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CN102407028A - Method for preparing polymer or drug particle by continuous supercritical fluid rapid expansion technology - Google Patents

Method for preparing polymer or drug particle by continuous supercritical fluid rapid expansion technology Download PDF

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CN102407028A
CN102407028A CN2011102699464A CN201110269946A CN102407028A CN 102407028 A CN102407028 A CN 102407028A CN 2011102699464 A CN2011102699464 A CN 2011102699464A CN 201110269946 A CN201110269946 A CN 201110269946A CN 102407028 A CN102407028 A CN 102407028A
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fluid
carbon dioxide
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supercritical carbon
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陈爱政
王士斌
赵政
李翼
刘源岗
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Huaqiao University
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Abstract

本发明公开了一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,包括如下步骤:先将聚合物或药物溶解于一种或多种有机溶剂中形成有机溶液,经高压泵泵入超临界二氧化碳流体中,使有机溶液与超临界二氧化碳流体混合均匀形成混合流体,然后将有机溶剂和超临界二氧化碳快速膨胀导致溶解能力大大下降,从而使溶质过饱和沉淀析出形成颗粒。本发明克服了目前抗溶剂法和快速膨胀法难于对在超临界二氧化碳流体部分溶解的溶质进行造粒的缺点,可成功地进行连续造粒。

The invention discloses a method for preparing polymer or drug granules by continuous supercritical fluid rapid expansion technology, which comprises the following steps: first dissolving the polymer or drug in one or more organic solvents to form an organic solution, and passing through a high-pressure pump Pump into the supercritical carbon dioxide fluid, so that the organic solution and supercritical carbon dioxide fluid are mixed uniformly to form a mixed fluid, and then the organic solvent and supercritical carbon dioxide are rapidly expanded, resulting in a greatly reduced solubility, so that the solute is supersaturated and precipitated to form particles. The invention overcomes the disadvantage that the current anti-solvent method and rapid expansion method are difficult to granulate the solute partially dissolved in the supercritical carbon dioxide fluid, and can successfully carry out continuous granulation.

Description

一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法A method for preparing polymer or drug particles by continuous supercritical fluid rapid expansion technology

技术领域 technical field

本发明涉及一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法。The invention relates to a method for preparing polymer or drug particles by continuous supercritical fluid rapid expansion technology.

背景技术 Background technique

超临界流体是指温度和压力均高于临界点的流体。目前研究较多的超临界流体是二氧化碳,超临界二氧化碳流体具有无毒、不可燃、相对便宜、溶解能力较高、可循环、临界点低等优点。由于超临界二氧化碳流体所具有的优良特性,使得超临界流体技术高分子科学、药学以及制备超细颗粒等领域得到了广泛的研究应用。目前,超临界二氧化碳流体技术在颗粒制备方面主要有两大类:一是以超临界二氧化碳流体为溶剂的超临界二氧化碳流体快速膨胀法,二是以超临界二氧化碳流体作为抗溶剂的超临界二氧化碳流体抗溶剂法。A supercritical fluid is a fluid whose temperature and pressure are above the critical point. At present, the most researched supercritical fluid is carbon dioxide. Supercritical carbon dioxide fluid has the advantages of non-toxic, non-flammable, relatively cheap, high dissolving capacity, recyclable, and low critical point. Due to the excellent characteristics of supercritical carbon dioxide fluid, supercritical fluid technology has been widely used in the fields of polymer science, pharmacy and preparation of ultrafine particles. At present, there are two main types of supercritical carbon dioxide fluid technology in the preparation of particles: one is the supercritical carbon dioxide fluid rapid expansion method using supercritical carbon dioxide fluid as a solvent, and the other is supercritical carbon dioxide fluid using supercritical carbon dioxide fluid as an antisolvent Anti-solvent method.

超临界二氧化碳流体快速膨胀法是利用超临界二氧化碳流体的溶解能力随压力变化这一特性,使溶有溶质的超临界二氧化碳溶液通过一喷嘴高速喷入沉淀设备内,超临界二氧化碳在沉淀器内迅速降压而膨胀成气态,其对溶质的溶解能力迅速降低,溶液迅速过饱和而结晶沉淀出溶质微粒。在超临界二氧化碳流体快速膨胀法中,需先将溶质溶解于超临界二氧化碳流体,然而由于大部分的聚合物和药物基本不溶于超临界二氧化碳流体,或溶解度较低,因此大大限制了超临界二氧化碳快速膨胀法在聚合物和药物颗粒制备方面的应用。此外,超临界二氧化碳流体快速膨胀法是间歇型操作模式,处理量少,无法连续式扩大生产而阻碍了其工业应用。The rapid expansion method of supercritical carbon dioxide fluid is to use the characteristic that the dissolving capacity of supercritical carbon dioxide fluid changes with pressure, so that the supercritical carbon dioxide solution dissolved in solute is sprayed into the sedimentation equipment at high speed through a nozzle, and the supercritical carbon dioxide is rapidly discharged in the precipitator. When the pressure is reduced and it expands into a gaseous state, its ability to dissolve solutes decreases rapidly, and the solution is rapidly supersaturated and crystallizes and precipitates solute particles. In the supercritical carbon dioxide fluid rapid expansion method, the solute needs to be dissolved in the supercritical carbon dioxide fluid first, but since most of the polymers and drugs are basically insoluble in the supercritical carbon dioxide fluid, or have low solubility, it greatly limits the ability of supercritical carbon dioxide Application of the rapid expansion method in the preparation of polymer and drug particles. In addition, the supercritical carbon dioxide fluid rapid expansion method is an intermittent operation mode, with a small processing capacity, and cannot continuously expand production, which hinders its industrial application.

当欲造粒的聚合物或药物不溶于超临界二氧化碳流体时,可选择一种能溶解超临界二氧化碳流体的溶剂溶解该物质。当作为抗溶剂的超临界二氧化碳流体与该溶液充分接触时,超临界二氧化碳流体迅速扩散到溶液中,溶液体积膨胀,密度下降、溶解能力下降,溶液过饱和而成核析出溶质微粒,这就是超临界二氧化碳流体抗溶剂法的基本原理。超临界二氧化碳抗溶剂法克服了超临界二氧化碳流体快速膨胀法的局限性,在该方法中,可将药物和/或聚合物溶解于一种或多种有机溶剂,然后经高压泵泵入超临界二氧化碳流体进行抗溶剂作用,药物和/或聚合物过饱和共沉淀析出,从而得到药物、聚合物颗粒或药物-聚合物复合颗粒。When the polymer or medicine to be granulated is insoluble in supercritical carbon dioxide fluid, a solvent capable of dissolving supercritical carbon dioxide fluid can be selected to dissolve the substance. When the supercritical carbon dioxide fluid as an anti-solvent is in full contact with the solution, the supercritical carbon dioxide fluid rapidly diffuses into the solution, the volume of the solution expands, the density decreases, the solubility decreases, and the solution is supersaturated to nucleate and precipitate solute particles. Fundamentals of the critical carbon dioxide fluid antisolvent method. The supercritical carbon dioxide anti-solvent method overcomes the limitations of the supercritical carbon dioxide fluid rapid expansion method. In this method, drugs and/or polymers can be dissolved in one or more organic solvents and then pumped into the supercritical fluid through a high-pressure pump. The carbon dioxide fluid is anti-solvent, and the drug and/or polymer are supersaturated and co-precipitated to obtain the drug, polymer particles or drug-polymer composite particles.

但是当使用超临界二氧化碳流体技术处理在超临界二氧化碳流体中部分溶解的聚合物或药物时,比如双亲性的聚乳酸-聚乙二醇-聚乳酸共聚物(PLA-PEG-PLA),如果采用抗溶剂法,当将共聚物的有机溶液喷入超临界二氧化碳流体时,有机溶剂将起到共溶剂的作用从而大大提高了共聚物在超临界二氧化碳流体中的溶解度,使得共聚物溶解或以小液滴的形式分散在超临界二氧化碳流体中,溶质也随着二氧化碳流体由放气阀流失,在高压釜内没有因抗溶剂作用而过饱和沉淀析出,因此得不到样品;而若采用快速膨胀法,共聚物在超临界二氧化碳流体中较低的溶解度以及操作的间歇性都大大限制了该方法对此类共聚物的应用。However, when using supercritical carbon dioxide fluid technology to process polymers or drugs partially dissolved in supercritical carbon dioxide fluid, such as amphiphilic polylactic acid-polyethylene glycol-polylactic acid copolymer (PLA-PEG-PLA), if using Anti-solvent method, when the organic solution of the copolymer is sprayed into the supercritical carbon dioxide fluid, the organic solvent will act as a co-solvent, thereby greatly improving the solubility of the copolymer in the supercritical carbon dioxide fluid, so that the copolymer dissolves or dissolves in a small amount The form of liquid droplets is dispersed in the supercritical carbon dioxide fluid, and the solute is also lost through the vent valve along with the carbon dioxide fluid. There is no supersaturated precipitation in the autoclave due to the effect of anti-solvent, so no sample can be obtained; and if rapid expansion is used However, the low solubility of copolymers in supercritical carbon dioxide fluid and the intermittent operation greatly limit the application of this method to such copolymers.

因此,目前的超临界二氧化碳流体技术在处理超临界二氧化碳流体中部分溶解的溶质时,均不能较好地进行造粒。Therefore, the current supercritical carbon dioxide fluid technology cannot perform granulation well when dealing with partially dissolved solutes in the supercritical carbon dioxide fluid.

发明内容 Contents of the invention

本发明的目的在于提供了一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法;本发明克服了目前抗溶剂法和快速膨胀法难于对在超临界二氧化碳流体部分溶解的溶质进行造粒的缺点,可成功地进行连续造粒。The object of the present invention is to provide a kind of method that continuous type supercritical fluid rapid expansion technology prepares polymer or medicine granule; Disadvantages of granulation, continuous granulation can be successfully performed.

为了达到上述目的,本发明的技术方案是:In order to achieve the above object, technical scheme of the present invention is:

一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,包括如下步骤:先将聚合物或药物溶解于一种或多种有机溶剂中形成有机溶液,经高压泵泵入超临界二氧化碳流体中,使有机溶液与超临界二氧化碳流体混合均匀形成混合流体,然后将有机溶剂和超临界二氧化碳快速膨胀导致溶解能力大大下降,从而使溶质过饱和沉淀析出形成颗粒。A method for preparing polymer or drug particles by continuous supercritical fluid rapid expansion technology, comprising the following steps: first dissolving the polymer or drug in one or more organic solvents to form an organic solution, and pumping it into the supercritical fluid through a high-pressure pump. In the carbon dioxide fluid, the organic solution is uniformly mixed with the supercritical carbon dioxide fluid to form a mixed fluid, and then the organic solvent and supercritical carbon dioxide are rapidly expanded, resulting in a great decrease in the dissolving capacity, so that the solute is supersaturated and precipitated to form particles.

所述的溶质采用在超临界二氧化碳流体中部分溶解的溶质、在超临界二氧化碳流体中完全溶解的溶质以及溶解度较高的溶质中的一种。The solute adopts one of the solutes partially dissolved in the supercritical carbon dioxide fluid, the solutes completely dissolved in the supercritical carbon dioxide fluid, and the solutes with higher solubility.

所述的有机溶剂为能与超临界二氧化碳流体互相混溶的有机溶剂。The organic solvent is an organic solvent that is miscible with the supercritical carbon dioxide fluid.

所述的有机溶剂为非极性或低极性且沸点较低的有机溶剂。The organic solvent is a non-polar or low-polar organic solvent with a lower boiling point.

所述的有机溶剂为二氯甲烷或丙酮。Described organic solvent is dichloromethane or acetone.

所述的有机溶液与超临界二氧化碳流体混合均匀形成混合流体后经喷嘴喷入常压釜内使有机溶剂和超临界二氧化碳快速膨胀导致溶解能力大大下降。The organic solution and the supercritical carbon dioxide fluid are uniformly mixed to form a mixed fluid, which is then sprayed into the normal pressure kettle through a nozzle, so that the organic solvent and the supercritical carbon dioxide rapidly expand and the dissolving capacity is greatly reduced.

所述的有机溶液经高压泵连续地泵入到超临界二氧化碳流体中混合形成均匀的混合流体,同时连续地快速膨胀形成颗粒。The organic solution is continuously pumped into the supercritical carbon dioxide fluid through a high-pressure pump and mixed to form a uniform mixed fluid, and at the same time continuously expands rapidly to form particles.

所述的混合流体以二氧化碳作为雾化剂或高压釜内其他物理分散方式的混合方法使有机溶液经高压泵连续地泵入到超临界二氧化碳流体中混合形成均匀的混合流体。The mixed fluid uses carbon dioxide as an atomizer or other physical dispersion methods in the autoclave to continuously pump the organic solution into the supercritical carbon dioxide fluid through a high-pressure pump and mix to form a uniform mixed fluid.

所述的二氧化碳作为雾化剂或高压釜内其他物理分散方式是指超临界流体强制分散法、超声强化质量传递超临界抗溶剂法、高压釜内搅拌法中的一种。The use of carbon dioxide as an atomizing agent or other physical dispersion methods in the autoclave refers to one of the supercritical fluid forced dispersion method, ultrasonic enhanced mass transfer supercritical anti-solvent method, and stirring method in the autoclave.

本发明的有益效果为:本发明克服了目前抗溶剂法和快速膨胀法难于对在超临界二氧化碳流体部分溶解的溶质进行造粒的缺点,可成功地进行连续造粒。The beneficial effects of the present invention are: the present invention overcomes the disadvantage that the current anti-solvent method and rapid expansion method are difficult to granulate the solute partially dissolved in the supercritical carbon dioxide fluid, and can successfully carry out continuous granulation.

附图说明 Description of drawings

图1是本发明连续式超临界流体技术制备聚合物或药物颗粒的工艺装置图;(1钢瓶,2制冷系统,3高压柱塞泵,4高压釜,5快速膨胀喷嘴,6有机溶液,7高压泵,8同轴喷嘴,9常压釜,10过滤器,11热交换器,12空气浴,13热交换器)Fig. 1 is the technological device figure that continuous type supercritical fluid technique of the present invention prepares polymkeric substance or drug granule; (1 steel cylinder, 2 refrigeration systems, 3 high pressure plunger pumps, 4 autoclaves, 5 rapid expansion nozzles, 6 organic solutions, 7 High pressure pump, 8 coaxial nozzles, 9 normal pressure kettle, 10 filter, 11 heat exchanger, 12 air bath, 13 heat exchanger)

图2是本发明实施例1中PLA-PEG-PLA微粒扫描电镜形貌图;Fig. 2 is the scanning electron microscope topography figure of PLA-PEG-PLA particle in the embodiment 1 of the present invention;

图3是本发明实施例1中PLA-PEG-PLA微粒粒度分布图。(Number:数量,Particle diameter:颗粒直径)Fig. 3 is a particle size distribution diagram of PLA-PEG-PLA particles in Example 1 of the present invention. (Number: quantity, Particle diameter: particle diameter)

具体实施方式 Detailed ways

实施例1Example 1

将聚乳酸-聚乙二醇-聚乳酸三嵌段共聚物(PLA-PEG-PLA)溶于有机溶剂二氯甲烷中,得到1.0%(wt/v)的溶液备用。Polylactic acid-polyethylene glycol-polylactic acid triblock copolymer (PLA-PEG-PLA) was dissolved in the organic solvent methylene chloride to obtain a 1.0% (wt/v) solution for future use.

图1是本实施例连续式超临界流体技术制备聚合物或药物颗粒的工艺装置图,该装置结合了超临界流体强制分散溶液过程和超临界流体快速膨胀过程,主要包括二氧化碳输送系统、有机溶液输送系统、二氧化碳与有机溶液同轴喷嘴、高压釜、常压釜、快速膨胀喷嘴部件。Figure 1 is a diagram of the process device for preparing polymer or drug particles by continuous supercritical fluid technology in this embodiment. The device combines the supercritical fluid forced dispersion process and supercritical fluid rapid expansion process, mainly including carbon dioxide delivery system, organic solution Conveyor systems, coaxial nozzles for carbon dioxide and organic solutions, autoclaves, autoclaves, rapid expansion nozzle components.

钢瓶1中的二氧化碳经制冷系统2液化后,由高压柱塞泵3加压,再由管路中的恒温水浴升温后,泵入高压釜4中,待高压釜4内达到要求的压力,维持二氧化碳泵入速率,开启快速膨胀喷嘴5以一定速率喷射,并调节高压釜外部干燥箱及管路水浴温度,以保持釜内压力、温度恒定。系统压力、温度稳定后,超临界二氧化碳通过高压釜4顶部同轴二流式喷嘴外侧通道,将1.0%(wt/v)的PLA-PEG-PLA二氯甲烷溶液6通过高压泵7经喷嘴8内侧通道,同时泵入高压釜4。系统压力为12MPa、温度为306K、二氧化碳流速为25NL/h,高压泵的流速为1.0ml/min。有机溶液泵入高压釜4形成混合流体后经另一个快速膨胀喷嘴5喷入常压釜9,PLA-PEG-PLA过饱和沉淀析出形成颗粒。PLA-PEG-PLA有机溶液输送结束后,维持压力及温度不变,继续通入二氧化碳30分钟以保持快速膨胀过程的条件稳定,待高压釜4内压力降为常压时,在常压釜9内收集产品。After the carbon dioxide in the steel cylinder 1 is liquefied by the refrigeration system 2, it is pressurized by the high-pressure plunger pump 3, and then pumped into the autoclave 4 after being heated up by the constant temperature water bath in the pipeline. The rate of carbon dioxide pumping, the rapid expansion nozzle 5 is opened to spray at a certain rate, and the temperature of the external drying box and pipeline water bath of the autoclave is adjusted to keep the pressure and temperature inside the autoclave constant. After the system pressure and temperature are stabilized, the supercritical carbon dioxide passes through the outer channel of the coaxial two-flow nozzle at the top of the autoclave 4, and the PLA-PEG-PLA methylene chloride solution 6 of 1.0% (wt/v) passes through the high-pressure pump 7 through the inner side of the nozzle 8 channel while pumping into the autoclave 4. The system pressure is 12MPa, the temperature is 306K, the flow rate of carbon dioxide is 25NL/h, and the flow rate of the high pressure pump is 1.0ml/min. The organic solution is pumped into the autoclave 4 to form a mixed fluid, and then sprayed into the normal pressure autoclave 9 through another rapid expansion nozzle 5, and PLA-PEG-PLA is supersaturated and precipitated to form particles. After the delivery of the PLA-PEG-PLA organic solution, keep the pressure and temperature constant, and continue to feed carbon dioxide for 30 minutes to keep the conditions of the rapid expansion process stable. Collect products.

图2、图3分别为本实施例常压釜内收集到的PLA-PEG-PLA微粒的扫描电镜形貌图和粒度分布图,微粒主要呈球形,平均粒径2.2微米,分布范围较窄。实验结果表明,利用该连续式超临界二氧化碳流体快速膨胀技术可成功地进行制备在超临界二氧化碳流体部分溶解的溶质的颗粒,克服了抗溶剂法和快速膨胀法的缺点,可成功地进行连续造粒。Figure 2 and Figure 3 are the scanning electron microscope topography and particle size distribution diagrams of the PLA-PEG-PLA particles collected in the atmospheric autoclave of this embodiment, respectively. The particles are mainly spherical, with an average particle size of 2.2 microns and a narrow distribution range. The experimental results show that the rapid expansion technology of continuous supercritical carbon dioxide fluid can successfully prepare particles of solute partially dissolved in supercritical carbon dioxide fluid, which overcomes the shortcomings of the anti-solvent method and rapid expansion method, and can be successfully produced continuously. grain.

实施例2Example 2

将布洛芬溶于丙酮中形成1%(wt/v)的溶液,实验流程与实施例1相同,即可在常压釜9内获得布洛芬微细颗粒。Dissolving ibuprofen in acetone to form a 1% (wt/v) solution, the experimental process is the same as in Example 1, and ibuprofen fine particles can be obtained in the autoclave 9.

实施例3Example 3

将聚丙交酯乙交酯一聚乙二醇共聚物(PLGA-PEG)溶解于二氯甲烷中形成1%(wt/v)的溶液,实验流程与实施例1相同,即可在常压釜9内获得PLGA-PEG微细颗粒。Polylactide glycolide-polyethylene glycol copolymer (PLGA-PEG) is dissolved in methylene chloride to form a 1% (wt/v) solution, and the experimental process is the same as in Example 1, that is, the 9 to obtain PLGA-PEG fine particles.

Claims (10)

1.一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于包括如下步骤:先将聚合物或药物溶解于一种或多种有机溶剂中形成有机溶液,经高压泵泵入超临界二氧化碳流体中,使有机溶液与超临界二氧化碳流体混合均匀形成混合流体,然后将有机溶剂和超临界二氧化碳快速膨胀导致溶解能力大大下降,从而使溶质过饱和沉淀析出形成颗粒。1. A method for preparing polymer or drug granules by continuous supercritical fluid rapid expansion technology, characterized in that it comprises the steps of: first dissolving polymer or medicine in one or more organic solvents to form an organic solution; The pump is pumped into the supercritical carbon dioxide fluid, so that the organic solution and the supercritical carbon dioxide fluid are mixed uniformly to form a mixed fluid, and then the organic solvent and supercritical carbon dioxide are rapidly expanded, resulting in a great decrease in the dissolving capacity, so that the solute is supersaturated and precipitated to form particles. 2.如权利要求1所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的溶质采用在超临界二氧化碳流体中部分溶解的溶质、在超临界二氧化碳流体中完全溶解的溶质以及溶解度较高的溶质中的一种。2. a kind of continuous supercritical fluid rapid expansion technology as claimed in claim 1 prepares the method for polymkeric substance or drug particle, it is characterized in that: described solute adopts the solute that partially dissolves in supercritical carbon dioxide fluid, in supercritical carbon dioxide fluid One of the completely soluble solutes and the more soluble solutes in the critical carbon dioxide fluid. 3.如权利要求1所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的有机溶剂为能与超临界二氧化碳流体互相混溶的有机溶剂。3. a kind of continuous supercritical fluid rapid expansion technology prepares the method for polymkeric substance or drug granule as claimed in claim 1, it is characterized in that: described organic solvent is the organic solvent that can be miscible with supercritical carbon dioxide fluid . 4.如权利要求3所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的有机溶剂为非极性或低极性且沸点较低的有机溶剂。4. a kind of continuous supercritical fluid fast expansion technique as claimed in claim 3 prepares the method for polymkeric substance or medicine granule, it is characterized in that: described organic solvent is nonpolar or low polarity and boiling point is lower Organic solvents. 5.如权利要求4所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的有机溶剂为二氯甲烷或丙酮。5. A method for preparing polymers or drug particles by continuous supercritical fluid rapid expansion technology according to claim 4, characterized in that: the organic solvent is dichloromethane or acetone. 6.如权利要求1所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的有机溶液与超临界二氧化碳流体混合均匀形成混合流体后经喷嘴喷入常压釜内使有机溶剂和超临界二氧化碳快速膨胀导致溶解能力大大下降。6. A kind of continuous supercritical fluid rapid expansion technology as claimed in claim 1 prepares the method for polymer or drug granule, is characterized in that: described organic solution and supercritical carbon dioxide fluid mix uniformly to form mixed fluid after nozzle Spraying into the autoclave makes the organic solvent and supercritical carbon dioxide expand rapidly, resulting in a great decrease in dissolving capacity. 7.如权利要求6所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的混合流体以气体或液态流体的形式经喷嘴喷入常压釜内。7. A kind of continuous supercritical fluid rapid expansion technology as claimed in claim 6 prepares the method for polymkeric substance or drug particle, it is characterized in that: described mixed fluid is sprayed into normal pressure through nozzle in the form of gas or liquid fluid Inside the cauldron. 8.如权利要求1所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的有机溶液经高压泵连续地泵入到超临界二氧化碳流体中混合形成均匀的混合流体,同时连续地快速膨胀形成颗粒。8. a kind of continuous supercritical fluid rapid expansion technology as claimed in claim 1 prepares the method for polymkeric substance or drug particle, it is characterized in that: described organic solution is continuously pumped into supercritical carbon dioxide fluid through high-pressure pump Mixing forms a homogeneous mixed fluid while continuous rapid expansion forms particles. 9.如权利要求8所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的混合流体以二氧化碳作为雾化剂或高压釜内其他物理分散方式的混合方法使有机溶液经高压泵连续地泵入到超临界二氧化碳流体中混合形成均匀的混合流体。9. A kind of continuous supercritical fluid rapid expansion technology as claimed in claim 8 prepares the method for polymkeric substance or medicine granule, it is characterized in that: described mixed fluid uses carbon dioxide as atomizer or other physical dispersion in autoclave The mixing method of the method makes the organic solution continuously pumped into the supercritical carbon dioxide fluid through a high-pressure pump and mixed to form a uniform mixed fluid. 10.如权利要求9所述的一种连续式超临界流体快速膨胀技术制备聚合物或药物颗粒的方法,其特征在于:所述的二氧化碳作为雾化剂或高压釜内其他物理分散方式是指超临界流体强制分散法、超声强化质量传递超临界抗溶剂法、高压釜内搅拌法中的一种。10. A kind of continuous supercritical fluid rapid expansion technology as claimed in claim 9 prepares the method for polymer or drug particle, it is characterized in that: described carbon dioxide refers to as atomizing agent or other physical dispersion modes in the autoclave It is one of supercritical fluid forced dispersion method, ultrasonic enhanced mass transfer supercritical antisolvent method, and stirring method in autoclave.
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CN105769814A (en) * 2016-04-25 2016-07-20 北京化工大学常州先进材料研究院 Method for preparing pharmaceutical adjuvant Eudragit E100 microparticles
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