CN107519134B - 一种热熔离心制备固体分散体的方法 - Google Patents
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Abstract
本发明涉及一种热熔离心制备固体分散体的方法。包括下述步骤:将质量分数1%‑50%的药物与质量分数50‑99%的载体材料熔融混合,高速离心制备固体分散体粉末,其中,药物可以是水溶性药物、难溶性药物或易吸潮药物;载体材料可以是水溶性或水不溶性材料。本发明提供了一种热熔离心直接制备固体分散体的方法。本方法生产过程中无需使用有机溶剂和水为介质,无需后续粉碎操作,设备简单,环保高效,适于工业化生产。本方法在制备难溶性药物速释粉末和中药粉末防潮等领域有良好的应用前景。
Description
技术领域
本发明属于制药技术领域,具体涉及一种热熔离心制备固体分散体的方法。
背景技术
本课题组采用热熔离心法,经处方工艺优化,研制出了载药微丝(直径10μm-500μm),具有速释和缓释等多种功能。相关内容已申请发明专利(一种含药微丝及其制备方法,CN201610110161.5)。经大量实验,我们又发现,采用新的载体和药物,优化处方工艺,热熔离心法可进一步制备载药粉末。经检测药物在载体中高度分散,符合固体分散体特征,具有缓释、速释和防潮等特殊效果,尤其适用于提高难溶性药物溶解度和防止中药成份吸潮。
现有固体分散体常规制备方法主要是:溶剂-熔融法、喷雾干燥法和热熔挤出法。本发明的热熔离心法无需有机溶剂和水为介质,比溶剂-熔融法和喷雾干燥法环保节能和高效。本发明的热熔离心法可以直接制备固体分散体粉末,无需热熔挤出条状物后再次粉碎,生产设备简单生产效率更高。
发明内容
本发明的目的在于解决现有技术的不足,提供了一种固体分散体的制备方法。该方法可以直接制备固体分散体粉末,无需热熔挤出条状物后再次粉碎,生产设备简单生产效率更高。
本发明解决技术问题所采用的技术方案为:
一种固体分散体的制备方法,包括下述步骤:将质量分数1%-50%的药物与质量分数50-99%的载体材料熔融混合,高速离心制备固体分散体粉末,其中,药物可以是水溶性药物、难溶性药物或易吸潮药物;载体材料可以是水溶性或水不溶性材料。
作为优选,所述水溶性载体材料为果糖、半乳糖、木糖醇、乳糖、甘露醇、山梨醇、聚乙二醇类、泊洛沙姆类、卖泽类、聚氧乙烯蓖麻油类、枸橼酸、富马酸、酒石酸、琥珀酸和聚乙烯醇中的任意一种或多种。
作为优选,所述水不溶性材料为单硬脂酸甘油酯、硬脂酸、硬脂醇和单油酸甘油酯中一种或多种。
作为优选,药物与载体重量比为1:3-1:9。
作为优选,药物与载体的重量比为1:3-1:4,用于制备速释的固体分散体。
作为优选,药物与载体的重量比为1:4-1:5,用于制备防潮的固体分散体。
作为优选,熔融温度为40-150℃;离心转速为500-10000 r/min;离心孔径为10-500 μm;固体分散体粉末收集距离10-50 cm。
作为优选,熔融温度为60-80℃;离心转速为1000-1500 r/min;离心孔径为50-100μm, 收集距离为20-40cm。
本发明的有益效果为:
本发明提供了一种热熔离心直接制备固体分散体的方法。本方法生产过程中无需使用有机溶剂和水为介质,无需后续粉碎操作,设备简单,环保高效,适于工业化生产。本方法在制备难溶性药物速释粉末和中药粉末防潮等领域有良好的应用前景。
附图说明
图1药辅比对微观形态的影响,放大90倍
图2药辅比对溶出行为的影响
图3黄芪多糖固体分散体外观,放大90倍
图4 不同制剂吸湿48h后外观图
图 5 不同制剂的吸湿曲线
图6 不同制备方法对溶出行为的影响
图7安乃近固体分散体外观,放大90倍
图8安乃近固体分散体的溶出行为。
具体实施方式
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅用以解释本发明,并不用于限定本发明。
实施例1 硝苯地平速释固体分散体(难溶性药物/水溶性载体)
分别取1 g,2 g,3 g,4 g 聚乙二醇在90℃下熔融,分别加入1 g硝苯地平粉末,搅匀,在熔融状态下,快速离心转动,转速为1000 r/min,收集距离为10 cm,则得到硝苯地平:聚乙二醇分别为1:1,1:2,1:3,1:4的硝苯地平固体分散体粉末。显微外观如图1所示。
将上述硝苯地平固体分散体和原料药进行体外释放行为评价,采用浆法,介质为0.5% 的十二烷基硫酸钠溶液,转速75 r/min,介质量为500 mL,每杯试样相当于含药量25mg。定时取样10 mL,补液。取滤液采用分光光度法,于333 nm处测定吸光度,计算药物累计释放百分率,体外释放行为结果如图2所示。
结果显示:硝苯地平固体分散体的释放速率和最大释放百分率随着聚乙二醇含量的提高而提高,其中硝苯地平:聚乙二醇比例为1:4,1:3,1:2,1:1的硝苯地平固体分散体2h的释放百分率分别为89.62%,81.57%,72.05%,64.54%,原料药2 h的释放百分率为54.47%,说明熔融离心法制备的固体分散体粉末可以有效促进硝苯地平的溶出,有利于硝苯地平在体内的吸收。
实施例2 黄芪多糖防潮固体分散体(易吸潮药物/水溶性载体)
将4 g聚乙二醇在60 ℃下熔融后加入1 g黄芪多糖混匀,转动离心,转速为500 r/min,收集距离为20 cm,得到黄芪多糖固体分散体粉末,显微外观如图3所示。
分别称取0.5 g上述黄芪多糖固体分散体、黄芪多糖与聚乙二醇物理混合物(黄芪多糖与聚乙二醇比例为1:4)、黄芪多糖于称量瓶中,放置在湿度为75%,温度为25摄氏度环境中48 h。吸湿后黄芪多糖、物理混合物、固体分散体外观如图4。吸湿曲线如图5。
结果显示:24h后黄芪多糖吸湿率为13.26%,黄芪多糖与聚乙二醇物理混合物为6.33%,黄芪多糖固体分散体为4.44%。黄芪多糖和物理混合物均产生明显外观变化,而黄芪多糖固体分散体仍为粉末,无明显外观变化。说明黄芪多糖固体分散体能够有效产生防吸潮效用,利于存储和运输。
实施例3 热熔挤出固体分散体与热熔离心固体分散体(不同工艺差异)
取1 g硝苯地平与4 g聚乙二醇混合,采用热熔挤出法制备固体分散体。转速为60r/min,温度控制为70 ℃,挤出物冷却至室温,得到热熔挤出混合物。用研钵分次研磨1 h,过筛,得到热熔挤出固体分散体粉末。平均粒径为321μm,形态为不规则粉末。粉末产率为53.2%,粉末堆密度为1.25g/mL。
取4 g聚乙二醇在70℃下熔融,加入1 g硝苯地平粉末,搅匀,在熔融状态下,快速离心转动,转速为3000 r/min。收集距离为20 cm。过筛直接得热熔离心固体分散体粉末。粉末平均粒径为214μm,形态为类球形或椭球形。粉末产率为86.5%,粉末堆密度为0.94g/mL。同样的处方工艺,改变收集距离为50 cm。过筛直接得热熔离心固体分散体粉末,平均粒径159μm,形态为类球形或椭球形。粉末产率为80.3%,粉末堆密度为0.92g/mL。
分别将上述方法制备的热熔挤出硝苯地平固体分散体粉末、50cm收集距离的热熔离心固体分散体粉末和原料药进行体外释放行为评价。采用溶出仪浆法,介质为0.5% 的十二烷基硫酸钠溶液,转速75 r/min,介质为500 mL,每杯试样相当于含药量25 mg。定时取样10 mL,补液。取滤液采用分光光度法,于333 nm处测定吸光度,计算药物累计释放百分率,体外释放行为结果如图6所示:
结果显示:热熔挤出法与热熔离心法制备的固体分散体的溶出行为无明显差异,但与热熔挤出法相比,热熔离心法可以直接制备粉末状的固体分散体,且制备工艺更简单,平均粒径更细,过筛粉末产率更高,形态相对更接近球形。扩大收集距离,会得到更细更均匀的粉末,就与较大粒子在分离过程中易沉降有关。
实施例4 安乃近缓释固体分散体(水溶性药物/难溶性载体)
取9 g 硬脂酸在80℃下熔融,分别加入1 g安乃近粉末,搅匀,在熔融状态下,快速离心转动,转速为1500 r/min,收集距离为40 cm,则得到安乃近固体分散体粉末。显微外观如图7所示:将上述安乃近固体分散体和原料药进行体外释放行为评价,采用浆法,介质为500 mL纯化水,转速75 r/min,每杯试样相当于含药量5 mg。定时取样10 mL,补液。取滤液采用分光光度法,于258nm处测定吸光度,计算药物累计释放百分率,体外释放行为结果如图8所示:结果显示:安乃近原料药迅速释放,而安乃近的固体分散体在8h处才释放完全,表现出了缓释特性,说明可用热熔离心法制备粉末型的缓释固体分散体。
Claims (3)
1.一种固体分散体的制备方法,其特征在于,所述制备方法包括下述步骤:将质量分数l%-50%的药物与质量分数50-99%的载体材料熔融混合,高速离心制得 ,所述药物为水溶性药物或易吸潮药物;载体材料为水不溶性材料,所述水不溶性载体材料为单硬脂酸甘油酯、硬脂酸、硬脂醇和单油酸甘油酯中一种或多种,所述熔融温度为60-80℃;离心转速为1000-1500r/min;离心孔径为50-100μm;固体分散体粉末收集距离20-40cm。
2.根据权利要求1所述的一种固体分散体的制备方法,其特征在于,所述药物与载体的重量比为1:3-1:9。
3.根据权利要求1所述的一种固体分散体的制备方法,其特征在于,所述药物与载体的重量比为1:4-1:5,用于制备防潮的固体分散体。
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