WO2009092333A1 - Device and process for preparing sodium alginate/chitosan slow release capsules with high efficiency - Google Patents
Device and process for preparing sodium alginate/chitosan slow release capsules with high efficiency Download PDFInfo
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- WO2009092333A1 WO2009092333A1 PCT/CN2009/070212 CN2009070212W WO2009092333A1 WO 2009092333 A1 WO2009092333 A1 WO 2009092333A1 CN 2009070212 W CN2009070212 W CN 2009070212W WO 2009092333 A1 WO2009092333 A1 WO 2009092333A1
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- sodium alginate
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
- A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
- A61K9/1605—Excipients; Inactive ingredients
- A61K9/1629—Organic macromolecular compounds
- A61K9/1652—Polysaccharides, e.g. alginate, cellulose derivatives; Cyclodextrin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/10—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic in stationary drums or troughs, provided with kneading or mixing appliances
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61J—CONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
- A61J3/00—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms
- A61J3/07—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms into the form of capsules or similar small containers for oral use
Definitions
- the invention discloses an apparatus and a preparation process for preparing sodium alginate/chitosan sustained-release microcapsules. Background technique
- Sodium alginate/chitosan sustained release microcapsules have good biocompatibility and mechanical strength and are an excellent sustained release drug delivery system widely used in drug controlled release vehicles, gene delivery vehicles, immunoisolation and Artificial organs, cell culture microreactors, environmental purification and other aspects.
- the preparation methods of sodium alginate/chitosan sustained-release microcapsules mainly include dripping method, spray calligraphy and emulsification method.
- the drip method is mainly prepared by using a syringe drop.
- the microcapsules are formed by drop, and the efficiency is low.
- the particle size of the sustained release microcapsules is limited by the inner diameter of the syringe needle and the viscosity of the solution.
- the spray method mainly uses a coaxial jet device and an electrostatic titration device.
- the microcapsules prepared by this method have larger particle size, poor microsphere shape and smoothness, and the particle size of the sustained release microcapsules is also affected by the inner diameter of the nozzle and the viscosity of the solution. Restricted, and the equipment is complex, it is difficult to scale production. Later, educators invented the emulsification method, which can carry out large-scale industrial production.
- the main disadvantage is that the gel bead shape is unstable, and the particle size distribution of the sustained-release microcapsules is wide and distributed in multiple intervals, and the preparation process is relatively complicated.
- the technical problem to be solved by the present invention is to overcome the defects of the prior art mentioned above, and provide an apparatus and a preparation process for efficiently and rapidly preparing sodium alginate/chitosan sustained-release microcapsules, and improving the microcapsule drug content, encapsulation efficiency and Uniformity of microcapsules, simplifying the preparation process, improving production efficiency and production Scale.
- the present invention adopts the following technical solutions:
- An apparatus for efficiently preparing sodium alginate/chitosan sustained-release microcapsules characterized by comprising an emulsifier device and a centrifugal sieve granulator which are automatically connected to each other by a draft tube, the emulsifier device comprising The emulsifying tank and the emulsifier motor and the three-way valve mounted thereon, the emulsification tank is divided into three parts, the upper part is a mixing tank with a feeding port, the middle part is a crusher, and the lower part is provided The emulsification tank of the discharge port, the three-way valve is installed at the discharge port and respectively connected with a return pipe and a draft tube, the output shaft of the emulsifier motor extends into the emulsion tank, and the output shaft is located at the mixing tank.
- the mixing tank is agitating the paddle, and the output shaft is located at the miller with a spiral grooved grinding rod matched with the inner wall of the mill, and the output shaft is located at the emulsion tank and is connected with the emulsifier pool stirring paddle.
- the centrifugal sieve granulator comprises a curing reaction tank, the upper part of the curing reaction tank is connected with the draft tube, and the collecting tube is connected at the bottom, and the tank is provided with a sieve barrel with a plurality of sieve holes on the side wall, and the curing reaction tank
- the top is provided with a bucket-shaped feeding tube which is connected with the sieve barrel, and the sieve barrel is mounted on the rotating shaft, and the rotating shaft is connected through the curing reaction tank and the external speed regulating motor.
- the curing reaction tank of the centrifugal sieve granulator is provided with a circle of waterfall grooves around the inner wall of the tank, and the waterfall tank is higher than the working surface of the sieve hole, and the curing reaction tank is externally connected with a circulation tube with a liquid pump, and one end of the circulation tube
- the curing reaction tank is connected to the waterfall tank, and the other end is connected to the bottom of the curing reaction tank; a filter screen is arranged at the bottom of the curing reaction tank and the connection of the circulation pipe.
- the rotating shaft is provided with a stirring paddle, and the stirring paddle is located below the screen barrel.
- the curing reaction tank is a split structure, which is formed by docking the detachable top cover and the can body.
- the screen barrel and the rotating shaft are detachably connected.
- the preparation process for efficiently preparing sodium alginate/chitosan sustained-release microcapsules using the above-mentioned equipment for efficiently preparing sodium alginate/chitosan sustained-release microcapsules adopts the following steps: First ⁇ , emulsification step: dissolving a fat-soluble or water-soluble drug in a sodium alginate solution as a dispersing agent, and preparing a medicated emulsified droplet or suspension by an automatic stirring ore emulsification device; ⁇ , granulation process: The first mash preparation solution is poured into a centrifugal sieve granulator, which is centrifuged and combined with a calcium chloride chitosan solution to form a drug-containing sodium alginate/chitosan sustained-release micro bag;
- Liquid A mass percentage of 1.5% sodium alginate solution + mass percentage of 2% drug
- liquid B volume fraction of 1% acetic acid + mass fraction of 1% calcium chloride + mass fraction 0.5% chitosan solution.
- the emulsifier After adding the liquid A to the emulsifier, it is fully suspended and emulsified by circulating stirring and milling.
- the speed of the emulsified motor is 500r/min-4000r/min, and the emulsification time is 30min-60min.
- liquid B Adding liquid B to the curing reaction tank of the centrifugal sieve granulator, the liquid A containing the emulsified drug enters the sieve barrel of the centrifugal sieve granulator through the diversion tube, and is centrifugally extracted into the curing reaction tank, and B
- the liquid-binding reaction generates a sodium alginate/chitosan sustained-release microcapsule; the speed of the speed regulating motor of the centrifugal sieve granulator is 300r/min-1000r/min.
- the invention has high automation degree by new equipment and preparation process, and can quickly and efficiently prepare sodium alginate/chitosan sustained release microcapsule with good spherical shape, high yield, high surface smoothness and narrow particle size distribution, and is easy to be prepared. Industrial production.
- the process of preparing the sustained-release microcapsules can also control the size of the microcapsules by adjusting the motor rotation speed, and prepare sodium alginate/chitosan sustained-release microcapsules with different particle diameters to meet the actual needs.
- FIG. 1 is a schematic view showing the structure of an emulsifier A and a centrifugal granulator B according to the present invention.
- an apparatus for efficiently preparing sodium alginate/chitosan sustained-release microcapsules comprising an emulsifier device and a centrifugal sieve granulator which are automatically connected to each other by a draft tube 11 and an emulsifier device
- the invention comprises an emulsifying tank and an emulsifier motor 1 and a three-way valve 9 mounted thereon, the emulsifier tank is divided into upper and lower parts, the upper part is a mixing tank 2 with a feeding port 6, the middle part is a crusher 3, and the lower part
- the three-way valve 9 is installed at the discharge port and is respectively connected with the return pipe 10 and the draft tube 11, and the output shaft of the emulsifier motor 1 extends into the emulsification tank, and the output shaft is located at the mixing
- the output shaft is located at the miller with a spiral grooved grinding rod 4 matched
- the centrifugal sieve granulator comprises a curing reaction tank 14, the upper part of the curing reaction tank 14 is connected with the draft tube 11, and the bottom is connected with a collecting tube 23, and the tank is provided with a sieve barrel 15 having a plurality of sieve holes on the side wall, and solidified.
- the top of the reaction tank 14 is provided with a bucket-shaped feed pipe 13 communicating with the sieve drum 15, and the sieve drum 15 is mounted on the rotating shaft, and the rotating shaft is connected through the curing reaction tank 14 and the external speed regulating motor 12.
- the curing reaction tank 14 of the centrifugal sieve granulator is provided with a circle of waterfall grooves 18 around the inner wall of the tank, the waterfall tank 18 is higher than the working surface of the screen hole, and the curing reaction tank 14 is connected with a pumping liquid.
- the circulation pipe 22 of the pump 21, the end of the circulation pipe 22 is connected to the curing reaction tank 14 and connected to the waterfall tank 18, and the other end is connected to the bottom of the curing reaction tank 14.
- the bottom of the curing reaction tank 14 and the circulation pipe 22 are provided with a filter screen. Web 20.
- a stirring paddle 16 is mounted on the rotating shaft, and the stirring paddle 16 is located below the sieve drum.
- the curing reaction tank 14 has a split structure and is formed by a detachable top cover and a can body. There is a detachable connection between the sieve drum 15 and the rotating shaft.
- Solution A Mass percentage of 1.5% sodium alginate solution + mass percentage of 2% curcumin
- Solution B acetic acid with a volume fraction of 1% + calcium chloride with mass fraction of 1% + mass fraction a 0.5% chitosan solution
- the liquid A is added to the mixing tank 2 at the upper portion of the emulsifying tank through the feeding port 6, and the emulsifier motor 1 is turned on, the rotation speed is 1000r/min, and the mixing tank stirring paddle 7 is stirred and pushed.
- the pulverizer 3 entering the middle of the emulsification tank is crushed by the sifting tank with the spiral groove and pushed into the emulsification tank 5 at the lower part of the emulsification tank, and the emulsification tank stirring paddle 8 is stirred one by one.
- the three-way valve 9 at the discharge port is turned to the state A2 to turn on the return pipe 10, and the liquid A is returned to the upper portion of the emulsion tank to be stirred and crushed, and fully suspended for 30 minutes to prepare a curcumin sodium alginate suspension. .
- the liquid B is supplied to the solidification reaction tank 14 of the centrifugal sieve granulator through the inlet pipe 17. Subsequently, the three-way valve 9 is turned to the state A4 to turn on the draft tube 11, and the obtained curcumin sodium alginate suspension sequentially flows into the bucket-shaped feed tube 13 and the sieve barrel 15 of the centrifugal sieve granulator.
- the pumping pump 21 is turned on to pump the liquid B in the curing reaction tank 14 to the rising tank 18 through the circulation pipe 22 and overflow to form a solution curtain.
- the rotation speed is 400r/min, centrifuge the curcumin sodium alginate suspension into the curing reaction tank 14, and react with the B liquid. A curcumin-containing sodium alginate/chitosan sustained release microcapsule is produced.
- the B liquid consumed can be continuously replenished from the inlet pipe 17 throughout the production process.
- the microcapsule product can be collected from collection tube 23.
- the collected microcapsule product was placed in solution B for further 30 minutes, and then the solution was sieved, washed with water, and dried by blowing at 55 ° C to prepare a microcapsule product.
- the production can work continuously without parking. If it is necessary to produce particles of different sizes, simply adjust the motor speed or change the diameter of the different types of sieve drums and the aperture of the sieve holes.
- Liquid A mass percentage of 1.5% sodium alginate solution + mass percentage of 2% zedoary turmeric oil
- liquid B volume fraction of 1% acetic acid + mass fraction of 1% calcium chloride + mass fraction It is a 0.5% chitosan solution.
- the liquid A is added to the mixing tank 2 at the upper portion of the emulsifying tank through the feeding port 6, and the emulsifier motor 1 is turned on, the rotation speed is 1000r/min, and the mixing tank stirring paddle 7 is stirred and pushed.
- the pulverizer 3 entering the middle of the emulsification tank is crushed by the sifting tank with the spiral groove and pushed into the emulsification tank 5 at the lower part of the emulsification tank, and the emulsification tank stirring paddle 8 is stirred one by one.
- the three-way valve 9 at the discharge port is turned to the state A2 to be connected to the return pipe 10, and the liquid A is returned to the upper portion of the emulsion tank for circulation stirring and grinding, and fully suspended for 30 minutes to prepare a sorghum oil sodium alginate suspension. .
- the liquid B is supplied to the solidification reaction tank 14 of the centrifugal sieve granulator through the inlet pipe 17. Subsequently, the three-way valve 9 is turned to the state A4 to turn on the draft tube 11, and the prepared zedoary turmeric sodium alginate suspension sequentially flows into the bucket-shaped feed tube 13 and the sieve barrel 15 of the centrifugal sieve granulator.
- the pumping pump 21 is turned on to pump the liquid B in the curing reaction tank 14 to the rising tank 18 through the circulation pipe 22 and overflow to form a solution curtain.
- the rotation speed is 400r/min, centrifuge the sorghum oil sodium alginate suspension into the curing reaction tank 14, and react with the B liquid.
- the sorghum oil sodium alginate/chitosan sustained release microcapsules were prepared.
- the B liquid consumed can be continuously replenished from the inlet pipe 17 throughout the production process.
- the microcapsule product can be collected from collection tube 23.
- the collected microcapsule product was placed in solution B for further 30 minutes, then the solution was sieved, washed with water, and dried at 45 ° C to form a microcapsule product.
- the production can work continuously without parking. If it is necessary to produce particles of different sizes, simply adjust the motor speed or change the diameter of the different types of sieve drums and the aperture of the sieve holes.
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Abstract
A device and a process for preparing sodium alginate/chitosan slow release capsules. The device comprises an emulsifier device (A) capable of automatically stirring and grinding and a centrifugal screen pelletizer (B) connected with each other by a guide pipe (11). The process comprises emulsification, pelletization, conditioning and other steps by use of the device.
Description
高效制备海藻酸钠 /壳聚糖缓释微囊的设备和制备工艺 技术领域 Equipment and preparation process for efficiently preparing sodium alginate/chitosan sustained-release microcapsule
本发明公开了一种制备海藻酸钠 /壳聚糖缓释微囊的设备和制备工艺。 背景技术 The invention discloses an apparatus and a preparation process for preparing sodium alginate/chitosan sustained-release microcapsules. Background technique
海藻酸钠 /壳聚糖缓释微囊说具有良好的生物相容性和机械强度, 是一种优 良的缓释给药系统, 广泛应用于药物控释载体、 基因运载工具、 免疫隔离作 用和人工器官、 细胞培养微反应器、 环境净化等各个方面。 目前海藻酸钠 /壳 聚糖缓释微囊的制备方法主要有滴液法、 喷雾书法和乳化法三大类。 滴液法主 要采用注射器滴液制备, 微囊是逐滴形成的, 效率低, 缓释微囊粒径受注射 器针头内径和溶液粘度的限制。 喷雾法主要采用同轴喷气装置和静电滴定装 置, 这种方法制备的微囊的粒径较大、 微囊球型度和光洁度较差, 缓释微囊 粒径同样受喷头内径和溶液粘度的限制, 且设备复杂, 难以规模生产。 后来 学者发明了乳化法, 此方法可以进行大规模的工业化生产, 主要缺点是凝胶 珠球型度不稳定, 缓释微囊粒径分布范围宽且呈多区间分布, 制备过程相对 复杂。 在制备海藻酸钙胶珠时, 由于钙盐很难分散均匀, 微囊化物质易流失, 致使包封率降低, 因此也无法满足医药、 化工领域中对物质活性和缓释微囊 均匀性的要求, 因此, 提高药物包封率和制剂稳定性是海藻酸钠 /壳聚糖缓释 制剂研究中亟待解决的问题。 Sodium alginate/chitosan sustained release microcapsules have good biocompatibility and mechanical strength and are an excellent sustained release drug delivery system widely used in drug controlled release vehicles, gene delivery vehicles, immunoisolation and Artificial organs, cell culture microreactors, environmental purification and other aspects. At present, the preparation methods of sodium alginate/chitosan sustained-release microcapsules mainly include dripping method, spray calligraphy and emulsification method. The drip method is mainly prepared by using a syringe drop. The microcapsules are formed by drop, and the efficiency is low. The particle size of the sustained release microcapsules is limited by the inner diameter of the syringe needle and the viscosity of the solution. The spray method mainly uses a coaxial jet device and an electrostatic titration device. The microcapsules prepared by this method have larger particle size, poor microsphere shape and smoothness, and the particle size of the sustained release microcapsules is also affected by the inner diameter of the nozzle and the viscosity of the solution. Restricted, and the equipment is complex, it is difficult to scale production. Later, scholars invented the emulsification method, which can carry out large-scale industrial production. The main disadvantage is that the gel bead shape is unstable, and the particle size distribution of the sustained-release microcapsules is wide and distributed in multiple intervals, and the preparation process is relatively complicated. In the preparation of calcium alginate beads, since the calcium salt is difficult to disperse uniformly, the microencapsulated material is easily lost, resulting in a lower encapsulation efficiency, and thus cannot satisfy the substance activity and the uniformity of the sustained release microcapsules in the fields of medicine and chemical industry. Therefore, improving the drug encapsulation efficiency and formulation stability is an urgent problem to be solved in the research of sodium alginate/chitosan sustained release preparation.
发明内容 Summary of the invention
本发明所要解决的技术问题是克服上述现有技术存在的缺陷, 提供一种 高效快速制备海藻酸钠 /壳聚糖缓释微囊的设备和制备工艺, 提高微囊药物含 量、 包封率和微囊粒径均一性, 进一歩简化制备工艺, 提高生产效率和生产
规模。 为此, 本发明采用如下的技术方案: The technical problem to be solved by the present invention is to overcome the defects of the prior art mentioned above, and provide an apparatus and a preparation process for efficiently and rapidly preparing sodium alginate/chitosan sustained-release microcapsules, and improving the microcapsule drug content, encapsulation efficiency and Uniformity of microcapsules, simplifying the preparation process, improving production efficiency and production Scale. To this end, the present invention adopts the following technical solutions:
高效制备海藻酸钠 /壳聚糖缓释微囊的设备, 其特征在于包括通过导流管 相互连接的可自动搅拌碾礦的乳化器装置和离心筛制粒机, 所述的乳化器装 置包括乳化罐及安装于其上的乳化器电机和三通阀, 所述的乳化罐分上中下 三部分, 上部为带有进料口的混匀池, 中部为碾礦器, 下部为设有出料口的 乳化池, 所述的三通阀安装于出料口并分别连接有返回管、 导流管, 乳化器 电机的输出轴伸入乳化罐中, 输出轴位于混匀池处设有混匀池搅拌桨, 输出 轴位于碾礦器处设有与碾礦器内壁配合的带有螺旋槽的碾礦棒, 输出轴位于 乳化池处连接有乳化池搅拌桨。 An apparatus for efficiently preparing sodium alginate/chitosan sustained-release microcapsules, characterized by comprising an emulsifier device and a centrifugal sieve granulator which are automatically connected to each other by a draft tube, the emulsifier device comprising The emulsifying tank and the emulsifier motor and the three-way valve mounted thereon, the emulsification tank is divided into three parts, the upper part is a mixing tank with a feeding port, the middle part is a crusher, and the lower part is provided The emulsification tank of the discharge port, the three-way valve is installed at the discharge port and respectively connected with a return pipe and a draft tube, the output shaft of the emulsifier motor extends into the emulsion tank, and the output shaft is located at the mixing tank. The mixing tank is agitating the paddle, and the output shaft is located at the miller with a spiral grooved grinding rod matched with the inner wall of the mill, and the output shaft is located at the emulsion tank and is connected with the emulsifier pool stirring paddle.
所述的离心筛制粒机包括一个固化反应罐, 固化反应罐上部与导流管相 连, 底部接有收集管, 罐内设有一个侧壁开有复数个筛孔的筛桶, 固化反应 罐顶部设有一个和筛桶连通的斗状进料管, 筛桶安装在转轴上, 转轴穿过固 化反应罐和外置的调速电机连接。 The centrifugal sieve granulator comprises a curing reaction tank, the upper part of the curing reaction tank is connected with the draft tube, and the collecting tube is connected at the bottom, and the tank is provided with a sieve barrel with a plurality of sieve holes on the side wall, and the curing reaction tank The top is provided with a bucket-shaped feeding tube which is connected with the sieve barrel, and the sieve barrel is mounted on the rotating shaft, and the rotating shaft is connected through the curing reaction tank and the external speed regulating motor.
所述的离心筛制粒机的固化反应罐中环绕罐内壁设有一圈起瀑槽, 起瀑 槽高于筛孔所在工作面, 固化反应罐外接一个带抽液泵的循环管, 循环管一 端接入固化反应罐内连接起瀑槽, 另一端接在固化反应罐底部; 固化反应罐 底部和循环管连接处设有过滤筛网。 The curing reaction tank of the centrifugal sieve granulator is provided with a circle of waterfall grooves around the inner wall of the tank, and the waterfall tank is higher than the working surface of the sieve hole, and the curing reaction tank is externally connected with a circulation tube with a liquid pump, and one end of the circulation tube The curing reaction tank is connected to the waterfall tank, and the other end is connected to the bottom of the curing reaction tank; a filter screen is arranged at the bottom of the curing reaction tank and the connection of the circulation pipe.
所述的转轴上装有搅拌桨, 所述的搅拌桨位于筛桶下方。 The rotating shaft is provided with a stirring paddle, and the stirring paddle is located below the screen barrel.
所述的固化反应罐为分体结构, 由可拆卸的顶盖和罐身上下对接而成。 所述的筛桶和转轴之间为可拆卸连接。 The curing reaction tank is a split structure, which is formed by docking the detachable top cover and the can body. The screen barrel and the rotating shaft are detachably connected.
高效制备海藻酸钠 /壳聚糖缓释微囊的制备工艺, 利用所述的高效制备海 藻酸钠 /壳聚糖缓释微囊的设备采用以下歩骤:
第一歩, 乳化歩骤: 以海藻酸钠溶液为分散剂, 将脂溶性或水溶性药物 分散溶解于其中, 经自动搅拌碾礦乳化裝置制成含药乳化小滴或混悬液; 第二歩, 制粒歩骤: 令第一歩的制备液流入离心筛制粒机, 经离心甩出 并和氯化钙壳聚糖溶液结合反应, 生成含药海藻酸钠 /壳聚糖缓释微囊; The preparation process for efficiently preparing sodium alginate/chitosan sustained-release microcapsules, using the above-mentioned equipment for efficiently preparing sodium alginate/chitosan sustained-release microcapsules adopts the following steps: First 歩, emulsification step: dissolving a fat-soluble or water-soluble drug in a sodium alginate solution as a dispersing agent, and preparing a medicated emulsified droplet or suspension by an automatic stirring ore emulsification device;歩, granulation process: The first mash preparation solution is poured into a centrifugal sieve granulator, which is centrifuged and combined with a calcium chloride chitosan solution to form a drug-containing sodium alginate/chitosan sustained-release micro bag;
第三歩, 整理歩骤: 固化、 收集、 水洗第二歩所得制备物, 以小于等于 The third step, the finishing step: curing, collecting, washing the second mash to obtain a preparation, less than or equal to
55°C的风干燥。 Dry at 55 ° C.
还包括以下歩骤: It also includes the following steps:
以制药用水配制下列溶液: Prepare the following solutions in pharmaceutical water:
A液: 质量百分含量为 1 .5%海藻酸钠溶液 +质量百分含量为 2%药物; B液: 容积分数为 1 %的乙酸 +质量分数为 1 %的氯化钙 +质量分数为 0.5% 的壳聚糖溶液。 Liquid A: mass percentage of 1.5% sodium alginate solution + mass percentage of 2% drug; liquid B: volume fraction of 1% acetic acid + mass fraction of 1% calcium chloride + mass fraction 0.5% chitosan solution.
将 A液加入乳化器后, 通过循环搅拌和碾礦使其充分混悬、 乳化, 乳化 电机的转速为 500r/min-4000r/min, 乳化时间为 30min-60min。 After adding the liquid A to the emulsifier, it is fully suspended and emulsified by circulating stirring and milling. The speed of the emulsified motor is 500r/min-4000r/min, and the emulsification time is 30min-60min.
将 B液加入离心筛制粒机的固化反应罐, 所述的含药已乳化的 A液经导 流管进入离心筛制粒机的筛桶, 经离心甩出至固化反应罐内, 与 B液结合反 应生成含药海藻酸钠 /壳聚糖缓释微囊; 离心筛制粒机的调速电机的转速为 300r/min-1000r/min。 Adding liquid B to the curing reaction tank of the centrifugal sieve granulator, the liquid A containing the emulsified drug enters the sieve barrel of the centrifugal sieve granulator through the diversion tube, and is centrifugally extracted into the curing reaction tank, and B The liquid-binding reaction generates a sodium alginate/chitosan sustained-release microcapsule; the speed of the speed regulating motor of the centrifugal sieve granulator is 300r/min-1000r/min.
本发明通过新的设备和制备工艺, 自动化成度高, 能高效快速制备出球 型度好、 产量高、 表面光洁度高、 粒径分布窄的海藻酸钠 /壳聚糖缓释微囊, 易于工业化生产。 此外, 该工艺制备缓释微囊的过程中还可以通过调节电机 转速来控制微囊粒径的大小, 制备出不同粒径的海藻酸钠 /壳聚糖缓释微囊, 满足实际需要。
下面结合说明书附图和具体实施方式对本发明作进一歩的说明。 The invention has high automation degree by new equipment and preparation process, and can quickly and efficiently prepare sodium alginate/chitosan sustained release microcapsule with good spherical shape, high yield, high surface smoothness and narrow particle size distribution, and is easy to be prepared. Industrial production. In addition, the process of preparing the sustained-release microcapsules can also control the size of the microcapsules by adjusting the motor rotation speed, and prepare sodium alginate/chitosan sustained-release microcapsules with different particle diameters to meet the actual needs. The invention will now be further described in conjunction with the drawings and specific embodiments.
附图说明 DRAWINGS
图 1为本发明乳化器 A与离心筛制粒机 B的结构示意图。 BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the structure of an emulsifier A and a centrifugal granulator B according to the present invention.
图中, 1、 乳化器电机, 2、 混匀池, 3、 碾礦器, 4、 带螺旋槽的碾礦捧, 5、 乳化池, 6、 进料口, 7、 混匀池搅拌桨, 8、 乳化池搅拌桨, 9、 三通阀, 10、 返回管, 11、 导流管, 12、 调速电机, 13、 进料管, 14、 固化反应罐, 15、 筛桶, 16、 搅拌桨, 17、 进液管, 18、 起瀑槽, 19、 液面, 20、 过滤筛 网, 21、 抽液泵, 22、 循环管, 23、 收集管。 In the figure, 1, the emulsifier motor, 2, the mixing tank, 3, the mill, 4, the grinding tank with the spiral groove, 5, the emulsification tank, 6, the feed port, 7, the mixing tank stirring paddle, 8. Emulsifying tank stirring paddle, 9, three-way valve, 10, return pipe, 11, diversion pipe, 12, speed regulating motor, 13, feed pipe, 14, curing reaction tank, 15, sieve drum, 16, stirring Paddle, 17, inlet tube, 18, waterfall tank, 19, liquid level, 20, filter screen, 21, pump, 22, circulation tube, 23, collection tube.
具体实施方式 detailed description
如图 1所示, 高效制备海藻酸钠 /壳聚糖缓释微囊的设备, 包括通过导流 管 11相互连接的可自动搅拌碾礦的乳化器装置和离心筛制粒机, 乳化器装置 包括乳化罐及安装于其上的乳化器电机 1和三通阀 9, 乳化罐分上中下三部 分, 上部为带有进料口 6的混匀池 2, 中部为碾礦器 3, 下部为设有出料口的 乳化池 5, 三通阀 9安装于出料口并分别连接有返回管 10、 导流管 11, 乳化 器电机 1的输出轴伸入乳化罐中,输出轴位于混匀池 2处设有混匀池搅拌桨 7, 输出轴位于碾礦器处设有与碾礦器内壁配合的带有螺旋槽的碾礦棒 4,输出轴 位于乳化池 5处连接有乳化池搅拌桨 8。 离心筛制粒机包括一个固化反应罐 14, 固化反应罐 14上部与导流管 11相连, 底部接有收集管 23, 罐内设有一 个侧壁开有复数个筛孔的筛桶 15, 固化反应罐 14顶部设有一个和筛桶 15连 通的斗状进料管 13, 筛桶 15安装在转轴上, 转轴穿过固化反应罐 14和外置 的调速电机 12连接。 离心筛制粒机的固化反应罐 14中环绕罐内壁设有一圈 起瀑槽 18, 起瀑槽 18高于筛孔所在工作面, 固化反应罐 14外接一个带抽液
泵 21的循环管 22, 循环管 22—端接入固化反应罐 14内连接起瀑槽 18, 另 一端接在固化反应罐 14底部;固化反应罐 14底部和循环管 22连接处设有过 滤筛网 20。 转轴上装有搅拌桨 16, 搅拌桨 16位于筛桶下方。 固化反应罐 14 为分体结构, 由可拆卸的顶盖和罐身上下对接而成。 筛桶 15和转轴之间为可 拆卸连接。 As shown in FIG. 1, an apparatus for efficiently preparing sodium alginate/chitosan sustained-release microcapsules, comprising an emulsifier device and a centrifugal sieve granulator which are automatically connected to each other by a draft tube 11 and an emulsifier device The invention comprises an emulsifying tank and an emulsifier motor 1 and a three-way valve 9 mounted thereon, the emulsifier tank is divided into upper and lower parts, the upper part is a mixing tank 2 with a feeding port 6, the middle part is a crusher 3, and the lower part For the emulsification tank 5 provided with the discharge port, the three-way valve 9 is installed at the discharge port and is respectively connected with the return pipe 10 and the draft tube 11, and the output shaft of the emulsifier motor 1 extends into the emulsification tank, and the output shaft is located at the mixing There is a mixing tank stirring paddle 7 at the leveling tank 2, and the output shaft is located at the miller with a spiral grooved grinding rod 4 matched with the inner wall of the mill, and the output shaft is located at the emulsification tank 5 and is connected with the emulsification tank. Stir the paddle 8. The centrifugal sieve granulator comprises a curing reaction tank 14, the upper part of the curing reaction tank 14 is connected with the draft tube 11, and the bottom is connected with a collecting tube 23, and the tank is provided with a sieve barrel 15 having a plurality of sieve holes on the side wall, and solidified. The top of the reaction tank 14 is provided with a bucket-shaped feed pipe 13 communicating with the sieve drum 15, and the sieve drum 15 is mounted on the rotating shaft, and the rotating shaft is connected through the curing reaction tank 14 and the external speed regulating motor 12. The curing reaction tank 14 of the centrifugal sieve granulator is provided with a circle of waterfall grooves 18 around the inner wall of the tank, the waterfall tank 18 is higher than the working surface of the screen hole, and the curing reaction tank 14 is connected with a pumping liquid. The circulation pipe 22 of the pump 21, the end of the circulation pipe 22 is connected to the curing reaction tank 14 and connected to the waterfall tank 18, and the other end is connected to the bottom of the curing reaction tank 14. The bottom of the curing reaction tank 14 and the circulation pipe 22 are provided with a filter screen. Web 20. A stirring paddle 16 is mounted on the rotating shaft, and the stirring paddle 16 is located below the sieve drum. The curing reaction tank 14 has a split structure and is formed by a detachable top cover and a can body. There is a detachable connection between the sieve drum 15 and the rotating shaft.
高效制备海藻酸钠 /壳聚糖缓释微囊的制备工艺: Preparation process of high-efficiency preparation of sodium alginate/chitosan sustained-release microcapsules:
实施例一 Embodiment 1
以制药用水配制下列溶液: Prepare the following solutions in pharmaceutical water:
A液: 质量百分含量为 1 .5%海藻酸钠溶液 +质量百分含量为 2%姜黄素; B液: 容积分数为 1 %的乙酸 +质量分数为 1 %的氯化钙 +质量分数为 0.5% 的壳聚糖溶液; Solution A: Mass percentage of 1.5% sodium alginate solution + mass percentage of 2% curcumin; Solution B: acetic acid with a volume fraction of 1% + calcium chloride with mass fraction of 1% + mass fraction a 0.5% chitosan solution;
三通阀 9转至状态 A1时, 将 A液经进料口 6加入乳化罐的上部的混匀 池 2, 开启乳化器电机 1, 转速为 1000r/min, 混匀池搅拌桨 7搅拌推动下进 入乳化罐的中部的碾礦器 3,经带螺旋槽的碾礦捧 4碾礦并推入乳化罐下部的 乳化池 5, 乳化池搅拌桨 8进一歩搅拌。 此时出料口处的三通阀 9转至状态 A2接通返回管 10,使 A液返回乳化罐的上部循环搅拌、碾礦,充分混悬 30min, 制得姜黄素海藻酸钠混悬液。 When the three-way valve 9 is turned to the state A1, the liquid A is added to the mixing tank 2 at the upper portion of the emulsifying tank through the feeding port 6, and the emulsifier motor 1 is turned on, the rotation speed is 1000r/min, and the mixing tank stirring paddle 7 is stirred and pushed. The pulverizer 3 entering the middle of the emulsification tank is crushed by the sifting tank with the spiral groove and pushed into the emulsification tank 5 at the lower part of the emulsification tank, and the emulsification tank stirring paddle 8 is stirred one by one. At this time, the three-way valve 9 at the discharge port is turned to the state A2 to turn on the return pipe 10, and the liquid A is returned to the upper portion of the emulsion tank to be stirred and crushed, and fully suspended for 30 minutes to prepare a curcumin sodium alginate suspension. .
将 B液经进液管 17加入离心筛制粒机的固化反应罐 14。随后,三通阀 9 转至状态 A4接通导流管 11, 制得的姜黄素海藻酸钠混悬液依次流入离心筛 制粒机的斗状进料管 13和筛桶 15。 开启抽液泵 21将固化反应罐 14内的 B 液经循环管 22抽至起瀑槽 18并溢出形成溶液幕。 开启调速电机 12, 转速为 400r/min, 将姜黄素海藻酸钠混悬液离心甩入固化反应罐 14内, 与 B液反应
生成含姜黄素海藻酸钠 /壳聚糖缓释微囊。 The liquid B is supplied to the solidification reaction tank 14 of the centrifugal sieve granulator through the inlet pipe 17. Subsequently, the three-way valve 9 is turned to the state A4 to turn on the draft tube 11, and the obtained curcumin sodium alginate suspension sequentially flows into the bucket-shaped feed tube 13 and the sieve barrel 15 of the centrifugal sieve granulator. The pumping pump 21 is turned on to pump the liquid B in the curing reaction tank 14 to the rising tank 18 through the circulation pipe 22 and overflow to form a solution curtain. Turn on the speed regulating motor 12, the rotation speed is 400r/min, centrifuge the curcumin sodium alginate suspension into the curing reaction tank 14, and react with the B liquid. A curcumin-containing sodium alginate/chitosan sustained release microcapsule is produced.
整个生产过程中, 消耗的 B液可从进液管 17不断补充加入。微囊产物可 从收集管 23收集。收集的微囊产物置于 B液中继续固化 30min, 随后筛去溶 液, 水洗, 经 55°C鼓风干燥制成微囊成品。 该生产可连续工作无需停车。 如 需生产不同大小粒径的颗粒时只要调整电机转速或更换不同型号的筛桶的直 径及筛孔的孔径不同即可。 The B liquid consumed can be continuously replenished from the inlet pipe 17 throughout the production process. The microcapsule product can be collected from collection tube 23. The collected microcapsule product was placed in solution B for further 30 minutes, and then the solution was sieved, washed with water, and dried by blowing at 55 ° C to prepare a microcapsule product. The production can work continuously without parking. If it is necessary to produce particles of different sizes, simply adjust the motor speed or change the diameter of the different types of sieve drums and the aperture of the sieve holes.
实施例二 Embodiment 2
以制药用水配制下列溶液: Prepare the following solutions in pharmaceutical water:
A液: 质量百分含量为 1 .5%海藻酸钠溶液 +质量百分含量为 2%莪术油; B液: 容积分数为 1 %的乙酸 +质量分数为 1 %的氯化钙 +质量分数为 0.5% 的壳聚糖溶液。 Liquid A: mass percentage of 1.5% sodium alginate solution + mass percentage of 2% zedoary turmeric oil; liquid B: volume fraction of 1% acetic acid + mass fraction of 1% calcium chloride + mass fraction It is a 0.5% chitosan solution.
三通阀 9转至状态 A1时, 将 A液经进料口 6加入乳化罐的上部的混匀 池 2, 开启乳化器电机 1, 转速为 1000r/min, 混匀池搅拌桨 7搅拌推动下进 入乳化罐的中部的碾礦器 3,经带螺旋槽的碾礦捧 4碾礦并推入乳化罐下部的 乳化池 5, 乳化池搅拌桨 8进一歩搅拌。 此时出料口处的三通阀 9转至状态 A2接通返回管 10,使 A液返回乳化罐的上部循环搅拌、碾礦,充分混悬 30min, 制得莪术油海藻酸钠混悬液。 When the three-way valve 9 is turned to the state A1, the liquid A is added to the mixing tank 2 at the upper portion of the emulsifying tank through the feeding port 6, and the emulsifier motor 1 is turned on, the rotation speed is 1000r/min, and the mixing tank stirring paddle 7 is stirred and pushed. The pulverizer 3 entering the middle of the emulsification tank is crushed by the sifting tank with the spiral groove and pushed into the emulsification tank 5 at the lower part of the emulsification tank, and the emulsification tank stirring paddle 8 is stirred one by one. At this time, the three-way valve 9 at the discharge port is turned to the state A2 to be connected to the return pipe 10, and the liquid A is returned to the upper portion of the emulsion tank for circulation stirring and grinding, and fully suspended for 30 minutes to prepare a sorghum oil sodium alginate suspension. .
将 B液经进液管 17加入离心筛制粒机的固化反应罐 14。随后,三通阀 9 转至状态 A4接通导流管 11, 制得的莪术油海藻酸钠混悬液依次流入离心筛 制粒机的斗状进料管 13和筛桶 15。 开启抽液泵 21将固化反应罐 14内的 B 液经循环管 22抽至起瀑槽 18并溢出形成溶液幕。 开启调速电机 12, 转速为 400r/min, 将莪术油海藻酸钠混悬液离心甩入固化反应罐 14内, 与 B液反应
制得莪术油海藻酸钠 /壳聚糖缓释微囊。 The liquid B is supplied to the solidification reaction tank 14 of the centrifugal sieve granulator through the inlet pipe 17. Subsequently, the three-way valve 9 is turned to the state A4 to turn on the draft tube 11, and the prepared zedoary turmeric sodium alginate suspension sequentially flows into the bucket-shaped feed tube 13 and the sieve barrel 15 of the centrifugal sieve granulator. The pumping pump 21 is turned on to pump the liquid B in the curing reaction tank 14 to the rising tank 18 through the circulation pipe 22 and overflow to form a solution curtain. Turn on the speed regulating motor 12, the rotation speed is 400r/min, centrifuge the sorghum oil sodium alginate suspension into the curing reaction tank 14, and react with the B liquid. The sorghum oil sodium alginate/chitosan sustained release microcapsules were prepared.
整个生产过程中, 消耗的 B液可从进液管 17不断补充加入。微囊产物可 从收集管 23收集。收集的微囊产物置于 B液中继续固化 30min, 随后筛去溶 液, 水洗, 经 45°C鼓风干燥制成微囊成品。 该生产可连续工作无需停车。 如 需生产不同大小粒径的颗粒时只要调整电机转速或更换不同型号的筛桶的直 径及筛孔的孔径不同即可。 The B liquid consumed can be continuously replenished from the inlet pipe 17 throughout the production process. The microcapsule product can be collected from collection tube 23. The collected microcapsule product was placed in solution B for further 30 minutes, then the solution was sieved, washed with water, and dried at 45 ° C to form a microcapsule product. The production can work continuously without parking. If it is necessary to produce particles of different sizes, simply adjust the motor speed or change the diameter of the different types of sieve drums and the aperture of the sieve holes.
以上所述实施例, 仅是本发明的较佳实施例而已, 已经体现出本发明突 出的实质性特点和显著的进歩, 并非对本发明的结构作任何形式上的限制。 凡是依据本发明的技术实质对以上实施例所作的任何简单修改、 等同变化与 修饰, 均落入本发明的保护范围内。
The embodiments described above are merely preferred embodiments of the present invention, and the substantial features and significant advantages of the present invention have been disclosed, and are not intended to limit the structure of the present invention in any way. Any simple modifications, equivalent changes and modifications of the above embodiments in accordance with the technical spirit of the present invention fall within the scope of the present invention.
Claims
1、高效制备海藻酸钠 /壳聚糖缓释微囊的设备,其特征在于包括通过导流 管 (11 ) 相互连接的可自动搅拌碾礦的乳化器装置和离心筛制粒机, 所述的 乳化器装置包括乳化罐及安装于其上的乳化器电机(1 )和三通阀 (9), 所述 的乳化罐分上中下三部分, 上部为带有进料口 (6) 的混匀池 (2), 中部为碾 礦器(3), 下部为设有出料口的乳化池 (5), 所述的三通阀 (9) 安装于出料 口并分别连接有返回管 (10)、 导流管(11 ), 乳化器电机(1 ) 的输出轴伸入 乳化罐中, 输出轴位于混匀池 (2) 处设有混匀池搅拌桨(7), 输出轴位于碾 礦器处设有与碾礦器内壁配合的带有螺旋槽的碾礦棒 (4), 输出轴位于乳化 池 (5) 处连接有乳化池搅拌桨 (8)。 1. An apparatus for efficiently preparing sodium alginate/chitosan sustained-release microcapsules, characterized by comprising an emulsifier device and a centrifugal sieve granulator capable of automatically stirring and pulverizing and connecting through a draft tube (11), The emulsifier device comprises an emulsification tank and an emulsifier motor (1) and a three-way valve (9) mounted thereon, the emulsification tank is divided into three parts, the upper part is provided with a feed port (6) The mixing tank (2), the middle part is a crusher (3), and the lower part is an emulsion tank (5) having a discharge port, and the three-way valve (9) is installed at the discharge port and respectively connected with a return pipe (10), the draft tube (11), the output shaft of the emulsifier motor (1) extends into the emulsion tank, and the output shaft is located at the mixing tank (2) with a mixing tank stirring paddle (7), and the output shaft is located The mill has a grinding rod (4) with a spiral groove matched with the inner wall of the mill, and the output shaft is located at the emulsion tank (5) and is connected with an emulsion tank stirring paddle (8).
2、根据权利要求 1所述的高效制备海藻酸钠 /壳聚糖缓释微囊的设备,其 特征在于所述的离心筛制粒机包括一个固化反应罐 (14), 固化反应罐 (14) 上部与导流管(11 ) 相连, 底部接有收集管(23), 罐内设有一个侧壁开有复 数个筛孔的筛桶(15), 固化反应罐(14)顶部设有一个和筛桶(15)连通的 斗状进料管(13), 筛桶 (15)安装在转轴上, 转轴穿过固化反应罐(14)和 外置的调速电机 (12) 连接。 2. The apparatus for efficiently preparing sodium alginate/chitosan sustained release microcapsule according to claim 1, wherein said centrifugal sieve granulator comprises a curing reaction tank (14), and a curing reaction tank (14). The upper part is connected to the draft tube (11), and the bottom is connected with a collecting tube (23). The tank is provided with a sieve barrel (15) having a plurality of sieve holes on the side wall, and a curing reaction tank (14) is provided at the top of the reaction tank (14). A bucket-shaped feed pipe (13) communicating with the sieve drum (15), the sieve drum (15) is mounted on the rotating shaft, and the rotating shaft is connected through the curing reaction tank (14) and an external speed regulating motor (12).
3、根据权利要求 2所述的高效制备海藻酸钠 /壳聚糖缓释微囊的设备,其 特征在于所述的离心筛制粒机的固化反应罐 (14) 中环绕罐内壁设有一圈起 瀑槽(18), 起瀑槽(18)高于筛孔所在工作面, 固化反应罐(14)外接一个 带抽液泵 (21 ) 的循环管 (22), 循环管 (22) —端接入固化反应罐 (14) 内连接起瀑槽 (18), 另一端接在固化反应罐 (14) 底部; 固化反应罐 (14) 底部和循环管 (22) 连接处设有过滤筛网 (20)。 The apparatus for efficiently preparing sodium alginate/chitosan sustained-release microcapsule according to claim 2, characterized in that the curing reaction tank (14) of the centrifugal sieve granulator is provided with a circle around the inner wall of the tank. The waterfall trough (18), the waterfall trough (18) is higher than the working surface of the screen hole, and the curing reaction tank (14) is externally connected with a circulation pipe (22) with a liquid pump (21), and the circulation pipe (22) is end The curing reaction tank (14) is connected to the waterfall tank (18), and the other end is connected to the bottom of the curing reaction tank (14); the bottom of the curing reaction tank (14) and the circulation pipe (22) are provided with a filtering screen ( 20).
4、 根据权利要求 2或 3所述的高效制备海藻酸钠 /壳聚糖缓释微囊的设
备, 其特征在于所述的转轴上装有搅拌桨(16), 所述的搅拌桨(16)位于筛 桶下方。 4. The high-efficiency preparation of sodium alginate/chitosan sustained-release microcapsule according to claim 2 or The utility model is characterized in that the rotating shaft is provided with a stirring paddle (16), and the stirring paddle (16) is located below the screen barrel.
5、根据权利要求 4所述的高效制备海藻酸钠 /壳聚糖缓释微囊的设备,其 特征在于所述的固化反应罐 (14) 为分体结构, 由可拆卸的顶盖和罐身上下 对接而成。 The apparatus for efficiently preparing sodium alginate/chitosan sustained-release microcapsule according to claim 4, wherein said curing reaction tank (14) is a split structure, and a removable top cover and a can It is made up of the body and the butt.
6、根据权利要求 4所述的高效制备海藻酸钠 /壳聚糖缓释微囊的设备,其 特征在于所述的筛桶 (15) 和转轴之间为可拆卸连接。 The apparatus for efficiently producing sodium alginate/chitosan sustained release microcapsule according to claim 4, wherein the sieve drum (15) and the rotating shaft are detachably connected.
7、高效制备海藻酸钠 /壳聚糖缓释微囊的制备工艺,其特征在于利用权利 要求 1 -7任一所述的高效制备海藻酸钠 /壳聚糖缓释微囊的设备并采用以下歩 骤: 7. A process for efficiently preparing a sodium alginate/chitosan sustained-release microcapsule, which is characterized by using the device for efficiently preparing sodium alginate/chitosan sustained-release microcapsule according to any one of claims 1 to 7 and adopting The following steps:
第一歩, 乳化歩骤: 以海藻酸钠溶液为分散剂, 将脂溶性或水溶性药物 分散溶解于其中, 经自动搅拌碾礦乳化裝置制成含药乳化小滴或混悬液; 第二歩, 制粒歩骤: 令第一歩的制备液流入离心筛制粒机, 经离心甩出 并和氯化钙壳聚糖溶液结合反应, 生成含药海藻酸钠 /壳聚糖缓释微囊; First 歩, emulsification step: dissolving a fat-soluble or water-soluble drug in a sodium alginate solution as a dispersing agent, and preparing a medicated emulsified droplet or suspension by an automatic stirring ore emulsification device;歩, granulation process: The first mash preparation solution is poured into a centrifugal sieve granulator, which is centrifuged and combined with a calcium chloride chitosan solution to form a drug-containing sodium alginate/chitosan sustained-release micro Sac
第三歩, 整理歩骤: 固化、 收集、 水洗第二歩所得制备物, 以小于等于 55°C的风干燥。 Third, finishing step: The preparation obtained by solidifying, collecting, and washing the second crucible is dried with air of 55 ° C or less.
8、 根据权利要求 7所述的高效制备海藻酸钠 /壳聚糖缓释微囊的制备工 艺, 其特征在于还包括以下歩骤: 8. The process for efficiently preparing a sodium alginate/chitosan sustained release microcapsule according to claim 7, which further comprises the following steps:
以制药用水配制下列溶液: Prepare the following solutions in pharmaceutical water:
A液: 质量百分含量为 1 .5%海藻酸钠溶液 +质量百分含量为 2%药物; B液: 容积分数为 1 %的乙酸 +质量分数为 1 %的氯化钙 +质量分数为 0.5% 的壳聚糖溶液。
Liquid A: mass percentage of 1.5% sodium alginate solution + mass percentage of 2% drug; liquid B: volume fraction of 1% acetic acid + mass fraction of 1% calcium chloride + mass fraction 0.5% chitosan solution.
9、 根据权利要求 8所述的高效制备海藻酸钠 /壳聚糖缓释微囊的制备工 艺, 其特征在于将 A液加入乳化器后, 通过循环搅拌和碾礦使其充分混悬、 乳化, 乳化电机的转速为 500r/min-4000r/min, 乳化时间为 30min-60min。 9. The process for efficiently preparing sodium alginate/chitosan sustained-release microcapsule according to claim 8, characterized in that after adding the liquid A to the emulsifier, it is fully suspended and emulsified by circulating stirring and milling. The speed of the emulsified motor is 500r/min-4000r/min, and the emulsification time is 30min-60min.
10、 根据权利要求 9所述的高效制备海藻酸钠 /壳聚糖缓释微囊的制备工 艺, 其特征在于将 B液加入离心筛制粒机的固化反应罐, 所述的含药已乳化 的 A液经导流管进入离心筛制粒机的筛桶, 经离心甩出至固化反应罐内, 与 B液结合反应生成含药海藻酸钠 /壳聚糖缓释微囊; 离心筛制粒机的调速电机 的转速为 300r/min-1000r/min。
10. The process for efficiently preparing a sodium alginate/chitosan sustained-release microcapsule according to claim 9, wherein the liquid B is added to a curing reaction tank of a centrifugal sieve granulator, and the drug-containing emulsified The liquid A enters the sieve barrel of the centrifugal sieve granulator through the diversion tube, is centrifugally extracted into the curing reaction tank, and combines with the liquid B to form a drug-containing sodium alginate/chitosan sustained-release microcapsule; The speed of the speed regulating motor of the machine is 300r/min-1000r/min.
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WO2015091885A2 (en) | 2013-12-20 | 2015-06-25 | Fresenius Kabi Deutschland Gmbh | Microcapsules with polymeric coating comprising a lipid and an active agent |
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