Lutein ester preparation for tabletting and preparation method thereof
A technology of lutein ester and preparation, which is applied to the field of tableted lutein ester preparation and preparation thereof, can solve the problems of not being able to achieve the ideal protection of lutein ester, easy to break, etc., and achieves good product stability, resistance to The effect of strong pressure resistance, increased stability and pressure resistance
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Embodiment 1
[0030] This embodiment relates to a preparation method of a lutein ester preparation, comprising the following steps:
[0031] 1) Add 2kg of gelatin, 2kg of maltodextrin and 0.2kg of ascorbic acid into 10kg of purified water, stir and dissolve in a water bath at 60°C to obtain an aqueous phase;
[0032] Stir and melt 1kg lutein ester, 0.1kg sunflower oil and 0.2kg vitamin E in a 70°C water bath to obtain the oil phase;
[0033] 2) Slowly add the oil phase into the water phase for high-shear emulsification with a linear velocity of 12m / s; the particle size of the emulsion after emulsification is 0.23μm;
[0034] 3) Degassing treatment is carried out under a vacuum degree of 2 Pa;
[0035] 4) One-step granulation of the defoamed emulsion by a spray-fluidized bed drying method, the spray drying conditions are: air inlet temperature 90°C, fluidized bed blast temperature 90°C; the obtained lutein ester particles;
[0036] 5) Further embedding the lutein ester particles with 45% g...
Embodiment 2
[0038] This embodiment relates to a preparation method of a lutein ester preparation, comprising the following steps:
[0039] 1) Add 20kg of gelatin, 30kg of sucrose and 2kg of ascorbic acid into 10kg of purified water, stir and dissolve in a water bath at 60°C to obtain an aqueous phase;
[0040] Stir and melt 1kg lutein ester, 0.1kg sunflower oil and 0.2kg vitamin E in a 70°C water bath to obtain the oil phase;
[0041] 2) Slowly add the oil phase into the water phase for high-shear emulsification with a linear velocity of 12m / s; the particle size of the emulsion after emulsification is 0.18μm;
[0042] 3) Degassing treatment is carried out under a vacuum degree of 5 Pa;
[0043] 4) The defoamed emulsion is subjected to one-step granulation by a spray-fluidized bed drying method, and the spray drying conditions are: the inlet air temperature is 100°C, and the fluidized bed blast temperature is 100°C;
[0044] 5) The obtained particles were further embedded in 40% gelatin ...
Embodiment 3
[0046] This embodiment relates to a preparation method of a lutein ester preparation, comprising the following steps:
[0047] 1) Add 0.2kg of gelatin, 0.3kg of sucrose and 0.5kg of ascorbic acid into 1kg of purified water, stir and dissolve in a water bath at 80°C to obtain an aqueous phase;
[0048] Stir and melt 0.1kg lutein ester, 0.02kg sunflower oil and 0.05kg vitamin E in an 80°C water bath to obtain the oil phase;
[0049] 2) Slowly add the oil phase into the water phase for high-shear emulsification with a line speed of 8m / s; the particle size of the emulsion after emulsification is 0.28μm;
[0050] 3) Degassing treatment is carried out under a vacuum degree of 10 Pa;
[0051] 4) The defoamed emulsion is subjected to one-step granulation by a spray-fluidized bed drying method, and the spray drying conditions are: the inlet air temperature is 100°C, and the fluidized bed blast temperature is 95°C;
[0052] 5) The obtained microparticles were further embedded with 50%...
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