WO2024119376A1 - 一种注射用阿哌沙班长效微球及其制备方法 - Google Patents
一种注射用阿哌沙班长效微球及其制备方法 Download PDFInfo
- Publication number
- WO2024119376A1 WO2024119376A1 PCT/CN2022/136980 CN2022136980W WO2024119376A1 WO 2024119376 A1 WO2024119376 A1 WO 2024119376A1 CN 2022136980 W CN2022136980 W CN 2022136980W WO 2024119376 A1 WO2024119376 A1 WO 2024119376A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- apixaban
- microspheres
- acting
- long
- suspension
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D487/00—Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00
- C07D487/02—Heterocyclic compounds containing nitrogen atoms as the only ring hetero atoms in the condensed system, not provided for by groups C07D451/00 - C07D477/00 in which the condensed system contains two hetero rings
- C07D487/08—Bridged systems
Definitions
- the present invention relates to the field of pharmaceutical preparations, and in particular to a method for preparing long-acting apixaban microspheres for injection.
- Apixaban is a new generation of potent, reversible, direct and highly selective active site inhibitor of Xa, and its structure is shown in the figure below. It is used to treat osteoarthritis-related diseases, including the prevention of venous thromboembolism in patients after hip or knee replacement surgery; stroke prevention in patients with atrial fibrillation; and acute coronary syndrome. It mainly acts on factor Xa and binds to the active site of factor Xa in a highly complementary manner, inhibiting free and clot-bound FXa, thereby inhibiting thrombin activity. By inhibiting FXa, the generation of thrombin can be inhibited and thrombosis can be prevented.
- the oral preparations of Apixaban are mainly available in China and abroad. For hip replacement, it is recommended to take the drug for 35 days, for patients with atrial fibrillation, it is recommended to take the drug for 36 months, and for patients with acute coronary syndrome, it is recommended to take the drug for 3 months.
- the oral preparations of Apixaban must be taken on time every day, and the patient compliance is poor; its tablets also contain a large number of excipients, and some patients who are allergic to the excipients are prohibited from taking it.
- the main adverse reaction of Apixaban is bleeding. Ordinary oral rapid-release preparations can easily reach a higher required concentration, and the blood drug concentration fluctuates greatly, leading to serious adverse reactions.
- Carnitine is required as a carrier when long-chain fatty acids enter the mitochondria for oxidation and energy supply, and carnitine is produced in the liver and kidneys of the human body, so the side effects are relatively large, especially for patients with poor liver and kidney function. There are restrictions on use. In addition, it is difficult to ensure a high encapsulation rate and drug loading of microspheres using the traditional O/W emulsification method, and there is a large burst release phenomenon, causing adverse reactions and bleeding.
- the present invention does not use unconventional fatty acids or lipid materials, but adopts water-in-oil-in-solid (S/O/W) technology to prepare an apixaban microsphere for injection.
- the preparation method is simple, significantly improves the encapsulation rate and drug loading, and can reduce burst release, further reducing adverse reactions and bleeding.
- a method for preparing long-acting microspheres of apixaban for injection comprising the following steps: dispersing apixaban micropowder in a polymer solution to form a suspension; then adding the suspension dropwise to an aqueous phase solution, removing an organic solvent, and then washing to obtain long-acting microspheres of apixaban for injection.
- the suspension is added dropwise to an aqueous phase solution, then volatilized to remove the organic solvent, and solidified in water, then washed, and finally freeze-dried to obtain long-acting microspheres of apixaban for injection.
- the preparation method of the above-mentioned apixaban long-acting microspheres for injection includes the following steps.
- the polymer is dissolved in an organic solvent to obtain a polymer solution.
- the apixaban micropowder is uniformly dispersed in the polymer solution to form an S/O suspension.
- step (2) under stirring, the suspension of step (2) is added dropwise to the aqueous solution of step (3), and then the organic solvent is removed, and the microspheres are washed and collected, and freeze-dried to obtain long-acting apixaban microspheres for injection.
- the polymer is selected from one or more of polylactic acid-co-glycolic acid, polylactic acid, polylactic acid-polyethylene glycol and polycaprolactone, preferably polylactic acid-co-glycolic acid.
- the number average molecular weight of polylactic acid-co-glycolic acid is 5 kDa to 150 kDa; the molar ratio of lactide to glycolide is 85:15 to 50:50; preferably, the molecular weight of polylactic acid-co-glycolic acid is 12 kDa to 150 kDa; preferably, the molar ratio of lactide to glycolide is 50:50.
- the weight ratio of the apixaban micropowder to the polymer is 1:2-50, preferably 1:3-10.
- the additive is selected from one or more of polyvinyl alcohol, polysorbate 20, polysorbate 80, polyethylene glycol and sodium lauryl sulfate; preferably polyvinyl alcohol; the concentration of the additive is 0.001 g/mL to 0.05 g/mL; preferably 0.01 g/mL to 0.02 g/mL.
- the volume ratio of the suspension to the aqueous solution is 1:5-50, preferably 1:10-20, such as 1:15.
- the apixaban API is prepared as apixaban micropowder; the D50 particle size of the apixaban micropowder is 1-10 ⁇ m; preferably, the apixaban API is ground to prepare the apixaban micropowder; or the apixaban API is precipitated by a solvent to prepare the apixaban micropowder.
- the present invention discloses apixaban long-acting microspheres for injection prepared by the preparation method of the above-mentioned apixaban long-acting microspheres for injection and application of the apixaban long-acting microspheres for injection in preparing sustained-release drugs; further, application of the above-mentioned apixaban long-acting microspheres for injection in preparing drugs for treating diseases related to postoperative thrombosis prevention of osteoarthritis, drugs for preventing stroke in patients with atrial fibrillation, anti-thrombotic related drugs such as acute coronary syndrome.
- the present invention adopts a new S/O/W preparation method, which significantly improves the encapsulation rate and drug loading, and can reduce burst release, further reducing adverse reactions and bleeding phenomena; in particular, the present invention uses polymers, organic solvents, additives, water and apixaban micropowder as raw materials, and does not require other substances such as small molecule reagents, fatty acids, glycerides, etc., and the obtained apixaban long-acting microspheres have high encapsulation rate and drug loading, and excellent release performance.
- FIG1 is a scanning electron micrograph of the apixaban microspheres prepared in Example 2 of the invention.
- FIG. 2 is a scanning electron micrograph of the apixaban microspheres prepared in Example 6 of the invention.
- FIG3 is a scanning electron micrograph of the apixaban microspheres prepared in Example 7 of the invention.
- FIG. 4 is an in vitro release curve of the apixaban microspheres prepared in Example 1 and Example 2 at 37° C.
- FIG. 5 is an in vitro release curve of the apixaban microspheres prepared in Example 6 and Example 7 at 37° C.
- the present invention is further described below in conjunction with the examples and drawings.
- the raw materials used in the present invention are existing products, and the specific preparation operations and performance tests are conventional techniques.
- the apixaban bulk drug was ground in a mortar to obtain an apixaban micropowder with a D50 of 5 ⁇ m, which was used in other examples except Comparative Example 1 and Comparative Example 2.
- the dropwise addition of the S/O suspension is continuous dropwise addition below the liquid level; in a fume hood, the organic solvent is removed by a conventional stirring volatilization method; the microspheres are collected using a stainless steel sieve (apertures of 38.5 ⁇ m and 150 ⁇ m, respectively, between the two); freeze dryer model: FDU-2110.
- the ethyl acetate was evaporated, and the microspheres were collected and washed with water three times.
- the suspension was pre-frozen in a -80°C refrigerator for 10 h, and then freeze-dried for 48 h to obtain microsphere powder apixaban microspheres.
- the ethyl acetate was evaporated, and the microspheres were collected and washed with water three times.
- the suspension was pre-frozen in a -80°C refrigerator for 10 h, and then freeze-dried for 48 h to obtain microsphere powder apixaban microspheres.
- the S/O suspension was added dropwise to 40 mL of 0.01 g/mL polyvinyl alcohol aqueous solution, and the stirring was continued for 15 min (to evaporate the ethyl acetate), and then added to 250 mL of water and solidified for 10 min.
- the microspheres were collected and washed with water three times, pre-frozen in a -80°C refrigerator for 10 h, and freeze-dried for 48 h to obtain microsphere powder apixaban microspheres.
- the apixaban raw material was dissolved in dichloromethane to form an oil phase, which was then added dropwise to a 0.01 g/mL Tween 80 solution.
- the mixture was homogenized at 5000 rpm for 8 min, and then the organic solvent was evaporated under magnetic stirring (800 rpm) until the drug was precipitated.
- the mixture was centrifuged and the supernatant was discarded.
- the mixture was washed with water, and the precipitate was collected and pre-frozen in a -80°C refrigerator for 10 h, followed by freeze-drying for 48 h to obtain apixaban micropowder with a D50 of 5 ⁇ m.
- the apixaban bulk drug was ground in a mortar to obtain apixaban fine powder with a D50 of 30 ⁇ m.
- the formed emulsion was quickly added to 225 mL of water within 10 s, and magnetic stirring was carried out at 500 rpm for 5 hours.
- the microspheres were collected and washed with water three times, pre-frozen in a -80°C refrigerator for 10 hours, and freeze-dried for 48 hours to obtain microsphere powder apixaban microspheres.
- apixaban micropowder and 150 mg of polylactic acid-co-glycolic acid were weighed and dissolved in 3 mL of dichloromethane to form an oil phase.
- the oil phase was continuously added dropwise to 45 mL of 0.01 g/mL polyvinyl alcohol aqueous solution at 350 rpm for emulsification. Stirring was continued for 10 minutes to evaporate dichloromethane.
- the initially formed microspheres were added to 225 mL of water and solidified for 10 min. The microspheres were collected and washed with water three times, pre-frozen in a -80 °C refrigerator for 10 h, and freeze-dried for 48 h to obtain microsphere powder apixaban microspheres.
- microspheres prepared in Examples 1 to 10 and Comparative Examples 1 to 4 were dispersed in water, and the particle size of the microspheres was measured using a BT-2001 laser particle size distribution analyzer. The results are shown in Table 1.
- the particle size (particularly the median diameter) of the microspheres in the examples is below 90 mm, which is suitable for injection.
- the particle size of the microspheres in Comparative Example 1 is larger.
- the API reduced by the solvent precipitation method has good dispersibility and the particle size of the prepared microspheres is more suitable.
- the particle size of the microspheres prepared in Comparative Example 4 is larger, which is mainly related to the poor microsphere formability and dispersibility.
- Test Example 2 Microsphere morphology.
- the microspheres prepared in Examples 2, 6 and 7 were observed using a scanning electron microscope. The results are shown in Figures 1, 2 and 3, respectively. It can be seen that the apixaban microspheres are spherical or quasi-spherical with a smooth surface.
- Test Example 3 Drug loading and encapsulation efficiency of microspheres.
- Octadecylsilane bonded silica gel was used as a filler; 10 mmol/L ammonium acetate: acetonitrile (65:35) was used as a mobile phase, the flow rate was adjusted so that the main peak elution time was about 9 minutes, and the detection wavelength was 280 nm; 10 mg of apixaban reference substance was weighed, placed in a 50 mL volumetric flask, dissolved with the mobile phase and diluted to the scale, and shaken; 1 mL was measured, placed in a 10 mL volumetric flask, diluted to the scale with the mobile phase, and shaken to obtain the control solution; 10 mg of the microspheres prepared in Examples 1-10 were respectively taken, accurately weighed, placed in a 10 mL centrifuge tube, 1 mL of acetonitrile was added to completely dissolve, 7 mL of methanol was added to precipitate the polylactic acid-glycolic acid copolymer, and then centrifuge
- the encapsulation efficiency of the microspheres prepared in the examples is higher than that of the comparative examples. It can be seen that changing the molecular weight and concentration of PLGA50/50 has little effect on the encapsulation efficiency and drug loading of the microspheres. Although the type of PLGA has no obvious effect on the encapsulation efficiency of the microspheres, it has a greater effect on the later release of the microspheres. PLGA50/50 has a better release rate than PLGA75/25. Adding solidification in the process can improve the encapsulation efficiency of the microspheres to a certain extent, but the encapsulation efficiency of the microspheres decreases after the solidification time increases from 10 min to 120 min.
- the small D50 of the apixaban raw material drug has a great improvement on the encapsulation efficiency.
- the solvent precipitation method can also reduce the D50 of the apixaban raw material drug to 5 ⁇ m, compared with the grinding method, the microspheres formed by the raw material drug after the particle size is reduced have a larger particle size and the drug encapsulation effect is poor, and the encapsulation efficiency is about 84%.
- the results of comparative example 3 show that the apixaban microspheres prepared by the preparation method of the existing drug-loaded microspheres have a relatively poor encapsulation rate result, which does not reach the expected ideal effect, indicating that the preparation method of the existing drug-loaded microspheres is not suitable for the preparation of apixaban microspheres.
- the results of comparative example 4 show that the apixaban microspheres are prepared by the O/W method, and the "quicksand" phenomenon (drug precipitation) occurs during the preparation process, resulting in the microspheres being difficult to encapsulate, and the microsphere encapsulation rate is low, only about 37%.
- the present invention adopts the S/O/W method to prepare the apixaban microspheres, which can avoid the "quicksand” phenomenon in the drug, and the encapsulation rate is more than 85%, especially the present invention does not use auxiliary materials such as fatty acids, the composition is relatively simpler, the drug loading is higher, and it is safer.
- Example 6 From the release curve of Figure 5, the in vitro release of Example 6 is slower than that of Example 7, indicating that the polylactic acid-glycolic acid copolymer has a better in vitro release when the ratio is 50/50, and its release can last for 42 days or longer.
- This is applicable to the prevention of thrombosis after osteoarthritis surgery, the prevention of stroke in patients with atrial fibrillation, and the treatment of anti-thrombotic related diseases such as acute coronary syndrome.
- the present invention adopts the S/W/O method combined with the grinding method to control the particle size of the raw material drug, which can obtain a better encapsulation efficiency and drug loading, especially the release performance of the apixaban microspheres is very good.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Medicinal Preparation (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
一种注射用阿哌沙班长效微球及其制备方法,先将可降解聚合物溶解于有机溶剂中,得到聚合物溶液;再将阿哌沙班微粉)均匀分散在聚合物溶液中,形成油包固(S/O)混悬液:在搅拌条件下,将S/O混悬液滴加到水相中,去除混悬液中的有机溶剂并固化,洗涤并收集微球,冷冻干燥,即得微球成品。其中所述有机溶剂选自乙酸乙酯、二氯甲烷、甲醇和二甲基亚砜等;所述水相中含有添加剂,所述添加剂的浓度为0.001~0.05 g/mL。阿哌沙班微球制备工艺简单,粒径适宜,载药量高,突释小,具有明显的缓释作用,可用于血栓的预防,并降低出血风险。
Description
本发明涉及药物制剂领域,具体涉及一种注射用阿哌沙班长效微球的制备方法。
阿哌沙班是新一代Xa强效、可逆、直接且高度选择性的活性部位抑制剂,其结构如下图所示。用于治疗骨关节炎相关的疾病,包括预防髋关节或膝关节置换术后患者发生的静脉血栓栓塞症;心房颤动患者的卒中预防;用于急性冠脉综合征。它主要作用于Xa 因子,与Xa 因子活性位点之间以高度互补的方式结合,可以抑制游离以及与血凝块结合的 FXa,并由此抑制凝血酶活性。通过抑制 FXa,可以抑制凝血酶的产生、预防血栓形成。
。
目前国内外上市的主要是阿哌沙班的口服制剂,针对髋关节置换建议给药35天,针对心房颤动患者建议连续给药36个月,针对急性冠脉综合征建议连续给药3个月,然而阿哌沙班口服制剂必须每天按时服药,患者依从性差;其片剂中也含有较多的辅料成份,一些对辅料成份过敏的患者是禁用的。同时阿哌沙班主要的不良反应是出血现象,普通的口服速释制剂容易达到较高需要浓度,且血药浓度波动较大,导致严重的不良反应。因此,为了提高患者的顺应性,降低出血风险,扩大患者应用范围,研制阿哌沙班长效微球具有重要意义。现有技术关于阿哌沙班长效微球的报道很少,仅见的一种技术方案以卤素有机溶剂为溶剂,将脂肪酸或甘油三酯加入分散相,使用乳化溶剂挥发法和微流控法制备微球,其处方中使用了辅料脂肪酸(C12-C18)或甘油三酯抑制药物结晶和形成聚合物‑阿哌沙班沉淀物,其中长链脂肪酸进入线粒体氧化供能时需要肉毒碱作为载体,而肉毒碱在人体的肝脏和肾中产生,所以副作用偏大,尤其对于肝肾功能不良的患者存在使用限制。另外,采用传统的O/W乳化法很难保证微球的高包封率和载药量,且具有较大的突释现象,引起不良反应和出血现象。
为解决上述技术问题,本发明中未使用非常规脂肪酸或脂类材料,采用水包油包固(S/O/W)技术,制备得到一种注射用的阿哌沙班微球,制备方法简单,显著提高了包封率和载药量,且能降低突释,进一步降低不良反应和出血现象。
本发明是通过以下技术方案实现的:一种注射用阿哌沙班长效微球的制备方法,包括以下步骤:将阿哌沙班微粉分散在聚合物溶液中,形成混悬液;然后将混悬液滴加到水相溶液中,再去除有机溶剂,然后洗涤,得到注射用阿哌沙班长效微球。优选的,将混悬液滴加到水相溶液中,再挥发去除有机溶剂,并在水中固化,然后洗涤,最后冷冻干燥,得到注射用阿哌沙班长效微球。
具体的,上述注射用阿哌沙班长效微球的制备方法包括以下步骤。
(1)先将聚合物溶解于有机溶剂中,得到聚合物溶液。
(2)将阿哌沙班微粉均匀分散在聚合物溶液中,形成S/O混悬液。
(3)将添加剂溶于水中,得到水相溶液。
(4)在搅拌条件下,将步骤(2)的混悬液滴加到步骤(3) 的水相溶液中,然后去除有机溶剂,再洗涤并收集微球,冷冻干燥,即得注射用阿哌沙班长效微球。
本发明中,所述聚合物选自聚乳酸-羟基乙酸共聚物、聚乳酸、聚乳酸-聚乙二醇和聚己内酯中的一种或几种,优选聚乳酸-羟基乙酸共聚物。优选的,聚乳酸-羟基乙酸共聚物的数均分子量为5 kDa~150
kDa;丙交脂与乙交酯的摩尔比为85∶15~50∶50;优选聚乳酸-羟基乙酸共聚物分子量为12 kDa~150 kDa;优选丙交脂与乙交酯的摩尔比为50∶50。
本发明中,所述阿哌沙班微粉与聚合物的重量比为1∶2~50,优选1∶3~10。
本发明中,所述添加剂选自聚乙烯醇、聚山梨酯20、聚山梨酯80、聚乙二醇和十二烷基硫酸钠的一种或几种;优选聚乙烯醇;添加剂的浓度为0.001 g/mL~0.05 g/mL;优选0.01 g/mL~0.02 g/mL。
本发明中,所述混悬液与水相溶液的体积比为1∶5~50,优选1∶10~20,比如1∶15。
本发明中,阿哌沙班原料药制备为阿哌沙班微粉;阿哌沙班微粉的D50粒径为1~10 μm;优选的,将阿哌沙班原料药研磨,制备为阿哌沙班微粉;或者将阿哌沙班原料药经过溶剂析出,制备为阿哌沙班微粉。
本发明公开了上述注射用阿哌沙班长效微球的制备方法制备的注射用阿哌沙班长效微球以及所述注射用阿哌沙班长效微球在制备缓释药物中的应用;进一步的,上述注射用阿哌沙班长效微球在制备治疗骨关节炎术后血栓预防相关疾病的药物、心房颤动患者的卒中预防药物、急性冠脉综合征等抗血栓相关药物中的应用。
本发明的有益效果是:本发明采用了新S/O/W制备法,显著提高了包封率和载药量,且能降低突释,进一步降低不良反应和出血现象;尤其是,本发明以聚合物、有机溶剂、添加剂、水与阿哌沙班微粉为原料,无需其他物质比如无需小分子试剂、无需脂肪酸、甘油酯等,得到的阿哌沙班长效微球包封率和载药量高,且释放性能优异。
上述说明仅是本发明技术方案的的概述,为了能够更清楚了解本发明的技术手段,并可依照说明书的内容予以实施,以下以本发明的较佳实施例并配合附图详细说明如后。
图1为发明实施例2制备的阿哌沙班微球扫描电镜图。
图2为发明实施例6制备的阿哌沙班微球扫描电镜图。
图3为发明实施例7制备的阿哌沙班微球扫描电镜图。
图4为实施例1和实施例2制备的阿哌沙班微球的37℃体外释放度曲线。
图5为实施例6和实施例7制备的阿哌沙班微球的37℃体外释放度曲线。
以下结合实施例及附图对本发明进一步说明。本发明采用的原料为现有产品,具体制备操作以及性能测试为常规技术。将阿哌沙班原料药在研钵内研磨,得到D50为5 μm的阿哌沙班微粉,用于除了对比例1、对比例2之外的其他例子。实施例中,S/O混悬液的滴加为液面以下连续滴加;在通风橱内,采用常规搅拌挥发法去除有机溶剂;利用不锈钢筛(孔径分别为38.5 μm和150 μm,取两者之间)收集微球;冷冻干燥机型号:FDU-2110。
实施例1。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL的聚乙烯醇水溶液中,继续搅拌17 min(挥发乙酸乙酯),然后加入225
mL水中,固化10 min,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例2。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=60
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL的聚乙烯醇水溶液中,继续搅拌17 min(挥发乙酸乙酯),然后加入225
mL水中固化10 min,收集微球并用水洗涤3次,混悬放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例3。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=12
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01g/mL聚乙烯醇水溶液中,继续搅拌17 min(挥发乙酸乙酯),然后加入225
mL水中,固化10 min,收集微球并用水洗涤3次,混悬放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例4。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于5 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL的聚乙烯醇水溶液中,继续搅拌17 min(挥发乙酸乙酯),然后加入225
mL水中,固化10 min,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例5。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL的聚乙烯醇水溶液中,继续搅拌17 min(挥发乙酸乙酯),然后加入225
mL水中,固化2 h,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例6。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL聚乙烯醇水溶液中,继续搅拌17 min,挥发乙酸乙酯,收集微球并用水洗涤3次,混悬放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例7。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=75∶25,Mw=90
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL聚乙烯醇水溶液中,继续搅拌17 min,挥发乙酸乙酯,收集微球并用水洗涤3次,混悬放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例8。
先将200 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3.5 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;500 rpm磁力搅拌下,将此S/O混悬液滴加到50 mL浓度为0.01 g/mL的聚乙烯醇水溶液中,继续搅拌20 min(挥发乙酸乙酯),然后加入200
mL水中,固化10 min,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例9。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于2.5 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到40 mL浓度为0.01 g/mL的聚乙烯醇水溶液中,继续搅拌15 min(挥发乙酸乙酯),然后加入250mL水中,固化10 min,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
实施例10。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;700 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.02 g/mL的聚乙烯醇水溶液中,继续搅拌15 min(挥发乙酸乙酯),然后加入200
mL水中,固化15 min,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
对比例1。
将阿哌沙班原料药溶解在二氯甲烷中,形成油相,将油相滴加到浓度为0.01g/mL吐温80溶液中,先在5000 rpm条件下,均质8 min,然后在磁力搅拌(800 rpm)条件下挥干有机溶剂至药物析出,离心,弃上清;用水洗涤,收集沉淀于-80℃冰箱预冻10 h,再冷冻干燥48 h,得到D50为5 μm的阿哌沙班微粉。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3 mL乙酸乙酯中,再将上述溶剂析出法得到的50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL聚乙烯醇水溶液中,继续搅拌17 min(挥发乙酸乙酯),然后加入225
mL水中,固化10 min,收集微球并用水洗涤3次,混悬放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
对比例2。
将阿哌沙班原料药在研钵内研磨,得到D50为30 μm的阿哌沙班微粉。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉(D50:30 μm)均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液滴加到45 mL浓度为0.01 g/mL的聚乙烯醇水溶液中,继续搅拌17 min(挥发乙酸乙酯),然后加入225
mL水中,固化10 min,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
对比例3。
先将150 mg的聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50∶50,Mw=88
kDa)溶解于3 mL乙酸乙酯中,再将50 mg阿哌沙班微粉均匀分散在含有聚乳酸-羟基乙酸共聚物的乙酸乙酯溶液中,形成S/O混悬液;600 rpm磁力搅拌下,将此S/O混悬液3 s内迅速加入到45 mL浓度为0.01g/mL聚乙烯醇水溶液中,1500 rpm磁力搅拌10分钟,然后将形成的乳液10 s内迅速加入到225 mL水中,500 rpm磁力搅拌5小时,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
对比例4。
称取50 mg 阿哌沙班微粉、150 mg 聚乳酸-羟基乙酸共聚物(丙交脂与乙交酯的摩尔比=50:50,Mw=88
kDa)一起溶于3 mL二氯甲烷中,形成油相,在350
rpm条件下,将此油相连续滴加到45 mL质量浓度为0.01g/mL聚乙烯醇水溶液中乳化,继续搅拌10分钟,挥发二氯甲烷;将初步形成的微球,加入到225 mL水中,固化10
min,收集微球并用水洗涤3次,放入-80℃冰箱预冻10 h后,冷冻干燥48 h,得到微球粉末阿哌沙班微球。
测试例1 微球粒径。
取实施例1~10,对比例1~4制备的微球分别分散在水中,采用BT-2001激光粒度分布仪进行微球粒径测定。结果见表1,实施例微球的粒径(特指中位径)范围在90 mm以下,适合注射使用。
。
由表1可以看出,与实施例1相比,对比例1微球粒径较大,与采用溶剂析出法减小的原料药相比,研磨法减小的原料药其分散性好,制备的微球粒径较适宜。与实施例相比,对比例4制备的微球粒径较大,主要微球成形性和分散性较差有关。
测试例2 微球形态。
取实施例2、6、7制备的微球,用扫描电镜观察微球形态,结果分别见图1、图2以及图3,可以看出,阿哌沙班微球呈球形或类球形,表面光滑。
测试例3微球载药量与包封率。
用十八烷基硅烷键合硅胶为填充剂;以10 mmol/L乙酸铵∶乙腈(65∶35)为流动相,调节流速使主峰出峰时间为约9分钟,检测波长为280 nm;称取阿哌沙班对照品10 mg,置50 mL容量瓶中,加流动相溶解并稀释至刻度,摇匀;量取1 mL,置10 mL容量瓶中,用流动相稀释至刻度,摇匀,即为对照溶液;分别取实施例1-10制备的微球10 mg,精密称定,置10 mL离心管中,加入1mL乙腈完全溶解后,加入7 mL甲醇沉淀聚乳酸-羟基乙酸共聚物,然后离心(10000 r/min,10
min),取上清于50 mL容量瓶中,加甲醇定容至刻度。精密量取20 mL,注入液相色谱仪,记录色谱图;另取阿哌沙班对照品,同法测定,按外标法以峰面积计算,即得总药物量。进一步换算为微球的载药量与包封率。结果见表2。载药量与包封率的计算公式如下。
。
。
实施例制备的微球包封率均比对比例制备的高。可以看到改变PLGA50/50分子量及浓度对微球包封率与载药量影响不大。PLGA类型虽对微球包封率没有明显影响,但对微球后期的释放有较大影响,PLGA50/50较PLGA75/25释放度好。工艺中增加固化,可在一定程度上改善微球包封率,但固化时间由10
min提高至120 min后,导致微球包封率有下降。阿哌沙班原料药D50小对包封率有较大程度提高,采用溶剂析出法虽然也能将阿哌沙班原料药D50降至5 μm,但相比研磨法,其减小粒径后的原料药形成的微球粒径较大且药物包载效果较差,包封率在84%左右。
对比例3的结果显示,利用现有载药微球的制备方法制备的阿哌沙班微球,其包封率结果相对较差,达不到预期理想的效果,表明现有载药微球的制备方法不适用阿哌沙班微球的制备。对比例4的结果显示,采用O/W法制备阿哌沙班微球,制备过程中出现“流沙”现象(药物析出),导致微球较难包封,微球包封率较低,只有37%左右。本发明采用S/O/W法制备阿哌沙班微球,可避免药物出现“流沙”现象,包封率均在85%以上,尤其是本发明没有使用脂肪酸等辅料,成分相对更简单,载药量更高,更安全。
测试例4微球的体外释放度。
称取2 g氢氧化钠溶于500 mL水中,弃去105 mL,加入6.8 g磷酸二氢钾和605 mL水一起溶解,加入0.02% (w/v)吐温20,得到释放介质为pH7.4的含0.02%吐温20的PBS溶液。
别称取20 mg实施例1~2、实施例6~7制备的阿哌沙班微球于50 mL具塞锥形瓶中,加入50 mL含0.02%吐温20的PBS溶液,放入37℃的水浴恒温振荡锅内,于4 h、1 d、2 d、3 d、7 d……不同时间点取1 mL,离心(10000 rpm,10 min),取上清0.7 mL,并补上0.7 mL含0.02%吐温20的PBS溶液,隔天换液,然后进行HPLC分析,计算累积释放百分率,绘制累积释放百分率-时间的释放度曲线图。结果见图4~5。从图4的释放度曲线来看,实施例1微球突释较小,4 h内的突释仅为2.26%,24 h内累积释放度为8.27%,整体释放缓慢,可持续释放至84天,累积释放度达90%,具有明显的缓释作用。从图5的释放度曲线来看,实施例6的体外释放度要慢于实施例7的体外释放度,说明采用聚乳酸-羟基乙酸共聚物的比例为50/50时,具有较优的体外释放度,其释放可持续至42天或更久。这对于骨关节炎术后血栓预防、心房颤动患者的卒中预防、急性冠脉综合征等抗血栓性相关疾病的治疗具有适用性。
综上所述,本发明采用S/W/O法,结合研磨法控制原料药粒径,可获得较好的包封率与载药量,尤其是阿哌沙班微球的释放性能非常好。
Claims (10)
- 一种注射用阿哌沙班长效微球的制备方法,其特征在于,包括以下步骤:将阿哌沙班微粉分散在聚合物溶液中,形成混悬液;然后在搅拌条件下,将混悬液加到水相溶液中,挥发有机溶剂并固化,然后洗涤收集,冷冻干燥,得到注射用阿哌沙班长效微球。
- 根据权利要求1所述注射用阿哌沙班长效微球的制备方法,其特征在于,所述聚合物溶液中,聚合物选自聚乳酸-羟基乙酸共聚物、聚乳酸、聚乳酸-聚乙二醇和聚己内酯中的一种或几种,溶剂包括乙酸乙酯。
- 根据权利要求1所述注射用阿哌沙班长效微球的制备方法,其特征在于,将阿哌沙班原料药制备为阿哌沙班微粉;阿哌沙班微粉的D50粒径为1~10 μm;混悬液中,所述阿哌沙班微粉与可降解聚合物的重量比为1:2~50。
- 根据权利要求3所述注射用阿哌沙班长效微球的制备方法,其特征在于,将阿哌沙班原料药研磨,制备为阿哌沙班微粉。
- 根据权利要求1所述注射用阿哌沙班长效微球的制备方法,其特征在于,混悬液、水相溶液的体积比为1∶5~50。
- 根据权利要求1所述注射用阿哌沙班长效微球的制备方法,其特征在于,将混悬液滴加到水相溶液中。
- 根据权利要求1所述注射用阿哌沙班长效微球的制备方法,其特征在于,水相溶液包括添加剂与水,添加剂选自聚乙烯醇、聚山梨酯、聚乙二醇和十二烷基硫酸钠的一种或几种;添加剂的浓度为0.001~0.05 g/mL。
- 根据权利要求1所述注射用阿哌沙班长效微球的制备方法制备的注射用阿哌沙班长效微球。
- 权利要求1所述注射用阿哌沙班长效微球在制备缓释药物中的应用。
- 权利要求1所述注射用阿哌沙班长效微球在制备治疗骨关节炎术后血栓预防相关疾病的药物、心房颤动患者的卒中预防药物、急性冠脉综合征等抗血栓性相关药物中的应用。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/CN2022/136980 WO2024119376A1 (zh) | 2022-12-06 | 2022-12-06 | 一种注射用阿哌沙班长效微球及其制备方法 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/CN2022/136980 WO2024119376A1 (zh) | 2022-12-06 | 2022-12-06 | 一种注射用阿哌沙班长效微球及其制备方法 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2024119376A1 true WO2024119376A1 (zh) | 2024-06-13 |
| WO2024119376A9 WO2024119376A9 (zh) | 2024-08-22 |
Family
ID=91378228
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2022/136980 Ceased WO2024119376A1 (zh) | 2022-12-06 | 2022-12-06 | 一种注射用阿哌沙班长效微球及其制备方法 |
Country Status (1)
| Country | Link |
|---|---|
| WO (1) | WO2024119376A1 (zh) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002012670A (ja) * | 2000-04-24 | 2002-01-15 | Tanabe Seiyaku Co Ltd | マイクロスフェアの製法 |
| DE102005017777A1 (de) * | 2005-04-13 | 2006-10-19 | Pharmasol Gmbh | Verfahren zur schonenden Herstellung von hochfeinen Partikelsuspensionen |
| DE102006002877A1 (de) * | 2006-01-18 | 2007-07-19 | Friedrich-Schiller-Universität Jena | Verfahren zur Herstellung sehr kleiner organischer Nanopartikel, insbesondere mit einer mittleren Partikelgröße von weniger als 20 nm |
| CN104055738A (zh) * | 2013-03-20 | 2014-09-24 | Cj第一制糖株式会社 | 利用具有溶胶-凝胶转变特性的聚合物制备微球的方法以及由此制备的微球 |
| CN104367554A (zh) * | 2013-08-15 | 2015-02-25 | 中国医学科学院药用植物研究所 | 一种异烟肼缓释微球的制备方法 |
| CN109718225A (zh) * | 2019-02-01 | 2019-05-07 | 苏州大学 | 一种格拉司琼缓释微球及其制备方法 |
| CN113950322A (zh) * | 2019-03-27 | 2022-01-18 | Hlb制药有限责任公司 | 制备基于生物相容性聚合物的负载阿哌沙班的微球的方法 |
-
2022
- 2022-12-06 WO PCT/CN2022/136980 patent/WO2024119376A1/zh not_active Ceased
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002012670A (ja) * | 2000-04-24 | 2002-01-15 | Tanabe Seiyaku Co Ltd | マイクロスフェアの製法 |
| DE102005017777A1 (de) * | 2005-04-13 | 2006-10-19 | Pharmasol Gmbh | Verfahren zur schonenden Herstellung von hochfeinen Partikelsuspensionen |
| DE102006002877A1 (de) * | 2006-01-18 | 2007-07-19 | Friedrich-Schiller-Universität Jena | Verfahren zur Herstellung sehr kleiner organischer Nanopartikel, insbesondere mit einer mittleren Partikelgröße von weniger als 20 nm |
| CN104055738A (zh) * | 2013-03-20 | 2014-09-24 | Cj第一制糖株式会社 | 利用具有溶胶-凝胶转变特性的聚合物制备微球的方法以及由此制备的微球 |
| CN104367554A (zh) * | 2013-08-15 | 2015-02-25 | 中国医学科学院药用植物研究所 | 一种异烟肼缓释微球的制备方法 |
| CN109718225A (zh) * | 2019-02-01 | 2019-05-07 | 苏州大学 | 一种格拉司琼缓释微球及其制备方法 |
| CN113950322A (zh) * | 2019-03-27 | 2022-01-18 | Hlb制药有限责任公司 | 制备基于生物相容性聚合物的负载阿哌沙班的微球的方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2024119376A9 (zh) | 2024-08-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN115969796B (zh) | 一种jak抑制剂长效微球及其制备方法与应用 | |
| Patil et al. | Mucoadhesive microspheres: a promising tool in drug delivery | |
| CA2248592A1 (en) | Microspheres for use in the treatment of cancer | |
| CN116098872B (zh) | 一种注射用阿哌沙班长效微球及其制备方法 | |
| CN103877029B (zh) | 一种磁性载5-氟尿嘧啶聚乳酸羟基乙酸共聚物材料的制备方法 | |
| CN110237052A (zh) | 一种醋酸曲安奈德缓释微球及其制备方法 | |
| WO2003004024A1 (en) | Injectable sustained-release microspheres of huperzine a compounds | |
| CN1861041B (zh) | 局部注射用温敏型缓释凝胶剂及制备方法 | |
| WO2023015851A1 (zh) | 一种注射用曲安奈德微球植入剂及其制备方法 | |
| CN119837834B (zh) | 一种布瑞哌唑长效微球及其制备方法 | |
| CN101288673A (zh) | 一种盐酸米诺环素微球及其制备方法以及在制药中的应用 | |
| CN108403663A (zh) | 具有核壳结构的go-peg凝胶微球及其制备方法和应用 | |
| WO2020143662A1 (zh) | 一种壳寡糖修饰的自携式无载体鼻腔纳米制剂脑靶向递送系统及其制备方法 | |
| CN104288093A (zh) | 纳米药物透皮制剂在肿瘤中的应用 | |
| CN101282716B (zh) | 具有改善的初始溶解率的普仑司特固体分散体的药物组合物和制备该组合物的方法 | |
| CN115105585B (zh) | 一种靶向的长循环尿激酶纳米粒及其制备方法 | |
| CN116459220A (zh) | 昔萘酸普拉克索缓释微球及其制备方法与应用 | |
| CN100366249C (zh) | 一种替莫唑胺控释给药系统 | |
| JPS6163613A (ja) | 顆粒状に調整された徐放性製剤 | |
| WO2024119376A1 (zh) | 一种注射用阿哌沙班长效微球及其制备方法 | |
| CN109701071B (zh) | 改性丝素蛋白动脉栓塞微球及其制备方法 | |
| CN109939220A (zh) | 具有速释和缓释效果的多肽微球及其制备方法 | |
| WO2024119375A1 (zh) | 一种jak抑制剂长效微球及其制备方法与应用 | |
| CN113786393A (zh) | 一种利伐沙班微球及其制备方法与应用 | |
| CN105997887A (zh) | 一种含小分子添加剂的托特罗定缓释微球制剂及制备方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 22967537 Country of ref document: EP Kind code of ref document: A1 |
|
| NENP | Non-entry into the national phase |
Ref country code: DE |
|
| 122 | Ep: pct application non-entry in european phase |
Ref document number: 22967537 Country of ref document: EP Kind code of ref document: A1 |
|
| 122 | Ep: pct application non-entry in european phase |
Ref document number: 22967537 Country of ref document: EP Kind code of ref document: A1 |