mg core 75 mg core core venlafaxine hcl ( equivelant to 28 . 30 42 . 45 56 . 60 84 . 90 26 . 87 1 : 1 . 132 venlafaxine base ) sodium lauryl sulphate 6 . 32 9 . 48 12 . 64 18 . 96 6 . 00 eudragit rs 100 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 methocel k100 m 56 . 04 84 . 06 112 . 08 168 . 12 53 . 20 kollidon sr 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 magnesium stearate 0 . 53 0 . 79 1 . 05 1 . 58 0 . 50 total 105 . 33 158 . 00 210 . 67 316 . 00 100 . 00 manufacturing process : the same manufacturing process as the one recited above with respect to the core of example 2 . 1 . kollidon sr ® is a commercial name for polyvinulpyrolidon acetate and it was added in the internal phase . venlafaxine venlafaxine venlafaxine venlafaxine % in the ingredient 25 mg core 37 . 5 mg core 50 mg core 75 mg core core venlafaxine hcl ( equivelant to 28 . 30 42 . 45 56 . 60 84 . 90 26 . 87 1 : 1 . 132 venlafaxine base ) sodium lauryl sulphate 8 . 43 12 . 64 16 . 85 25 . 28 8 . 00 eudragit rs 100 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 methocel k100 m 53 . 93 80 . 90 107 . 87 161 . 80 51 . 20 kollidon sr 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 magnesium stearate 0 . 53 0 . 79 1 . 05 1 . 58 0 . 50 total 105 . 33 158 . 00 210 . 67 316 . 00 100 . 00 manufacturing process : the same manufacturing process as the one recited above with respect to the core of example 2 . 1 . kollidon sr ® is a commercial name for polyvinulpyrolidon acetate and it was added in the internal phase . venlafaxine venlafaxine venlafaxine venlafaxine % in the ingredient 25 mg core 37 . 5 mg core 50 mg core 75 mg core core venlafaxine hcl ( equivelant to 28 . 30 42 . 45 56 . 60 84 . 90 26 . 87 1 : 1 . 132 venlafaxine base ) sodium lauryl sulphate 8 . 43 12 . 64 16 . 85 25 . 28 8 . 00 eudragit rs 100 14 . 15 21 . 22 28 . 29 42 . 44 13 . 43 methocel k100 m 35 . 57 53 . 36 71 . 15 106 . 72 33 . 77 kollidon sr 14 . 15 21 . 22 28 . 29 42 . 44 13 . 43 magnesium stearate 0 . 53 0 . 79 1 . 05 1 . 58 0 . 50 talc 4 . 21 6 . 32 8 . 43 12 . 64 4 . 00 total 105 . 33 158 . 00 210 . 67 316 . 00 100 . 00 manufacturing process : the same manufacturing process as the one recited above with respect to the core of example 2 . 1 . kollidon sr ® is a commercial name for polyvinylpyrrolidon acetate and it was added in the internal phase . venlafaxine venlafaxine venlafaxine venlafaxine % in the ingredient 25 mg core 37 . 5 mg core 50 mg core 75 mg core core venlafaxine hcl ( equivelant to 28 . 30 42 . 45 56 . 60 84 . 90 26 . 87 1 : 1 . 132 venlafaxine base ) hpc 5 . 00 7 . 50 10 . 00 15 . 00 4 . 75 eudragit rs 100 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 methocel k100 m 57 . 36 86 . 04 114 . 72 172 . 08 54 . 46 kollidon sr 7 . 07 10 . 61 14 . 15 21 . 22 6 . 72 magnesium stearate 0 . 53 0 . 79 1 . 05 1 . 58 0 . 50 total 105 . 33 158 . 00 210 . 67 316 . 00 100 . 00 manufacturing process : the same manufacturing process as the one recited above with respect to the core of example 2 . 1 . kollidon sr ® is a commercial name for polyvinulpyrrolidon acetate and it was added in the internal phase . the release profiles of the above formulations were tested using a dissolution apparatus with paddles at 100 rpm using 500 ml of a ph 1 . 2 solution for the first two hours and 1000 ml of phosphate buffer solution for the rest of the test ( total duration 24 h ). the results of the dissolution tests are presented in the following table ( table 1 ) and fig2 : similar results were noticed when the other strengths were tested for the release of the drug substance , as well as when combinations of the above cores were tested . the cores containing a conjugation agent exhibited lower initial release of the drug substance venlafaxine hcl , in a degree the ranges between 3 - 10 %. there is an optimal ratio between the quantities of the swelling polymer , the non - swelling polymer and the conjugation agent . at this ratio the initial release of venlafaxine hcl from the formulation is reduced , while the drug substance is quantitatively released from the core at the end of the test ( set at 24 hours ). the following examples of the coating layer are applied using the core described in example 2 . 1 as a model core , so that the effect of the coating layer on the formulation can be evaluated . the 75 mg core was enabled as a worst case as it is the core with the biggest surface . example 3 . 1 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 1 coating layer constituents % cellulose acetate propionate 99 . 0 magnesium stearate 1 . 0 the constituents of the coating layer are mixed until a uniform powder mixture is prepared . then the coating layer is applied by compression on the precompressed core . for the two layer and the three layer tablets the coating layer is applied using the same punches as the ones used for the compression of the core . in the case that the perimeter and one side of the core are coated the punch used for the application of the coating layer is of bigger diameter ( usually 1 to 4 mm larger than the diameter of the core ). two levels of the thickness of the coating layer were tested , 1 . 0 and 2 . 0 mm , as for the effect of the coating layer on the dissolution profile of complex tablets . example 3 . 2 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 2 coating layer constituents % methocel e 50lv 99 magnesium stearate 1 manufacturing process : the same manufacturing process as the one recited above with respect to the coating layers of example 3 . 1 . example 3 . 3 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 3 coating layer constituents % polyox 900000 99 magnesium stearate 1 manufacturing process : the same manufacturing process as the one recited above with respect to the coating layers of example 3 . 1 . example 3 . 4 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 4 cellulose acetate propionate 79 . 0 pvp 20 . 0 magnesium stearate 1 . 0 manufacturing process : the same manufacturing process as the one recited above with respect to the coating layers of example 3 . 1 . example 3 . 5 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 5 cellulose acetate propionate 74 . 0 pvp 20 . 0 peg 5 . 0 magnesium stearate 1 . 0 manufacturing process : the same manufacturing process as the one recited above with respect to the coating layers of example 3 . 1 . example 3 . 6 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 6 cellulose acetate propionate 71 . 5 pvp 17 . 5 peg 10 . 0 magnesium stearate 1 . 0 manufacturing process : the same manufacturing process as the one recited above with respect to the coating layers of example 3 . 1 . example 3 . 7 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 7 methocel e 50lv 79 . 0 pvp 20 . 0 magnesium stearate 1 . 0 manufacturing process : the same manufacturing process as the one recited above with respect to the coating layers of example 3 . 1 . example 3 . 8 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating layer : example 3 . 8 methocel e 50lv 79 . 0 lactose 20 . 0 magnesium stearate 1 . 0 manufacturing process : the same manufacturing process as the one recited above with respect to the coating layers of example 3 . 1 . the release profiles of the above complex systems were tested using a dissolution apparatus with paddles at 100 rpm using 500 ml of a ph 1 . 2 solution for the first two hours and 1000ml of phosphate buffer solution for the rest of the test ( total duration 24 h ). the results of the dissolution tests performed for the most typical of the above systems are presented in the following tables : the above results show that the said complex systems can be applied with great flexibility and cause an extensive reduction of the initial drug release . this reduction ranges from 2 to 13 . 5 %, while the duration of the function of the coating layer can also be controlled and manipulated . the following examples of the coating films are applied on the core described in example 2 . 1 as a model core , so that the effect of the coating film on the formulation can be evaluated . the 75 mg core was enabled as a worst case as it is the core with the biggest surface . example 4 . 1 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating film : example 4 . 1 coating film constituents % eudragit rs 50 . 0 peg 5 . 0 talc 15 . 0 lactose 20 . 0 magnesium stearate 10 . 0 solvents : acetone , acetone : ethanol 1 : 1 manufacturing process : the constituents of the coating film are dispersed in the solvent mixture preparing a homogeneous dispersion of 5 - 15 % solid content . then the coating film is spray - coated on the cores that were preheated at 70 ° c . the coating process was completed when the film coating of each core reached a weight of 7 - 10 % of the weight of the core . the film coated cores were dried for 2 hours at 40 ° c . example 4 . 2 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating film : example 4 . 2 coating film constituents % ethyl cellulose 30 . 0 hpmc 50 cp 20 . 0 peg 5 . 0 talc 15 . 0 pvp 20 . 0 magnesium stearate 10 . 0 solvents : acetone : isopropanol 1 : 1 manufacturing process : the same manufacturing process as the one recited above with respect to the coating film of example 4 . 1 . example 4 . 3 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating film : example 4 . 3 coating film constituents % cellulose acetate propionate 30 . 0 hpmc 50 cp 10 . 0 peg 15 . 0 talc 15 . 0 pvp 20 . 0 magnesium stearate 10 . 0 solvents : acetone : isopropanol 1 : 1 manufacturing process : the same manufacturing process as the one recited above with respect to the coating film of example 4 . 1 . example 4 . 4 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating film : example 4 . 4 coating film constituents % cellulose acetate phthalate 30 . 0 ethyl cellulose 10 . 0 peg 15 . 0 talc 15 . 0 pvp 20 . 0 magnesium stearate 10 . 0 solvents : acetone : ethanol 1 : 1 , acetone , acetone : h20 97 : 3 manufacturing process : manufacturing process : the same manufacturing process as the one recited above with respect to the coating film of example 4 . 1 . example 4 . 5 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating film : example 4 . 5 coating film constituents % kollicoat sr 30 d 60 . 0 propylene glycol 12 . 5 talc 7 . 5 pvp 10 . 0 magnesium stearate 10 . 0 water manufacturing process : the same manufacturing process as the one recited above with respect to the coating film of example 4 . 1 . example 4 . 6 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating film : example 4 . 6 coating film constituents % eudragit l 12 . 5 eudragit s 37 . 5 dibutyl sebacate 5 . 0 talc 15 . 0 lactose 20 . 0 magnesium stearate 10 . 0 solvents : acetone : isopropanol 1 : 1 manufacturing process : the same manufacturing process as the one recited above with respect to the coating film of example 4 . 1 . example 4 . 7 : based on the core described in example 2 . 1 and the following formulation was prepared for the coating film : example 4 . 7 coating film constituents % eudragit l 37 . 5 eudragit s 12 . 5 dibutyl sebacate 5 . 0 talc 15 . 0 pvp 20 . 0 magnesium stearate 10 . 0 solvents : acetone : isopropanol 1 : 1 manufacturing process : the same manufacturing process as the one recited above with respect to the coating film of example 4 . 1 . the above results show that the coating films can be applied with great flexibility and cause an extensive reduction of the initial drug release . this reduction ranges from about 3 to about 13 %, while the duration of the function of the film coating can also be controlled and manipulated .
the invention provides a sustained release composition that ; 1 . is free of initially increased drug delivery that occurs ( in sustained release systems containing the water soluble drug venlafaxine hcl , known as burst phenomenon , by using a functional core partially or totally coated by a functional coating layer or film . 2 . delivers the drug substance within 24 hours and is therefore suitable for once daily administration of the said drug substance . 3 . exhibits linearity between the strength dosage form and the ( total mass of the dosage form , by proportional increase of the amounts of the drug substance and the excipients in the formulation . 4 . is possible to be divided in smaller doses , without affecting the release of the drug substance . the invention provides a sustained release capsule formulation containing an appropriate number of functional complex mini tablets comprising of : i . a functional core comprising the active ingredient , especially the water - soluble drug venlafaxine hcl and appropriate excipients . 2 . a functional coating layer or film that reduces the initial surface of the core that is available for the release of the water - soluble drug venlafaxine hclt phenomenon .