generally , the controlled release soft capsules according to the invention comprise a shell and a matrix fill . the matrix fill can be a suspension - type matrix or an emulsion - type matrix . in an embodiment of the invention having a suspension - type matrix fill , the active ingredient or drug is incorporated in the matrix fill as solid particles in lipid or lipophilic materials such as vegetable oils , hydrogenated vegetable oils , silicon oils , fatty acids , waxes , or fatty acid esters , or a combination thereof . the matrix composition may further contain a release regulator to modify the release profile to suit an optimum therapeutic requirement . the release regulator can be a surface - active agent that enhances water penetration into the lipid or lipophilic matrix to increase drug release . examples of release regulators are fatty acid slats , fatty acid esters , or fatty acid polyoxyethylene derivatives . surfactants having hlb values between about 3 and about 40 can be selected as release regulators . in another embodiment of the invention having a suspension - type matrix fill , the matrix , at room or body temperature , can be in a fluid or structured solid state ( solid , semi - solid , or gel ). the drug can be partially soluble in the matrix while the rest of the drug is in a solid form . the presence of drug in two physical forms , solid particles and solution , can be useful by providing dual release patterns where one drug state is released faster than the other form . in addition to suspension - type matrix fills , the invention also includes emulsion - type fills . such fills are described herein as “ emulsion - type ” fills because they comprise an emulsion . the matrix fills for these embodiments can be characterized generally as emulsion - type fills , even though the active ingredient or drug can be present as a suspension in one or more phases of the emulsions of embodiments as described herein . in another embodiment of the invention , the soft gel matrix fill comprises two phases in the form of an emulsion ( emulsion - type matrix ). the emulsion can be a water - in - oil type emulsion . the internal phase comprises aqueous or hydrophilic materials , such as polyethylene glycol of molecular weight ranging from about 200 to about 8000 . the internal phase can also be an aqueous or hydro - alcoholic solution comprising cellulose derivatives , polyacrylates , or polyvinyl polymers . examples of such polymers include methylcellulose , hydroxypropylmethyl cellulose , polymethylmethacrylate , and polyvinylpyrrolidone ( pvp ). the internal phase state can be “ fluid ” or “ structured .” a “ fluid ” internal phase , as used herein , means a completely flowable liquid whose globules can aggregate to make a larger globule . a “ structured ” internal phase , as used herein , means a solid , semisolid or a gel whose shape is relatively stable and does not usually aggregate to form a large globule . a structured internal phase therefore provides more controlled drug release and stabilizes the physical state of the matrix . the external phase of the matrix fill emulsion comprises lipid or lipophilic materials similar to those described above . the active ingredient or drug can be dispersed in the internal phase as a solution and / or as a suspension . the emulsion matrix can contain a surfactant or combination of surfactants having hlb values ranging from about 2 to about 20 . the hlb range can also be from about 5 to about 15 . in another embodiment , the matrix fill is of an emulsion type , where the drug is distributed in both external and internal phases . one portion of the active ingredient or drug in form of solid particles can be incorporated in the internal phase , while another portion is dispersed in the external phase as solid particles . this invention also provides methods for making controlled release products in a soft capsule form . the methods are applicable for production of controlled release preparations of low dose ( potent ) drugs that are highly water - soluble . the methods are also suitable for preparing controlled release products of relatively less potent , moderately water - soluble drugs . the suspension - type matrix fill compositions can be used for drugs that are moderately water - soluble at a dosage of between about 25 mg to about 500 mg . such drugs include non - steroid anti - inflammatory drugs and anti - asthmatics , e . g ., diclofenac , naproxene , ibuprofen , ketoprofen , celecoxib , and theophylline . on the other hand , the emulsion - type matrix fill can be used for highly water - soluble molecules such as anti - asthmatics , narcotic analgesics , and analgesic antagonists as well as cardiovascular drugs , e . g ., diltiazem , nifidipine , oxycodone , morphine , morphine analogues , and morphine antagonists . the suspension - type matrix fill can be manufactured by mixing the active ingredient or drug with the lipid or lipophilic matrix ingredients using mechanical or ultrasonic forces . applying heat while or prior to mixing has the benefit of reducing the matrix viscosity . reduced matrix viscosity in turn results in more efficient mixing . the matrix materials can be heated to temperature at or close to the melting point of the matrix composite . the melting point of the composite matrix is workable in the range of from about 25 ° c . to about 70 ° c . the melting point range of the matrix composition can also be from about 30 ° c . to about 50 ° c . the drug - to - matrix ratio can be concentrated enough to provide a low total mass per unit dose , yet can still be flowable to allow encapsulation using a rotary die encapsulation machine . a workable drug - to - matrix ratio range is from about 1 : 9 to about 1 : 1 by weight . the drug - to - matrix ratio range can also be from about 1 : 8 to about 1 : 1 by weight . the emulsion - type of matrix fill can be manufactured by dispersing the active ingredient or drug in the internal phase to provide a clear solution or suspension . the active ingredient or drug can be dispersed using propeller or homogenizer mixers . the internal phase materials can then be added to the molten external phase containing surfactant from about 0 . 1 % to about 5 % by weight . the emulsion can be made using mechanical forces generated by a propeller mixer , a homogenizer , or a microfluidizer . the matrix is then cooled to a temperature of from about 20 ° c . to about 35 ° c . for encapsulation using a rotary die encapsulation machine . the internal - to - external phase workable ratio is in the range of from about 0 . 5 : 10 to about 1 : 1 by weight . the ratio range can also be from about 1 : 9 to about 1 : 1 by weight . the workable drug - to - matrix ratio can be from about 1 : 100 to about 1 : 2 by weight . the range of the drug - to - matrix can also be from about 1 : 50 to about 1 : 3 by weight . the following examples are intended for purposes of illustration only , and should not be interpreted as limiting in any way of the scope of the invention . vegetable shortening , vegetable flakes , glyceryl mono oleate , span 60 and soybean oil were melted together at 50 ° c . to 70 ° c . ( wax or lipophilic phase ). methylcellulose , peg 3350 and peg 400 were melted separately at 50 ° c . to 70 ° c . ( aqueous phase ). diltiazem hydrochloride was dispersed in the melted aqueous phase and added slowly to the wax phase with homogenization , while maintaining the temperature between 50 ° c . and 70 ° c . the resultant homogeneous emulsion phase was cooled and encapsulated . filled capsules were subjected to dissolution as per usp using the paddle method in distilled water at 100 rpm . result : t 50 ( time required for 50 % dissolution ) is about 18 h . note : the procedure and evaluation followed for formulation 1 was also used for formulations 2 - 24 below . result : t 50 ( time required for 50 % dissolution ) is about 3 h . result : t 50 ( time required for 50 % dissolution ) is about 1 h . result : t 50 ( time required for 50 % dissolution ) is about 4 h . result : t 50 ( time required for 50 % dissolution ) is about 8 h . result : t 50 ( time required for 50 % dissolution ) is about 3 . 5 h . result : t 50 ( time required for 50 % dissolution ) is about 4 h . result : t 50 ( time required for 50 % dissolution ) is about 11 h . result : t 50 ( time required for 50 % dissolution ) is about 10 h . result : t 50 ( time required for 50 % dissolution ) is about 3 . 5 h . result : t 50 ( time required for 50 % dissolution ) is about & gt ; 24 h . result : t 50 ( time required for 50 % dissolution ) is about & gt ; 24 h . result : t 50 ( time required for 50 % dissolution ) is about 6 . 5 h . result : t 50 ( time required for 50 % dissolution ) is about 3 . 5 h . result : t 50 ( time required for 50 % dissolution ) is about & gt ; 24 h . result : t 50 ( time required for 50 % dissolution ) is about 6 . 5 h . result : t 50 ( time required for 50 % dissolution ) is about 1 . 5 h . result : t 50 ( time required for 50 % dissolution ) is about 1 . 5 h . result : t 50 ( time required for 50 % dissolution ) is about 20 h . result : t 50 ( time required for 50 % dissolution ) is about 20 h . result : t 50 ( time required for 50 % dissolution ) is about 0 . 3 h . result : t 50 ( time required for 50 % dissolution ) is about 0 . 3 h . result : t 50 ( time required for 50 % dissolution ) is about 0 . 6 h . vegetable shortening , vegetable flakes , yellow beeswax , glyceryl mono oleate , lecithin , span 60 and soybean oil were melted together at 50 ° c . to 70 ° c . ( wax phase ). methylcellulose , peg 3350 and peg 400 were melted separately at 50 ° c . to 70 ° c . ( aqueous phase ). about 77 % of diltiazem hydrochloride was dispersed in the melted aqueous phase and added slowly to the wax phase with homogenization , while maintaining the temperature between 50 ° c . and 70 ° c . remaining 23 % of diltiazem hydrochloride was added to the final resultant homogeneous emulsion . the emulsion was cooled and encapsulated . filled capsules were subjected for dissolution as per usp using paddle method in distilled water at 100 rpm . result : t 50 ( time required for 50 % dissolution ) is about 4 . 2 h . result : t 50 ( time required for 50 % dissolution ) is about 3 . 5 h . procedure adopted was similar to formulation 25 , but the model drug was dissolved in water before adding to the rest of the formulation . filled capsules were subjected for dissolution as per usp using paddle method in distilled water at 100 rpm . result : t 50 ( time required for 50 % dissolution ) is about & gt ; 8 h . vegetable shortening , vegetable flakes , gmo , and cremophor el 40 were melted with soybean oil between 50 ° c . and 70 ° c . to this melted mass , theophylline was added and homogenized . the resultant mixture was cooled while mixing and encapsulated . result : t 50 ( time required for 50 % dissolution ) is about 1 h . result : t 50 ( time required for 50 % dissolution ) is about & gt ; 24 h . result : t 50 ( time required for 50 % dissolution ) is about 16 h . result : t 50 ( time required for 50 % dissolution ) is about 12 h .
controlled release preparations and soft capsules are provided . also provided are emulsions and suspensions , including compositions and methods of manufacturing controlled release soft capsules , where the fill contains a suspension and / or an emulsion .