in particular , according to a first aspect of the present invention , it was found that the pharmaceutical formula of thyroid hormones ( in particular of t3 and / or t4 or their salts , preferably their sodium salts ) in a uniform matrix of soft - gel which can be taken by mouth without chewing ( and that is in which the uniform matrix is composed of a three - dimensional body having the form and dimensions of a normal tablet or intense capsule for taking orally ), said matrix comprising , in the dried state , 30 %- 68 % in weight of gelatine of bovine , pig or fish origin , and characterised in that they comprise , in the dried state , 31 - 60 % in weight , preferably 32 - 55 % in weight of glycerol and 1 - 10 % in weight of water , offers considerable advantages in relation to normal administration in the known pharmaceutical forms which did not have an acceptable shelf - life . by the term dried state is meant , preferably , the state reached by the pharmaceutical formula after drying at a temperatures of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is reached , that is until two weighing operations carried out at a distance of 24 hours do not vary by more than 1 %. the uniform matrices of soft - gel of the present invention comprise t3 and / or t4 or their salts , preferably their sodium salts , in pharmaceutically acceptable quantities , preferably 0 . 001 - 1 % in weight . optionally , the uniform matrices of soft - gel of the present invention may be provided on the outside with enteric layers formulated according to known techniques so that they decompose substantially in the environment of the small intestine which is the principal site of absorption of thyroid hormones . besides ( or instead of ) enteric layers , the uniform matrices of soft - gel of the present invention may optionally present also further layers that facilitate ingestion , that is which are composed of excipients that reduce friction between the capsule and the patient &# 39 ; s oesophagus . the materials used to obtain the uniform matrices of soft - gel of the present invention are the so - called type a or b gelatines of bovine , pig and fish origin usually used in pharmaceutical technique for making capsules . in the uniform matrices of soft - gel of the present invention , the gelatines are present , in the dried product , from 30 % to 68 % in weight . a representative , but not exclusive example of a gelatine that may be used in the present invention is a gelatine with the following amino acidic profile : glycine : 26 %, alanine : 9 %, isoleucine : 1 . 5 %, leucine : 3 . 4 %, valine : 2 . 5 %, serine : 3 . 5 %, threonine : 2 %, proline : 16 %, phenylalanine : 2 . 4 %, tyrosine : 0 . 8 %, tryptophane : 0 %, methionine : 0 . 8 %, histidine : 0 . 8 %, arginine : 9 %, lysine : 5 %, aspartic acid : 6 %, glutamic acid : 11 %, hydroxyproline : 13 . 5 % and hydroxylysine : 1 %. preferably , the gelatines that may be used in the present invention have a grain size between 4 and 100 mesh and a ph between 3 and 10 . the solvent used necessarily in obtaining the uniform matrices of soft - gel of the present invention is glycerol , which must be present , in the dried product , with 31 - 60 % in weight , preferably with 32 - 55 % in weight , even more preferably with 32 . 5 %- 50 % in weight . a further solvent used in obtaining the uniform matrices of soft - gel of the present invention is water , which remains present , in the dried product , in a quantity of 1 - 10 % in weight . a further solvent that may be used in obtaining the uniform matrices of soft - gel of the present invention is ethanol which , when used , remains present , in the dried product , in a quantity of 0 . 5 - 5 % in weight . further solvents which may be used in obtaining the uniform matrices of soft - gel of the present invention are other polyhydroxy or polyether alcohols , such as for example sorbitol / sorbitans , 1 , 2 - propylenglycol , polyethylenglycols and mannitol or mixtures thereof . when these further solvents are used , they or their mixtures are added in quantities such as to remain present , altogether , in the dried product , in a quantity of 3 - 10 % in weight . further components that may be used in obtaining the uniform matrices of soft - gel of the present invention are excipients , for example all the usual pharmaceutically acceptable solid additives which may be used to modify the characteristics of the release of thyroid hormones from the resulting uniform matrix of soft - gel . further excipients that may be used in obtaining the uniform matrices of soft - gel of the present invention are colouring agents and / or preservatives such as parabenes , preferably methylparahydroxybenzoate , ethylparaoxybenzoate or propylparahydroxybenzoate . according to a particularly advantageous aspect of the present invention , the pharmaceutical formulae of thyroid hormones in uniform matrices of soft - gel can be obtained with two different procedures which both use the so - called “ rotary die ” machines commonly used in the pharmaceutical technique for producing soft capsules with a liquid or semi - liquid content . the specific contrivances proposed by the procedures of the present invention mean that , instead of the classic two - phase capsules , comprising a casing and a content of different consistency , “ full ” capsules are obtained , that is uniform matrices of soft - gel which are perfectly single - phase . according to a first procedure concerning the first aspect of the present invention , all the necessary components for obtaining the pharmaceutical composition in a uniform matrix of soft - gel of the present invention are mixed and the mixture is fed into a “ rotary die ” type machine for forming capsules , which then forms “ full ” capsules without injected material . these “ full ” capsules constitute the pharmaceutical compositions in uniform matrices of soft - gel of the present invention . according to a first variation of the first procedure concerning the first aspect of the present invention , all the necessary components for obtaining the pharmaceutical composition in a uniform matrix of soft - gel of the present invention are mixed , obtaining a medicated gelatinous mixture , the medicated gelatinous mixture is brought to melting point and fed into a “ rotary die ” type machine for forming capsules , which then forms “ full ” capsules without injected material . these “ full ” capsules constitute the pharmaceutical compositions in uniform matrices of soft - gel of the present invention . in particular , according to the first variation of the first procedure concerning the first aspect of the present invention , to prepare a pharmaceutical composition of thyroid hormones in a uniform matrix of soft - gel , the following steps are performed : preparation of a medicated gelatinous mixture comprising 10 - 50 % in weight of type a or b gelatine of bovine , pig or fish origin , 10 - 50 % in weight of glycerol , 0 - 10 % in weight of ethanol , 20 - 80 % in weight of water and 0 . 001 - 1 % in weight of t3 and / or t4 or their salts , melting of the medicated gelatinous mixture at a temperature between 30 ° and 55 ° c ., preferably between 35 ° and 45 ° c ., feeding of the medicated gelatinous mixture into the cavities of the shaping cylinders of a “ rotary die ” type machine for forming capsules , cutting and taking the pharmaceutical composition in a uniform matrix of soft - gel thus formed from the “ rotary die ” machine , and preferably , the “ rotary die ” machines are operated in an environment having a temperature between 20 ° c . and 24 ° c . and a relative humidity between 5 % and 35 %, preferably around 20 %. preferably , the pharmaceutical composition in a uniform matrix of soft - gel obtained as above is dried at a temperature of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %. if contemplated , further solvents , such as polyhydroxy or polyether alcohols , excipients , preservatives and / or colouring agents can be added to the medicated gelatinous mixture obtained in the first step . according to a second variation of the first procedure concerning the first aspect of as the present invention , some of the necessary components for obtaining the pharmaceutical composition in a uniform matrix of soft - gel of the present invention are mixed , among which gelatine , obtaining a gelatinous mixture , the gelatinous mixture is brought to melting point , a medicated composition containing the active principle is added to it , obtaining a medicated gelatinous mixture and it is fed into a “ rotary die ” type machine for forming capsules , which then forms “ full ” capsules without injected material . these “ full ” capsules constitute the pharmaceutical compositions in uniform matrices of soft - gel of the present invention . in particular , according to the second variation of the first procedure concerning the first aspect of the present invention , to prepare a pharmaceutical composition of thyroid hormones in a uniform matrix of soft - gel , the following steps are performed : preparation of a gelatinous mixture comprising 10 - 50 % in weight of type a or b gelatine of bovine , pig or fish origin , 5 - 45 % of glycerol , 0 - 10 % in weight of ethanol and 20 - 60 % in weight of water , melting of the gelatinous mixture at a temperature between 30 ° and 80 ° c ., preferably between 40 ° and 65 ° c ., when it is completely melted , lowering of the temperature of the gelatinous mixture to 45 °± 5 ° c . and addition of a medicated mixture comprising t3 and / or t4 or their salts as required and glycerol , the quantity of the medicated mixture corresponding to 5 %- 10 % in weight of the gelatinous mixture , obtaining a medicated gelatinous mixture , feeding of the medicated gelatinous mixture into the cavities of the shaping cylinders of a “ rotary die ” type machine for forming capsules , cutting and taking the pharmaceutical composition in a uniform matrix of soft - gel thus formed from the “ rotary die ” machine , and if contemplated , further solvents , such as polyhydric or polyether alcohols , excipients , preservatives and / or colouring agents can be added to the gelatinous mixture obtained in the first step and / or to the medicated mixture added in the third step . preferably , the “ rotary die ” machines are operated in an environment having a temperature between 20 ° c . and 24 ° c . and a relative humidity between 5 % and 35 %, preferably around 20 %. preferably , the pharmaceutical composition in a uniform matrix of soft - gel obtained as above is dried at a temperature of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %. a second procedure ( which is particularly preferred ) for obtaining pharmaceutical formulae of thyroid hormones in uniform matrices of soft - gel according to the first aspect of the present invention , contemplates the dissolving / suspension of the active principle and of any excipients in a liquid vehicle to give the so - called “ medicated injected material ” which is then injected into the gelatinous mixture at the time of forming the matrix . the components of the gelatinous mixture and respectively , of the medicated injected material , are particularly calibrated to allow the uniform diffusion of the medicated injected material in the matrix , without altering its single - phase structure . consequently , also with the second procedure concerning the first aspect of the present invention , the usual soft capsules filled with a liquid , semi - liquid or pasty phase are not obtained , but rather a matrix of uniform soft - gel comprising the active principle . in particular , to prepare a pharmaceutical composition of thyroid hormones in a uniform matrix of soft - gel according to the second procedure concerning the first aspect of the present invention , the following steps are performed : preparation of a gelatinous mixture comprising 10 - 50 % in weight of type a or b gelatine of bovine , pig or fish origin , 10 - 50 % in weight of glycerol , 0 - 10 % in weight of ethanol , 20 - 80 % in weight of water , melting of the gelatinous mixture at a temperature between 30 - 80 ° c . preferably between 40 - 65 ° c ., feeding of the gelatinous mixture into the cavities of the shaping cylinders of a “ rotary die ” type machine for forming capsules ; injection , at the time of closing the cavity , by means of the special injector , of a quantity of medicated injected material corresponding to from 1 % to 50 % in weight , preferably to from 5 % to 30 % in weight , of the quantity of gelatinous mixture placed in the cavity , said medicated injected material comprising cutting and taking the pharmaceutical composition in a uniform matrix of soft - gel thus formed from the “ rotary die ” machine , and preferably , the medicated injected material comprises 50 %- 90 % in weight of glycerol , 0 %- 30 % in weight of ethanol , 0 %- 45 % in weight of water , 5 %- 20 % in weight of gelatine , and as much as necessary in weight of t3 and / or t4 . even more preferably , the medicated injected material comprises 60 %- 90 % in weight of glycerol , 5 %- 15 % in weight of water , 5 - 10 % of gelatine and as much as necessary in weight of t3 and / or t4 . even more preferably , the medicated injected material comprises 50 - 70 % in weight of glycerol , 25 %- 30 % in weight of ethanol , 5 %- 10 % of gelatine and as much as necessary in weight of t3 and / or t4 . even more preferably , the medicated injected material comprises 50 - 70 % in weight of glycerol , 25 %- 45 % in weight of water , 5 %- 10 % of gelatine and as much as necessary in weight of t3 and / or t4 . if contemplated , further solvents , such as polyhydroxy or polyether alcohols , excipients , preservatives and / or colouring agents can be added to the gelatinous mixture obtained in the first step and / or to the medicated injected material added in the third step . preferably , the “ rotary die ” machines are operated in an environment having a temperature between 20 ° c . and 24 ° c . and a relative humidity between 5 % and 35 %, preferably around 20 %. preferably , the pharmaceutical composition in a uniform matrix of soft - gel obtained as above is dried at a temperature of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %. as has already been said , in the working conditions indicated above , the medicated injected material never remains a liquid or pasty phase , distinguishable from the gelatinous phase , but is spread uniformly in the gelatinous mixture , to give a uniform matrix of soft - gel which can be taken by mouth . moreover , according to a second aspect of the present invention it was found that the pharmaceutical formula of thyroid hormones ( in particular of t3 and / or t4 or their salts , preferably their sodium salts ) in a uniform matrix of soft - gel which can be taken by mouth without chewing ( and that is in which the uniform matrix is composed of a three - dimensional body having the form and the dimensions of a normal tablet or intense capsule for taking orally ), said matrix comprising , in the dried state , 30 %- 70 % in weight of gelatine of bovine , pig or fish origin , and characterised in that they comprise , in the dried state , 20 - 60 % in weight , preferably 25 - 55 % in weight of sorbitol / sorbitans and 1 - 10 % in weight of water , offers considerable advantages in relation to normal administration in the known pharmaceutical forms which did not have an acceptable shelf - life . by the term dried state is meant , preferably , the state reached by the pharmaceutical formula after drying at a temperatures of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is reached , that is until two weighing operations carried out at a distance of 24 hours do not vary by more than 1 %. the uniform matrices of soft - gel of the present invention comprise t3 and / or t4 or their salts , preferably their sodium salts , in pharmaceutically acceptable quantities , preferably 0 . 001 - 1 % in weight . optionally , the uniform matrices of soft - gel of the present invention may be provided on the outside with enteric layers formulated according to known techniques so that they decompose substantially in the environment of the small intestine which is the principal site of absorption of thyroid hormones . besides ( or instead of ) enteric layers , the uniform matrices of soft - gel of the present invention may be optionally provided with also further layers that facilitate ingestion , that is which are composed of excipients that reduce friction between the capsule and the patient &# 39 ; s oesophagus . the materials used to obtain the uniform matrices of soft - gel of the present invention are the so - called type a or b gelatines of bovine , pig and fish origin usually used in pharmaceutical technique for making capsules . in the uniform matrices of soft - gel of the present invention , the gelatines are present , in the dried product , from 30 % to 70 % in weight . a representative , but not exclusive example of a gelatine that may be used in the present invention is a gelatine with the following amino acidic profile : glycine : 26 %, alanine : 9 %, isoleucine : 1 . 5 %, leucine : 3 . 4 %, valine : 2 . 5 %, serine : 3 . 5 %, threonine : 2 %, proline : 16 %, phenylalanine : 2 . 4 %, tyrosine : 0 . 8 %, tryptophane : 0 %, methionine : 0 . 8 %, histidine : 0 . 8 %, arginine : 9 %, lysine : 5 %, aspartic acid : 6 %, glutamic acid : 11 %, hydroxyproline : 13 . 5 % and hydroxylysine : 1 %. preferably , the gelatines that may be used in the present invention have a grain size between 4 and 100 mesh and a ph between 3 and 10 . the solvent used necessarily in obtaining the uniform matrices of soft - gel of the present invention is a mixture of sorbitol / sorbitans , which must be present , in the dried product , with 20 - 60 % in weight , preferably with 25 - 55 % in weight , even more preferably with 25 - 50 % in weight . a further solvent - used in obtaining the uniform matrices of soft - gel of the present invention is water , which remains present , in the dried product , in a quantity of 1 - 10 % in weight . a further solvent that may be used in obtaining the uniform matrices of soft - gel of the present invention is ethanol which , when used , remains present , in the dried product , in a quantity of 0 . 5 - 5 % in weight . further solvents which may be used in obtaining the uniform matrices of soft - gel of the present invention are other polyhydroxy or polyether alcohols , such as for example glycerol , 1 , 2 - propylenglycol , polyethylenglycols and mannitol or mixtures thereof . when these further solvents are used , they or their mixtures are added in quantities such as to remain present , altogether , in the dried product , in a quantity of 1 - 10 % in weight . among the further solvents as above , glycerol is particularly preferred . further components that may be optionally used for obtaining the uniform matrices of soft - gel of the present invention are excipients , for example all the usual pharmaceutically acceptable solid additives which may be used to modify the characteristics of the release of thyroid hormones from the resulting uniform matrix of soft - gel . further excipients that may be used in obtaining the uniform matrices of soft - gel of the present invention are colouring agents and / or preservatives such as parabenes , preferably methylparahydroxybenzoate , ethylparaoxybenzoate or propylparahydroxybenzoate . according to a particularly advantageous aspect of the present invention , the pharmaceutical formulations of thyroid hormones in uniform matrices of soft - gel can be obtained with two different procedures which both use the so - called “ rotary die ” machines commonly used in the pharmaceutical technique for producing soft capsules with a liquid or semi - liquid content . the specific contrivances proposed by the procedures of the present invention mean that , instead of the classic two - phase capsules , comprising a casing and a content of different consistency , “ full ” capsules are obtained , that is uniform matrices of soft - gel which are perfectly single - phase . according to a first procedure concerning the second aspect of the present invention , all the necessary components for obtaining the pharmaceutical composition in a uniform matrix of soft - gel of the present invention are mixed and the mixture is fed into a “ rotary die ” type machine for forming capsules , which then forms “ full ” capsules without injected material . these “ full ” capsules constitute the pharmaceutical compositions in uniform matrices of soft - gel of the present invention . according to a first variation of the first procedure concerning the second aspect of the present invention , all the necessary components for obtaining the pharmaceutical composition in a uniform matrix of soft - gel of the present invention are mixed , obtaining a medicated gelatinous mixture , the medicated gelatinous mixture is brought to melting point and fed into a “ rotary die ” type machine for forming capsules , which then forms “ full ” capsules without injected material . these “ full ” capsules constitute the pharmaceutical compositions in uniform matrices of soft - gel of the present invention . in particular , according to the first variation of the first procedure concerning the second aspect of the present invention , to prepare a pharmaceutical composition of thyroid hormones in a uniform matrix of soft - gel , the following steps are performed : preparation of a medicated gelatinous mixture comprising 10 - 50 % in weight of type a or b gelatine of bovine , pig or fish origin , 10 - 50 % in weight of sorbitol / sorbitans solution , 0 - 10 % in weight of ethanol , 20 - 80 % in weight of water and 0 . 001 - 1 % in weight of t3 and / or t4 or their salts , melting of the medicated gelatinous mixture at a temperature between 30 ° and 55 ° c ., preferably between 35 ° and 45 ° c ., feeding of the medicated gelatinous mixture into the cavities of the shaping cylinders of a “ rotary die ” type machine for forming capsules , cutting and taking the pharmaceutical composition in a uniform matrix of soft - gel thus formed from the “ rotary die ” machine , and drying of the pharmaceutical composition in a uniform matrix of soft - gel . solutions of sorbitol / sorbitans are available on the market , for example anidrisorb 85 which contains a mixture of sorbitol / sorbitans and 15 % of water . preferably , the “ rotary die ” machines are operated in an environment having a temperature between 20 ° c . and 24 ° c . and a relative humidity between 5 % and 35 %, preferably around 20 %. preferably , the pharmaceutical composition in a uniform matrix of soft - gel obtained as above is dried at a temperature of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %. if contemplated , further solvents , such as polyhydroxy or polyether alcohols , in particular glycerol , excipients , preservatives and / or colouring agents can be added to the medicated gelatinous mixture obtained in the first step . according to a second variation of the first procedure concerning the second aspect of the present invention , some of the necessary components for obtaining the pharmaceutical composition in a uniform matrix of soft - gel of the present invention are mixed , among which gelatine , obtaining a gelatinous mixture , the gelatinous mixture is brought to melting point , a medicated composition containing the active principle is added to it , obtaining a medicated gelatinous mixture and it is fed into a “ rotary die ” type machine for forming capsules , which then forms “ full ” capsules without injected material . these “ full ” capsules constitute the pharmaceutical compositions in uniform matrices of soft - gel of the present invention . in particular , according to the second variation of the first procedure concerning the second aspect of the present invention , to prepare a pharmaceutical composition of thyroid hormones in a uniform matrix of soft - gel , the following steps are performed : preparation of a gelatinous mixture comprising 10 - 50 % in weight of type a or b gelatine of bovine , pig or fish origin , 10 - 50 % of sorbitol / sorbitan solution , 0 - 10 % in weight of ethanol and 20 - 60 % in weight of water , melting of the gelatinous mixture at a temperature between 30 ° and 80 ° c ., preferably between 40 ° and 65 ° c ., when it is completely melted , lowering of the temperature of the gelatinous mixture to 45 ± 5 ° c . and addition of a medicated mixture comprising t3 and / or t4 or their salts as required and glycerol , the quantity of the medicated mixture corresponding to 1 %- 5 % in weight of the gelatinous mixture , obtaining a medicated gelatinous mixture , feeding of the medicated gelatinous mixture into the cavities of the shaping cylinders of a “ rotary die ” type machine for forming capsules , cutting and taking the pharmaceutical composition in a uniform matrix of soft - gel thus formed from the “ rotary die ” machine , and solutions of sorbitol / sorbitans are available on the market , for example anidrisorb 85 which contains a mixture of sorbitol / sorbitans and 15 % of water . if contemplated , further solvents , such as polyhydroxy or polyether alcohols , excipients , preservatives and / or colouring agents can be added to the gelatinous mixture obtained in the first step and / or to the medicated mixture added in the third step . preferably , the “ rotary die ” machines are operated in an environment having a temperature between 20 ° c . and 24 ° c . and a relative humidity between 5 % and 35 %, preferably around 20 %. preferably , the pharmaceutical composition in a uniform matrix of soft - gel obtained as above is dried at a temperature of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %. a second procedure ( which is particularly preferred ) for obtaining pharmaceutical formulae of thyroid hormones in uniform matrices of soft - gel according to the second aspect of the present invention , contemplates the dissolving / suspension of the active principle and of any excipients in a liquid vehicle to give the so - called “ medicated injected material ” which is then injected into the gelatinous mixture at the time of forming the matrix . the components of the gelatinous mixture and respectively , of the medicated injected material , are particularly calibrated to allow the uniform diffusion of the medicated injected material in the matrix , without altering its single - phase structure . consequently , also with the second procedure concerning the second aspect of the present invention , the usual soft capsules filled with a liquid , semi - liquid or pasty phase are not obtained , but rather a matrix of uniform soft - gel comprising the active principle . in particular , to prepare a pharmaceutical composition of thyroid hormones in a uniform matrix of soft - gel according to the second procedure concerning the second aspect of the present invention , the following steps are performed : preparation of a gelatinous mixture comprising 10 - 50 % in weight of type a or b gelatine of bovine , pig or fish origin , 10 - 50 % in weight of sorbitol / sorbitans solution , 0 - 10 % in weight of ethanol , 20 - 80 % in weight of water , melting of the gelatinous mixture at a temperature between 30 - 80 ° c . preferably between 40 - 65 ° c , feeding of the geltinous mixture into the cavities of the shaping cylinders of a “ rotary die ” type machine for forming capsules ; injection , at the time of closing the cavity , by means of the special injector , of a quantity of medicated injected material corresponding to from 1 % to 30 % in weight , preferably to from 5 % to 15 % in weight , of the quantity of gelatinous mixture placed in the cavity , said medicated injected material comprising cutting and taking the pharmaceutical composition in a uniform matrix of soft - gel thus formed from the “ rotary die ” machine , and solutions of sorbitol / sorbitans are available on the market , for example anidrisorb 85 which contains a mixture of sorbitol / sorbitans and 15 % of water . preferably , the medicated injected material comprises 50 %- 90 % in weight of glycerol , 0 %- 30 % in weight of ethanol , 5 %- 45 % in weight of water , 0 %- 20 % in weight of gelatine , and as much as necessary in weight of t3 and / or t4 . even more preferably , the medicated injected material comprises 60 %- 90 % in weight of glycerol , 5 %- 15 % in weight of water , 0 - 50 % weight of gelatine , and as much as necessary in weight of t3 and / or t4 . even more preferably , the medicated injected material comprises 50 - 70 % in weight of glycerol , 25 %- 30 % in weight of ethanol , 5 %- 10 % of gelatine and as much as necessary in weight of t3 and / or t4 . even more preferably , the medicated injected material comprises 50 - 70 % in weight of glycerol , 25 %- 45 % in weight of water , 0 %- 10 % of gelatine and as much as necessary in weight of t3 and / or t4 . if contemplated , further solvents , such as polyhydric or polyether alcohols , excipients , preservatives and / or colouring agents can be added to the gelatinous mixture obtained in the first step and / or to the medicated injected material added in the third step . preferably , the “ rotary die ” machines are operated in an environment having a temperature between 20 ° c . and 24 ° c . and a relative humidity between 5 % and 35 %, preferably around 20 %. preferably , the pharmaceutical composition in a uniform matrix of soft - gel obtained as above is dried at a temperature of 20 ° c .- 24 ° c . and a relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %. as has already been said , in the working conditions indicated above , the medicated injected material never remains a liquid or pasty phase , distinguishable from the gelatinous phase , but is spread uniformly in the gelatinous mixture , to give a uniform matrix of soft - gel which can be taken by mouth . consequently , the pharmaceutical compositions of thyroid hormones in a uniform matrix of soft - gel according to both aspects of the present invention can be easily divided by the patient — unlike the normal soft capsules with a liquid or semi - liquid content — to make an adaptation of the individual dose prescribed by the doctor . below are given some examples of formulae according to the present invention : the following formulae concern the first aspect of the present invention and were obtained according to the second procedure of the present invention : the first three columns refer to the initial situation , that is before injection : first column : percentage composition of the medicated injected material and of the gelatinous mixture . second column : total quantity of medicated injected material and of gelatinous mixture . third column : quantity of each ingredient in mg / uniform matrix of soft - gel for the newly formed matrix . fourth column : percentages of each ingredient in the newly formed matrix of soft - gel . fifth and sixth column : percentages of each ingredient in the dried matrix of soft - gel . in the dried matrices ( at a temperature between 20 ° c .- 24 ° c . and relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %) the weight is reduced on account of the almost complete elimination of water and ethanol which remain linked to the gelatine in the specified quantities . initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 85 . 70 138 . 00 118 . 266 27 . 43481 gelatine 5 . 00 138 . 00 6 . 9 1 . 600631 water 9 . 00 138 . 00 12 . 42 2 . 881136 t4 0 . 30 138 . 00 0 . 414 0 . 096038 0 . 096038 0 . 1 gelatinous mixture gelatine 42 470 . 00 197 . 4 45 . 79196 42 . 6926 42 . 7 glycerol 23 470 . 00 108 . 1 25 . 07655 52 . 51137 52 . 5 water 35 470 . 00 164 . 5 38 . 15997 4 . 7 4 . 7 weight of uniform 608 431 . 08 matrix of soft - gel [ 0134 ] 1 . 2 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 64 . 70 50 . 00 32 . 35 9 . 500734 gelatine 5 . 00 50 . 00 2 . 5 0 . 734214 water 30 . 00 50 . 00 15 4 . 405286 t4 0 . 30 50 . 00 0 . 15 0 . 044053 0 . 044053 0 . 045 gelatinous mixture gelatine 42 470 . 00 197 . 4 57 . 97357 52 . 90778 52 . 9 glycerol 23 470 . 00 108 . 1 31 . 74743 41 . 24816 41 . 25 water 35 470 . 00 164 . 5 48 . 31131 5 . 8 5 . 8 weight of uniform 520 340 . 5 matrix of soft - gel [ 0135 ] 1 . 3 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 64 . 70 50 . 00 32 . 35 9 . 500734 gelatine 5 . 00 50 . 00 2 . 5 0 . 734214 ethanol 30 . 00 50 . 00 15 4 . 405286 2 . 00 2 . 0 t4 0 . 30 50 . 00 0 . 15 0 . 044053 0 . 044053 0 . 045 gelatinous mixture gelatine 42 470 . 00 197 . 4 57 . 97357 52 . 70778 52 . 7 glycerol 23 470 . 00 108 . 1 31 . 74743 41 . 24816 41 . 25 water 35 470 . 00 164 . 5 48 . 31131 4 . 00 4 . 0 weight of uniform 520 340 . 5 matrix of soft - gel the following formulae were obtained according to the first procedure concerning the first aspect of the present invention . gelatine 56 . 58 % 56 . 60 % 60 . 55 % glycerol 37 . 07 % 37 . 09 % 32 . 68 % t4 0 . 06 % 0 . 023 % 0 . 029 % water 6 . 29 % 6 . 287 % 6 . 741 % the following formulae concern the second aspect of the present invention and were obtained according to the second procedure of the present invention : the first three columns refer to the initial situation , that is before injection : first column : percentage composition of the medicated injected material and of the gelatinous mixture . second column : total quantity of medicated injected material and of gelatinous mixture . third column : quantity of each ingredient in mg / uniform matrix of soft - gel for the newly formed matrix . fourth column : percentages of each ingredient in the newly formed matrix of soft - gel . fifth and sixth column : percentages of each ingredient in the dried matrix of soft - gel . in the dried matrices ( at a temperature between 20 ° c .- 24 ° c . and relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %) the weight is reduced on account of the almost complete elimination of water and ethanol which remain linked to the gelatine in the specified quantities . initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 50 . 00 20 . 00 10 4 . 54 4 . 54 4 . 5 gelatine 35 . 00 20 . 00 7 3 . 18 water 10 . 00 20 . 00 2 0 . 91 t4 0 . 30 20 . 00 0 . 06 0 . 03 0 . 03 0 . 027 gelatinous mixture 0 0 . 00 gelatine 42 330 . 00 138 . 6 52 . 95 56 . 80 56 . 8 sorbitol / sorbitans 85 % 23 330 . 00 75 . 9 34 . 47 29 . 30 29 . 3 water 35 330 . 00 115 . 5 52 . 46 9 . 373 weight of uniform matrix ( mg ) 349 . 06 220 . 175 100 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 48 . 00 50 . 00 24 9 . 81 9 . 81 9 . 8 gelatine 35 . 00 50 . 00 17 . 5 7 . 15 water 10 . 00 50 . 00 5 2 . 04 t4 0 . 30 50 . 00 0 . 15 0 . 06 0 . 06 0 . 061 gelatinous mixture 0 0 . 00 gelatine 42 330 . 00 138 . 6 56 . 63 57 . 40 57 . 2 sorbitol / sorbitans 85 % 23 330 . 00 75 . 9 31 . 01 26 . 36 26 . 2 water 35 330 . 00 115 . 5 47 . 19 5 . 739 weight of uniform matrix ( mg ) 376 . 65 244 . 765 100 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 50 . 00 20 . 00 10 5 . 85 5 . 85 5 . 9 gelatine 35 . 00 20 . 00 7 4 . 10 water 10 . 00 20 . 00 2 1 . 17 t4 0 . 30 20 . 00 0 . 06 0 . 04 0 . 04 0 . 04 gelatinous mixture 0 0 . 00 gelatine 42 250 . 00 105 61 . 43 58 . 97 59 sorbitol / sorbitans 85 % 23 250 . 00 57 . 5 33 . 64 28 . 59 28 . 6 water 35 250 . 00 87 . 5 51 . 19 6 . 46 weight of uniform matrix ( mg ) 269 . 06 170 . 935 100 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 29 . 75 60 . 00 17 . 85 9 . 25 9 . 25 9 . 25 gelatine 35 . 00 60 . 00 21 10 . 89 water 35 . 25 60 . 00 21 . 15 10 . 96 t4 0 . 30 60 . 00 0 . 18 0 . 09 0 . 09 0 . 09 gelatinous mixture 0 0 . 00 gelatine 42 250 . 00 105 54 . 43 58 . 79 58 . 8 sorbitol / sorbitans 85 % 23 250 . 00 57 . 5 29 . 81 25 . 34 25 . 3 water 35 250 . 00 87 . 5 45 . 36 6 . 56 weight of uniform matrix ( mg ) 310 . 18 192 . 905 100 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 27 . 75 150 . 00 41 . 625 9 . 80 9 . 80 9 . 8 gelatine 50 . 00 150 . 00 75 17 . 65 water 27 . 25 150 . 00 40 . 875 9 . 62 t4 0 . 30 150 . 00 0 . 45 0 . 11 0 . 11 0 . 11 gelatinous mixture 0 0 . 00 gelatine 42 500 . 00 210 49 . 43 60 . 38 60 . 4 sorbitol / sorbitans 85 % 23 500 . 00 115 27 . 07 23 . 01 23 water 35 500 . 00 175 41 . 19 6 . 69 weight of uniform matrix ( mg ) 657 . 95 424 . 825 100 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 85 . 00 20 . 00 17 7 . 72 7 . 72 7 . 7 gelatine 0 . 00 20 . 00 0 0 . 00 water 15 . 00 20 . 00 3 1 . 36 t4 0 . 30 20 . 00 0 . 06 0 . 03 0 . 03 0 . 03 gelatinous mixture 0 0 . 00 gelatine 42 330 . 00 138 . 6 62 . 95 56 . 65 56 . 7 sorbitol / sorbitans 85 % 23 330 . 00 75 . 9 34 . 47 29 . 30 29 . 3 water 35 330 . 00 115 . 5 52 . 46 6 . 27 weight of uniform matrix ( mg ) 350 . 06 220 . 175 100 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerine 85 . 00 20 . 00 17 8 . 00 8 . 00 8 gelatine 0 . 00 20 . 00 0 0 . 00 water 15 . 00 20 . 00 3 1 . 41 t4 0 . 30 20 . 00 0 . 06 0 . 03 0 . 03 0 . 03 gelatinous mixture 0 0 . 00 gelatine 38 330 . 00 125 . 4 58 . 99 53 . 09 53 . 1 sorbitol / sorbitans 85 % 25 330 . 00 82 . 5 38 . 81 32 . 99 33 water 37 330 . 00 122 . 1 57 . 44 5 . 87 weight of uniform matrix ( mg ) 350 . 06 212 . 585 100 initial final % mg / matrix mg / matrix final composition % medicated injected material glycerol 57 . 00 20 . 00 11 . 4 9 . 90 9 . 90 gelatine 0 . 00 20 . 00 0 0 . 00 water 43 . 00 20 . 00 8 . 6 7 . 47 t4 0 . 30 20 . 00 0 . 06 0 . 05 0 . 05 gelatinous mixture 0 0 . 00 gelatine 38 175 . 00 66 . 5 57 . 75 51 . 98 sorbitol / sorbitans 85 % 25 175 . 00 43 . 75 37 . 99 32 . 30 water 37 175 . 00 64 . 75 56 . 23 weight of uniform matrix ( mg ) 195 . 06 115 . 1475 the following formulae were obtained according to the first procedure concerning the second aspect of the present invention . the initial composition refers to before drying , while the final composition refers to after drying according to the conditions defined above ( at a temperature between 20 ° c .- 24 ° c . and relative humidity of 20 % with a continuous change of the surrounding air until a constant weight is obtained , that is until two weighing operations carried out at an interval of 24 h do not differ by more than 1 %). initial final % mg / matrix mg / matrix final composition % medicated gelatinous material 0 gelatine 42 330 . 00 138 . 6 59 . 47 59 . 5 sorbitol / sorbitans 85 % 23 330 . 00 75 . 9 30 . 76 30 . 8 glycerine 2 330 . 00 6 . 6 3 . 15 3 . 1 t4 0 . 0075 330 . 00 0 . 02475 0 . 012 water 33 330 . 00 108 . 9 6 . 6 weight of uniform matrix ( mg ) 330 . 0 209 . 7 100 initial final % mg / matrix mg / matrix final composition % medicated gelatinous material 0 gelatine 38 330 . 00 125 . 4 56 . 48 56 . 5 sorbitol / sorbitans 85 % 23 330 . 00 75 . 9 32 . 28 32 . 3 glycerine 3 330 . 00 9 . 9 4 . 95 5 t4 0 . 0075 330 . 00 0 . 02475 0 . 013 water 36 330 . 00 118 . 8 6 . 187 weight of uniform matrix ( mg ) 330 . 0 199 . 8 100 initial final % mg / matrix mg / matrix final composition % medicated gelatinou material 0 gelatine 38 330 . 00 125 . 4 58 . 37 58 . 4 sorbitol / sorbitans 85 % 23 330 . 00 75 . 9 33 . 36 33 . 4 glycerine 1 330 . 00 3 . 3 1 . 71 1 . 7 t4 0 . 046 330 . 00 0 . 1518 0 . 013 water 38 330 . 00 125 . 4n 6 . 487 weight of uniform matrix ( mg ) 330 . 2 193 . 4 100 initial final % mg / matrix mg / matrix final composition % medicated gelatinou material 0 gelatine 38 330 . 00 125 . 4 62 . 24 62 . 2 sorbitol / sorbitans 85 % 14 330 . 00 46 . 2 21 . 66 21 . 7 glycerine 5 330 . 00 16 . 5 9 . 10 9 . 1 t4 0 . 046 330 . 00 0 . 1518 0 . 08 water 43 330 . 00 141 . 9 6 . 92 weight of uniform matrix ( mg ) 330 . 2 181 . 3 100 initial final % mg / matrix mg / matrix final composition % medicated gelatinou material 0 gelatine 30 330 . 00 99 47 . 78 47 . 8 sorbitol / sorbitans 85 % 30 330 . 00 99 45 . 12 45 . 1 glycerine 1 330 . 00 3 . 3 1 . 77 1 . 8 t4 0 . 01 330 . 00 0 . 033 0 . 02 water 39 330 . 00 128 . 7 5 . 28 weight of uniform matrix ( mg ) 330 . 0 186 . 5 100 initial final % mg / matrix mg / matrix final composition % medicated gelatinou material 0 gelatine 24 330 . 00 79 . 2 35 . 21 35 . 1 sorbitol / sorbitans 85 % 38 330 . 00 125 . 4 52 . 65 52 . 7 glycerine 5 330 . 00 16 . 5 8 . 15 8 . 1 t4 0 . 046 330 . 00 0 . 1518 0 . 07 water 33 330 . 00 108 . 9 4 . 03 weight of uniform matrix ( mg ) 330 . 2 202 . 4 100 obtaining formulae for thyroid hormones in uniform matrices of soft - gel according to both aspects of the present invention , in particular according to the first variation of the first procedure : introduction , in a stainless steel reactor , equipped with a heating system , mixer and equipment for operating in a vacuum and under pressure , of a medicated gelatinous mixture as defined above ; the mass thus obtained is brought to melting point around 50 ° c ., stirring all the time and working in a vacuum . when it is completely melted the mixture is transferred to suitable thermostat - controlled stainless steel containers , where it is kept at about 45 ° c . from there , the mixture is fed into a “ rotary die ” type machine for forming capsules , for example a “ mksj encapsulating machine ( sen jin sdn . bhd )”. in particular , the hot gelatinous mixture feeds two dosing devices on the machine , which form two gelatinous films of a determined and constant thickness on two air - cooled rollers . the two films pass through two capsule - shaping cylinders which turn concentrically , on top of which is a particular heated wedge , called injector segment , which is not used in this procedure . passing through the cylinders , the capsule - shaping cavities form uniform matrices of soft - gel from the two gelatinous films . the cut uniform matrices of soft - gel fall below the shaping cylinders in rotating baskets from which , after staying there several hours , they are turned out onto trays for drying . if starting from a non medicated gelatinous mixture , that is in the second variation of the first procedure , the procedure is similar , but the melting temperature is higher , around 65 ° c . when it is completely melted the mixture is transferred to suitable thermostat - controlled stainless steel containers , where it is kept at about 45 ° c . for the desired time . then the medicated mixture is added , homogenised , and from there , preferably within one hour , the mixture is fed into a “ rotary die ” type machine for forming capsules , which completes the shaping of uniform matrices of soft - gel as described above with relation to the first variation of the first procedure . obtaining formulae for thyroid hormones in uniform matrices of soft - gel according to both aspects of the present invention , in particular according to the second procedure : the procedure corresponds to the second variation of the first procedure , without adding the medicated substance to the mixture before feeding it to the machine . the hot gelatinous mixture feeds two dosing devices on the machine , which form two gelatinous films of a determined and constant thickness on two air - cooled rollers . the two films pass through two capsule - shaping cylinders which turn concentrically , on top of which is a particular heated wedge , called the injector segment . the medicated injected substances is fed directly to a dosing pump that has precision syringes which , sliding alternately , feed the injector segment through small pipes , injecting a quantity of medicated injected substance into the gelatinous mixture contained in the cavities of the two shaping cylinders . the medicated injected substance spreads through the gelatinous mixture , thus forming the uniform matrices of soft - gel which are cut and fall below the shaping cylinders in rotating baskets from which , after staying there several hours , they are turned out onto trays for drying . the following compositions were obtained according to the first procedure concerning the first aspect of the invention ( preparation without injection of a medicated solution ; matrix with high glycerol content , sorbitol / sorbitans - free ). the table displays the final composition in the dried state , as herein defined . composition % batch ingredient 100 104 116 127 130 133 134 gelatin 61 . 1 56 . 59 59 59 . 25 58 . 89 59 . 25 58 . 89 glycerol 32 . 3 37 . 069 35 34 . 95 34 . 73 34 . 95 34 . 73 water 6 . 5 6 . 309 6 5 . 75 5 . 72 5 . 75 5 . 72 titanium dioxide 0 . 60 0 . 60 t4 0 . 029 0 . 023 0 . 046 0 . 046 0 . 046 0 . 023 0 . 023 respective stability studies were conducted according to ich guide lines in two different packaging conditions stability studies were carried out in glass bottles with a stopper including silica gel , in order to guarantee the highest moisture barrier . stability data : 25 ° c ./ 60 % rh and 30 ° c ./ 60 % rh (% of drug substance ) 25 ° c .- 60 % rh 30 ° c .- 60 % rh time batch ( days ) 100 104 116 127 130 133 134 100 104 116 127 130 133 134 initial 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 30 94 . 60 98 . 63 94 . 86 — — 94 . 16 99 . 17 93 . 50 98 . 44 97 . 38 103 . 44 96 . 87 91 . 43 96 . 17 60 97 . 50 96 . 43 94 . 11 — — — — 96 . 60 92 . 77 94 . 29 92 . 21 100 . 62 90 93 . 80 95 . 70 97 . 10 104 . 50 94 . 13 99 . 81 99 . 69 92 . 60 92 . 50 94 . 95 95 . 95 101 . 96 97 . 86 99 . 59 180 96 . 60 97 . 53 98 . 32 99 . 19 99 . 71 94 . 06 91 . 75 95 . 20 95 . 79 94 . 76 97 . 16 95 . 89 89 . 48 97 . 62 270 96 . 30 100 . 00 96 . 28 360 94 . 30 for the blisters packaging , 2 different types of plastic materials have been tested : bilayer pvc - pvdc and pentapharm aclar ®. the stability controls carried out on development batches yield good results with no significant differences between both kind of plastic materials : coupled pvc - pvdc and aclar stability data : 25 ° c .- 60 % rh (% of drug substance ) pvdc aclar time batch ( days ) 100 116 127 133 134 104 116 127 133 134 initial 100 . 00 100 . 00 98 . 7 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 30 96 . 50 97 . 44 — 95 . 42 97 . 41 99 . 63 97 . 42 95 . 33 97 . 62 60 97 . 00 97 . 35 — 95 . 33 99 . 62 90 98 . 50 97 . 25 103 99 . 32 99 . 48 93 . 41 99 . 71 98 . 58 98 . 73 98 . 96 180 94 . 80 91 . 75 92 . 02 96 . 89 94 . 78 98 . 57 98 . 48 92 . 41 95 . 96 270 97 . 44 97 . 71 97 . 90 360 92 . 20 [ 0161 ] stability data : 30 ° c .- 60 % rh (% of drug substance ) pvdc aclar time batch ( days ) 116 127 130 133 134 116 127 130 133 134 initial 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 100 . 00 98 . 7 102 . 3 102 . 7 96 . 6 30 96 . 87 102 . 94 100 . 3 93 . 57 97 . 1 96 . 76 102 . 23 97 . 94 92 . 31 97 . 62 60 96 . 02 — — — — 97 . 52 — — — 90 97 . 91 101 . 82 100 . 1 97 . 17 97 . 22 98 . 09 96 . 05 96 . 28 96 . 11 97 . 1 180 95 . 92 98 . 09 98 . 28 96 . 28 90 . 79 270 360 the following compositions were obtained according to the second procedure concerning the first aspect of the invention ( manufacture through injection of medicated solution which spreads uniformly across the matrix without affecting the single - phase structure thereof ; matrix with high glycerol content ; sorbitol / sorbitans - free ). the table displays the final composition in the dried state , as herein defined . batches 141 / ib - 79 , 142 / ib - 79 and 143 / ib - 79 composition for levothyroxine soft gelatin matrices 12 . 5 μg percent unitary formula amount name of the components ( w / w ) mg / sgm active ingredient sodium levothyroxine 0 . 0061 0 . 0125 excipients hydrolyzed gelatin 8 . 5366 17 . 5 gelatin 80 bloom 1 . 2195 2 . 5 glycerol 85 % 8 . 5366 17 . 5 anhydrous glycerol 28 . 0488 57 . 5 gelatin 150 bloom 47 . 5610 97 . 5 purified water 6 . 0915 12 . 488 total 100 . 0000 205 . 0000 [ 0163 ] batch 144 / ib - 79 composition for levothyroxine soft gelatin matrices 25 μg percent unitary formula amount name of the components ( w / w ) mg / sgm active ingredient sodium levothyroxine 0 . 0122 0 . 025 excipients hydrolyzed gelatin 8 . 5366 17 . 5 gelatin 80 bloom 1 . 2195 2 . 5 glycerol 85 % 8 . 5366 17 . 5 anhydrous glycerol 28 . 0488 57 . 5 gelatin 150 bloom 47 . 5610 97 . 5 purified water 6 . 0854 12 . 475 total 100 . 0000 205 . 0000 [ 0164 ] batch 145 / ib - 79 composition for levothyroxine soft gelatin matrices 50 μg percent unitary formula amount name of the components ( w / w ) mg / sgm active ingredient sodium levothyroxine 0 . 0244 0 . 05 excipients hydrolyzed gelatin 8 . 5366 17 . 5 gelatin 80 bloom 1 . 2195 2 . 5 glycerol 85 % 8 . 5366 17 . 5 anhydrous glycerol 28 . 0488 57 . 5 gelatin 150 bloom 47 . 5610 97 . 5 purified water 6 . 0732 12 . 450 total 100 . 0000 205 . 0000 [ 0165 ] batches 146 / ib - 79 , 147 / ib - 79 , 148 / ib - 79 composition for levothyroxine soft gelatin matrices 75 μg percent unitary formula amount name of the components ( w / w ) mg / sgm active ingredient sodium levothyroxine 0 . 0366 0 . 075 excipients hydrolyzed gelatin 8 . 5366 17 . 5 gelatin 80 bloom 1 . 2195 2 . 5 glycerol 85 % 8 . 5366 17 . 5 anhydrous glycerol 28 . 0488 57 . 5 gelatin 150 bloom 47 . 5610 97 . 5 purified water 6 . 0610 12 . 425 total 100 . 0000 205 . 0000 [ 0166 ] batch 136 / ib - 79 composition for levothyroxine soft gelatin matrices 100 μg percent unitary formula amount name of the components ( w / w ) mg / sgm active ingredient sodium levothyroxine 0 . 0488 0 . 1 excipients hydrolyzed gelatin 8 . 5366 17 . 5 gelatin 80 bloom 1 . 2195 2 . 5 glycerol 85 % 8 . 5366 17 . 5 anhydrous glycerol 28 . 0488 57 . 5 gelatin 150 bloom 47 . 5610 97 . 5 purified water 6 . 0488 12 . 400 total 100 . 0000 205 . 0000 [ 0167 ] batch 149 / ib - 79 composition for levothyroxine soft gelatin matrices 125 μg percent unitary formula amount name of the components ( w / w ) mg / sgm active ingredient sodium levothyroxine 0 . 0610 0 . 125 excipients hydrolyzed gelatin 8 . 5366 17 . 5 gelatin 80 bloom 1 . 2195 2 . 5 glycerol 85 % 8 . 5366 17 . 5 anhydrous glycerol 28 . 0488 57 . 5 gelatin 150 bloom 47 . 5610 97 . 5 purified water 6 . 0366 12 . 375 total 100 . 0000 205 . 0000 [ 0168 ] batches 150 / ib - 79 , 151 / ib - 79 , 152 / ib - 79 composition for levothyroxine soft gelatin matrices 150 μg percent unitary formula amount name of the components ( w / w ) mg / sgm active ingredient sodium levothyroxine 0 . 0732 0 . 15 excipients hydrolyzed gelatin 8 . 5366 17 . 5 gelatin 80 bloom 1 . 2195 2 . 5 glycerol 85 % 8 . 5366 17 . 5 anhydrous glycerol 28 . 0488 57 . 5 gelatin 150 bloom 47 . 5610 97 . 5 purified water 6 . 0244 12 . 350 total 100 . 0000 205 . 0000 with the formulations according to example 8 , stability testing was conducted as specified herein below : t4 soft - gel matrices - batch n o 141 / ib - 79 , dosage : 12 . 5 μg ; manufactured february 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 4 % * 0 . 4 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 96 . 7 % 96 . 2 % * 96 . 4 % * 95 . 6 % * 95 . 8 % * theoretical value average weight 205 . 0 mg ± 10 % 198 . 1 mg 197 . 7 mg 200 . 2 mg 196 . 6 mg 195 . 9 mg dissolution ≧ 70 % in 45 minutes complies not not not test performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 65 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0170 ] t4 soft gel matrices - batch n o 141 / ib - 79 , dosage : 12 . 5 μg ; manufactured february 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 3 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 96 . 7 % 96 . 0 % * 96 . 2 % * 95 . 6 % * 95 . 8 % * theoretical value average weight 205 . 0 mg ± 10 % 198 . 1 mg 198 . 8 mg 199 . 8 mg 198 . 8 mg 199 . 4 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 65 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0171 ] t4 soft gel matrices - batch n o 142 / ib - 79 , dosage : 12 . 5 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 5 % * 0 . 6 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 95 . 4 % 94 . 9 % * 95 . 3 % * 94 . 8 % * 95 . 0 % * theoretical value average weight 205 . 0 mg ± 10 % 196 . 3 mg 201 . 3 mg 199 . 6 mg 195 . 6 mg 196 . 8 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 40 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0172 ] t4 soft gel matrices - batch n o 142 / ib - 79 , dosage : 12 . 5 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 4 % * 0 . 4 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 95 . 4 % 94 . 8 % * 95 . 4 % * 93 . 5 * 95 . 1 * theoretical value average weight 205 . 0 mg ± 10 % 196 . 3 mg 200 . 0 mg 200 . 7 mg 197 . 8 mg 197 . 5 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 40 cfu / g performed performed performed cfu / g & lt ; 5 cfu / g moulds and absent / g yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0173 ] t4 soft gel matrices - batch n o 143 / ib - 79 , dosage : 12 . 5 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 4 % 0 . 5 % * 0 . 5 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 94 . 4 % 94 . 1 % * 94 . 3 % * 93 . 5 % * 94 . 2 % * theoretical value average weight 205 . 0 mg ± 10 % 197 . 6 mg 200 . 8 mg 200 . 9 mg 197 . 8 mg 199 . 3 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 35 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0174 ] t4 soft gel matrices - batch n o 143 / ib - 79 , dosage : 12 . 5 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 4 % 0 . 4 % * 0 . 4 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 94 . 4 % 94 . 0 % * 94 . 3 % * 93 . 5 % * 94 . 0 % * theoretical value average weight 205 . 0 mg ± 10 % 197 . 6 mg 202 . 7 mg 201 . 4 mg 198 . 1 mg 198 . 8 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 35 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0175 ] t4 soft gel matrices - batch n o 144 / ib - 79 , dosage : 25 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c .± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 8 % 0 : 3 % * 0 . 4 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 91 . 8 % 90 . 8 % * 91 . 0 % * 89 . 5 % * 90 . 5 % * theoretical value average weight 205 . 0 mg ± 10 % 203 . 0 mg 206 . 7 mg 207 . 2 mg 202 . 4 mg 200 . 0 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 60 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0176 ] t4 soft gel matrices - batch n o 144 / ib - 79 , dosage : 25 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies . complies matrices , amber - coloured degradation ≦ 4 % 0 . 8 % 0 . 4 % * 0 . 4 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 91 . 8 % 91 . 3 % * 91 . 6 % * 91 . 0 % * 91 . 4 % * theoretical value average weight 205 . 0 mg ± 10 % 203 . 0 mg 205 . 4 mg 206 . 5 mg 204 . 1 mg 204 . 5 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 60 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0177 ] t4 soft gel matrices - batch n o 145 / ib - 79 , dosage : 50 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 3 % 0 . 3 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 97 . 6 % 97 . 0 % * 97 . 0 % * 97 . 0 % * 97 . 5 % * theoretical value average weight 205 . 0 mg ± 10 % 208 . 4 mg 205 . 7 mg 206 . 0 mg 203 . 9 mg 203 . 4 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 35 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0178 ] t4 soft gel matrices - batch n o 145 / ib - 79 , dosage : 50 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 3 % 0 . 4 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 1 . 4 %) ( lod = 1 . 4 %) content ) average assay 90 - 110 % of the 97 . 6 % 96 . 7 % * 97 . 4 % * 95 . 0 % * 97 . 0 % * theoretical value average weight 205 . 0 mg 208 . 4 mg 205 . 3 mg 205 . 7 mg 204 . 6 mg 202 . 3 mg ± 10 % dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 35 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0179 ] t4 soft gel matrices - batch n o 146 / ib - 79 , dosage : 75 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 3 % 0 . 4 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 9 %) ( lod = 0 . 9 %) content ) average assay 90 - 110 % of the 94 . 0 % 92 . 3 % * 93 . 9 % * 92 . 8 % * 92 . 4 % * theoretical value average weight 205 . 0 mg ± 10 % 199 . 4 mg 200 . 1 mg 201 . 3 mg 198 . 6 mg 198 . 4 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 25 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0180 ] t4 soft gel matrices - batch n o 146 / ib - 79 , dosage : 75 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 3 % 0 . 4 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 9 %) ( lod = 0 . 9 %) content ) average assay 90 - 110 % of the 94 . 0 % 93 . 4 % * 93 . 9 % * 92 . 6 % * 93 . 5 % * theoretical value average weight 205 . 0 mg ± 10 % 199 . 4 mg 200 . 0 mg 200 . 5 mg 198 . 7 mg 200 . 2 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 25 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0181 ] t4 soft gel matrices - batch n o 147 / ib - 79 , dosage : 75 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 4 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 9 %) ( lod = 0 . 9 %) content ) average assay 90 - 110 % of the 94 . 9 % 90 . 6 % * 94 . 6 % * 93 . 5 % * 91 . 4 % * theoretical value average weight 205 . 0 mg ± 10 % 201 . 5 mg 201 . 0 mg 201 . 6 mg 198 . 4 mg 199 . 9 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 10 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0182 ] t4 soft gel matrices - batch n o 147 / ib - 79 , dosage : 75 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 3 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 9 %) ( lod = 0 . 9 %) content ) average assay 90 - 110 % of the 94 . 9 % 92 . 0 % * 94 . 1 % * 92 . 1 % * 93 . 3 % * theoretical value average weight 205 . 0 mg ± 10 % 201 . 5 mg 199 . 6 mg 201 . 6 mg 198 . 7 mg 201 . 3 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 10 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0183 ] t4 soft gel matrices - batch n o 148 / ib - 79 , dosage : 75 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 3 % 0 . 4 % * 0 . 4 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 9 %) ( lod = 0 . 9 %) content ) average assay 90 - 110 % of the 96 . 5 % 92 . 5 % * 96 . 5 % * 92 . 1 % * 92 . 8 % * theoretical value average weight 205 . 0 mg ± 10 % 201 . 0 mg 200 . 5 mg 200 . 8 mg 198 . 8 mg 199 . 4mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 10 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0184 ] t4 soft gel matrices - batch n o 148 / ib - 79 , dosage : 75 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 3 % 0 . 4 % * 0 . 4 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 9 %) ( lod = 0 . 9 %) content ) average assay 90 - 110 % of the 96 . 5 % 91 . 7 % * 95 . 2 % * 91 . 4 % * 92 . 7 % * theoretical value average weight 205 . 0 mg ± 10 % 201 . 0 mg 200 . 8 mg 200 . 5 mg 198 . 9 mg 199 . 3 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 10 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0185 ] t4 soft gel matrices - batch n o 136 / ib - 79 , dosage : 100 μg ; manufactured february 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 3 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 7 %) ( lod = 0 . 7 %) content ) average assay 90 - 110 % of the 97 . 6 % 96 . 1 % * 96 . 5 % * 94 . 0 % * 94 . 6 % * theoretical value average weight 205 . 0 mg ± 10 % 205 . 3 mg 204 . 5 mg 203 . 5 mg 202 . 4 mg 201 . 9 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 & lt ; 5 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0186 ] t4 soft gel matrices - batch n o 136 / ib - 79 , dosage : 100 μg ; manufactured february 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 4 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 7 %) ( lod = 0 . 7 %) content ) average assay 90 - 110 % of the 97 . 6 % 94 . 9 % * 97 . 0 % * 93 . 1 % * 97 . 0 % * theoretical value average weight 205 . 0 mg ± 10 % 205 . 3 mg 203 . 0 mg 203 . 2 mg 203 . 9 mg 206 . 9 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 & lt ; 5 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0187 ] t4 soft gel matrices - batch n o 149 / ib - 79 , dosage : 125 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 1 % 0 . 3 % * 0 . 2 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 6 %) ( lod = 0 . 6 %) content ) average assay 90 - 110 % of the 97 . 3 % 99 . 6 % * 99 . 5 % * 97 . 6 % * 97 . 8 % * theoretical value average weight 205 . 0 mg ± 10 % 198 . 7 mg 200 . 4 mg 199 . 5 mg 198 . 6 mg 197 . 9 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 5 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0188 ] t4 soft gel matrices - batch n o 149 / ib - 79 , dosage : 125 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 1 % 0 . 3 % * 0 . 3 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 6 %) ( lod = 0 . 6 %) content ) average assay 90 - 110 % of the 97 . 3 % 99 . 5 % * 99 . 7 % * 97 . 1 % * 98 . 5 % * theoretical value average weight 205 . 0 mg ± 10 % 198 . 7 mg 200 . 1 mg 199 . 3 mg 200 . 4 mg 198 . 9 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 5 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0189 ] t4 soft gel matrices - batch n o 150 / ib - 79 , dosage : 150 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 1 % 0 . 2 % * 0 . 2 % * & lt ; lod & lt ; lod product ( t 3 ( lod = 0 . 5 %) ( lod = 0 . 5 %) content ) average assay 90 - 110 % of the 99 . 2 % 94 . 4 % * 96 . 1 % * 95 . 7 % * 96 . 6 % * theoretical value average weight 205 . 0 mg ± 10 % 200 . 8 mg 201 . 1 mg 201 . 4 mg 199 . 8 mg 198 . 5 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 25 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : & lt ; 100 cfu / g escherichia coli : absent / g [ 0190 ] t4 soft gel matrices - batch n o 150 / ib - 79 , dosage : 150 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 1 % 0 . 3 % * 0 . 2 % * & lt ; lod ( lod = 0 . 5 %) & lt ; lod ( lod = 0 . 5 %) product ( t 3 content ) average assay 90 - 110 % of the 99 . 2 % 94 . 5 % * 97 . 5 % * 94 . 1 % * 96 . 2 % * theoretical value average weight 205 . 0 mg ± 10 % 200 . 8 mg 199 . 6 mg 201 . 2 mg 200 . 1 mg 198 . 9 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 25 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0191 ] t4 soft gel matrices - batch n o 151 / ib - 79 , dosage : 150 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 1 % 0 . 2 % * 0 . 2 % * & lt ; lod ( lod = 0 . 5 %) & lt ; lod ( lod = 0 . 5 %) product ( t 3 content ) average assay 90 - 110 % of the 97 . 2 % 94 . 3 % * 97 . 7 % * 95 . 5 % * 96 . 9 % * theoretical value average weight 205 . 0 mg ± 10 % 200 . 4 mg 201 . 7 mg 201 . 7 mg 198 . 1 mg 198 . 7 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 30 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0192 ] t4 soft gel matrices - batch n o 151 / ib - 79 , dosage ; 150 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 1 % 0 . 2 % * 0 . 2 % * & lt ; lod ( lod = 0 . 5 %) & lt ; lod ( lod = 0 . 5 %) product ( t 3 content ) average assay 90 - 110 % of the 97 . 2 % 95 . 0 % * 97 . 9 % * 92 . 9 % * 95 . 2 % * theoretical value average weight 205 . 0 mg ± 10 % 200 . 4 mg 200 . 3 mg 202 . 4 mg 200 . 2 mg 200 . 9 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 30 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0193 ] t4 soft gel matrices - batch n o 152 / ib - 79 , dosage : 150 μg ; manufactured march 2003 - start stability march 2003 - contained in glass flacon 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 2 % * 0 . 2 % * & lt ; lod ( lod = 0 . 5 %) & lt ; lod ( lod = 0 . 5 %) product ( t 3 content ) average assay 90 - 110 % of the 96 . 3 % 96 . 2 % * 96 . 5 % * 95 . 9 % * 96 . 7 % * theoretical value average weight 205 . 0 mg ± 10 % 200 . 0 mg 201 . 7 mg 202 . 7 mg 198 . 5 mg 197 . 3 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 10 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g [ 0194 ] t4 soft gel matrices - batch n o 152 / ib - 79 , dosage : 150 μg ; manufactured march 2003 - start stability march 2003 - contained in blister acclar 3 months 6 months stability 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ 30 ° c . ± 2 ° c ./ 25 ° c . ± 2 ° c ./ test specifications t0 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . 60 % ± 5 % r . h . characters round biconvex complies complies complies complies complies matrices , amber - coloured degradation ≦ 4 % 0 . 2 % 0 . 2 % * 0 . 2 % * & lt ; lod ( lod = 0 . 5 %) & lt ; lod ( lod = 0 . 5 %) product ( t 3 content ) average assay 90 - 110 % of the 96 . 3 % 96 . 0 % * 97 . 0 % * 95 . 8 % * 96 . 3 % * theoretical value average weight 205 . 0 mg ± 10 % 200 . 0 mg 202 . 5 mg 202 . 5 mg 198 . 6 mg 199 . 2 mg dissolution test ≧ 70 % in 45 minutes complies not not not performed performed performed microbial aerobic complies : not not not controls : bacteria : ≦ 1000 10 cfu / g & lt ; 5 cfu / g performed performed performed cfu / g absent / g moulds and yeasts : ≦ 100 cfu / g escherichia coli : absent / g
the present invention provides pharmaceutical formulation for thyroid hormones which allow safe and stable administration by mouth within the ambit of the narrow therapeutic index prescribed in the case of thyroid dysfunctions , as well as procedures for obtaining