Compositions for oral adminstration of active principles requiring masking of taste
a technology of oral administration and active principles, applied in the field of pharmaceutical compositions, can solve the problems of unsuitable pediatric or oral formulation preparation, unacceptable organoleptic properties, and extremely prejudicial, or even vital, consequences
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example 1
[0029]2 400 g of precirol melted beforehand in an incubator at 60° C. are introduced into a jacketed reactor, the set jacket temperature of which is fixed at 75° C. 78 g of soybean lecithin are added. When the soybean lecithin is dissolved, the set temperature is lowered to 65° C. and 540 g of pristinamycin are added. Stirring is carried out for 20 minutes at 300 rpm, and then the suspension is passed over a bore mill.
[0030]1 248 g of the ground suspension are then sprayed via a two-fluid nozzle in a prilling tower precooled with a current of cold nitrogen. At the beginning of spraying the temperature is 0° C. at the top of the tower and −20° C. at the bottom of the tower. The air pressure on the two-fluid nozzle is 1.5 bar, which produces a spray-air flow rate of 2.3 m3 / h. The flow rate of liquid is 4.7 kg / h.
[0031]At the end of spraying, the product is then fluidized for 20 minutes at −20° C., and then for 2 hours at 32° C.
[0032]The particle size of the product obtained, measured b...
example 2
[0039]704 g of precirol are introduced into a jacketed reactor, the set jacket temperature of which is fixed at 75° C. When the precirol is molten, 18 g of soybean lecithin are added. When the soybean lecithin is dissolved, 182 g of pristinamycin premicronized in an air jet micronizer, and exhibiting, after grinding, a median diameter of 2 μm, are added. Stirring is carried out for 45 minutes at 800 rpm in order to obtain a homogeneous suspension.
[0040]The suspension is then sprayed via a two-fluid nozzle in a prilling tower precooled with a current of cold nitrogen. At the beginning of spraying, the temperature is −14° C. at the top of the tower and −42° C. at the bottom of the tower. The air pressure on the two-fluid nozzle is 1.5 bar, which produces a spray-air flow rate of 2.3 m3 / h. The flow rate of liquid is 10.8 kg / h.
[0041]The particle size of the product obtained, measured by sieving, is:[0042]30% of particles between 0 and 100 μm[0043]54% of particles between 100 and 315 μm[...
example 3
[0048]907 g of precirol are added to a jacketed reactor, the set jacket temperature of which is fixed at 70° C. When the precirol is molten, 23 g of soybean lecithin are added. When the soybean lecithin is dissolved, 207 g of unground telithromycin exhibiting a median diameter of 114 μm are introduced. Stirring is carried out for 50 minutes at 500 rpm in order to obtain a homogeneous liquid: the telithromycin is visibly soluble in the precirol.
[0049]The suspension is then sprayed via a two-fluid nozzle in a prilling tower precooled with a current of cold nitrogen. At the beginning of spraying, the temperature is 0° C. at the top of the tower and −20° C. at the bottom of the tower. The air pressure on the two-fluid nozzle is 1.3 bar, which produces a spray-air flow rate of 4 m3 / h. The flow rate of liquid is 8.5 kg / h.
[0050]The particle size of the product obtained, measured by sieving, is:[0051]59% of particles between 0 and 100 μm[0052]38% of particles between 100 and 315 μm[0053]3% ...
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