Pancreatin microspheres and production method thereof
A production method, pancreatin technology, applied in the direction of pharmaceutical formulations, medical preparations of non-active ingredients, digestive system, etc., can solve the problems of unfavorable enzyme stability, loss of enzyme activity, low industrial cost, etc., and achieve high bioavailability , high activity persistence, and the effect of reducing process costs
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Example Embodiment
[0018] Implementation mode 1:
[0019] This embodiment provides a pancreatin microsphere, which is composed of pancreatin, a mixture of corn starch and sucrose and polyethylene glycol (PEG 4000); wherein the weight percentage of pancreatin is 56.7%, The weight percentage of polyethylene glycol is 26.7%, and the weight percentage of the mixture of corn starch and sucrose is 16.6%.
[0020] The production method of the above pancreatin microspheres is as follows:
[0021] 680.0 g of pancreatin, 320.0 g of polyethylene glycol, and 200.0 g of a mixture of corn starch and sucrose were added to the reactor and heated to 70° C., mixed for 40 minutes, and then transferred to a basket with a fluidized bed with a rotor inserted. The disc is a knurled type, the speed is 1200rpm / min, while the hot air is blown to 70°C, running at a speed of 1-2m / s. The filter hose is shaken for 5 seconds within 6 seconds. After 20 minutes of heating and spheroidizing, the temperature of the air introduced was...
Example Embodiment
[0022] Implementation mode 2:
[0023] This embodiment provides a pancreatin microsphere, which is a pharmaceutical composition composed of pancreatin, microcrystalline cellulose and polyethylene glycol; the weight percentage of pancreatin is 71.8%, polyethylene glycol The weight percentage of cellulose is 19%, and the weight percentage of microcrystalline cellulose is 9.2%.
[0024] The production method of the above pancreatin microspheres is as follows:
[0025] 717.8 grams of pancreatin, 190.8 grams of polyethylene glycol and 91.4 grams of microcrystalline cellulose were added to the storage tank of a high-energy mixer. The operating speed of the blades of the machine is 900 rpm, and the heating jacket is 70°C. After 45 minutes of spheroidization, the heating is turned off, the blade speed is reduced to 120 rpm, and the outer jacket is cooled by the pipe water flow. After cooling for 15 minutes, the pellets were removed. The total process time is 60 minutes. The enzyme activ...
Example Embodiment
[0026] Implementation mode 3:
[0027] This embodiment provides a pancreatin microsphere, which is a pharmaceutical composition composed of pancreatin, colloidal silicon dioxide, a mixture of triethyl citrate and talc and polyethylene glycol; pancreatin The weight percentage is 40%, the weight percentage of polyethylene glycol is 50%, and the weight percentage of the mixture of colloidal silicon dioxide, triethyl citrate and talc is 10%.
[0028] Add 400.0 grams of pancreatin, 500.0 grams of polyethylene glycol, and 100.0 grams of colloidal silicon dioxide, triethyl citrate and talc mixture into the reactor, mix at 70°C for 20 minutes, and transfer to a rotor insert The fluidized bed basket. The disc is a knurled type, the speed is 1200rpm / min, while the hot air is blown to 70°C, running at a speed of 1-2m / s. The filter hose is shaken for 5 seconds within 6 seconds. After 20 minutes of spheroidization, the temperature of the introduced air dropped to 20°C. The mixed pellets are...
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