Colon-targeted active agent delivery carrier and uses thereof
US-2024390501-A1 · Nov 28, 2024 · US
US2020188302A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020188302-A1 |
| Application number | US-201916598299-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 10, 2019 |
| Priority date | Apr 14, 2017 |
| Publication date | Jun 18, 2020 |
| Grant date | — |
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The purpose of the present invention is to provide a method for producing granules of having a uniform size. To this end, the present invention provides a method for producing granules, the method characterized by including preparing an organic member solution, uniformly dispersing an inorganic member in the organic member solution at a weight ratio of 1 to 10 based on an organic member to form an organic-inorganic composite solution, spraying the organic-inorganic composite solution in an electrostatic charge manner, and polymerizing the sprayed organic-inorganic composite solution to form a hydrogel phase. The production method of the present invention has advantages in that granules having a uniform size may be mass-produced in a short time and the granules may be produced at a high yield. Accordingly, the production method of the present invention has advantages in that the method may be applied to a variety of fields, such as a pharmaceutical field, a medical field, a cosmetics field, and a food field and that the method may replace a conventional spray drying method.
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1 . A method for manufacturing granules, the method comprising: preparing an organic member solution; uniformly dispersing an inorganic member in the organic member solution at a weight ratio of 1 to 10 based on an organic member to form an organic-inorganic composite solution; spraying the organic-inorganic composite solution in an electrostatic charge manner; and polymerizing the sprayed organic-inorganic composite solution to form a hydrogel phase. 2 . The method of claim 1 , wherein the weight ratio of the inorganic member dispersed in the organic member solution to the organic member is 5 to 10. 3 . The method of claim 1 , further comprising, after forming the organic-inorganic composite solution, dispersing the inorganic member with a rotation and revolution mixer and stirring the resultant composite solution with an ultrasonic mixer. 4 . The method of claim 1 , wherein the polymerizing of the organic-inorganic composite solution is performed by dropping sprayed granules to a polymerization-inducing solution. 5 . The method of claim 1 , wherein the inorganic member comprises a functional member. 6 . The method of claim 1 , further comprising supporting a functional member or cells in the formed organic-inorganic composite solution. 7 . The method of claim 1 , wherein the concentration of the organic member solution is 0.5-5 wt %. 8 . The method of claim 1 , wherein the size of the inorganic member is 20 nm to 10 μm. 9 . The method of claim 3 , wherein the dispersing of the inorganic member with a rotation and revolution mixer and stirring the resultant composite solution with an ultrasonic mixer is performed in a range where the temperature of the organic-inorganic composite solution does not exceed 40° C. 10 . The method of claim 1 , wherein the spraying of the organic-inorganic composite solution in an electrostatic charge manner is performed by using a micro-granule coater, and the micro-granule coater has a spray nozzle size in the range of 50-1,000 μm, a voltage in the range of 500-2,500 V, a pressure in the range of 100-1,500 mbar, and a vibration frequency in the range of 100-6,000 Hz. 11 . The method of claim 1 , wherein the hydrogel phase does not comprise a dispersant. 12 . The method of claim 1 , further comprising washing and drying the formed hydrogel phase; and sintering the washed and dried hydrogel phase. 13 . The method of claim 1 , wherein the organic member comprises at least one organic matter among alginate, collagen, gelatin, chitosan, cellulose, natural polymers, and a biopolymer. 14 . The method of claim 1 , wherein the inorganic member comprises at least one among hydroxy apatite (HA), dicalcium phosphate (DCP), tricalcium phosphate (TCP), tetracalcium phosphate (TTCP), and octacalcium phosphate (OCP). 15 . The method of claim 10 , wherein the average diameter of the granules is controlled according to change in the spray nozzle size, pneumatic condition and frequency of the micro-granule coater. 16 . The method of claim 1 , the polymerizing is performed by any one among ion crosslinking, chemical crosslinking, and photo crosslinking. 17 . The method of claim 16 , wherein the ion crosslinking uses at least one polymerization-inducing material among calcium chloride (CaCl 2 )), calcium sulfate (CaSO 4 ), and calcium carbonate (CaCO 3 ). 18 . The method of claim 12 , wherein the sintering is performed at a temperature range of 1000-1300° C. to remove the organic member. 19 . The method of claim 12 , wherein the size and porosity of the granules are controlled according to the content of the inorganic member to the organic member. 20 . The method of claim 12 , wherein the produced granules are granulated particles comprising calcium oxide (CaO) and the content of the calcium oxide is 1 to 10 mass %.
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