Gasparini G, Kosvintsev S R, Stillwell M T, Holdich R G
Department of Chemical Engineering, Loughborough University, Leicestershire LE11 3TU, UK.
Colloids Surf B Biointerfaces. 2008 Feb 15;61(2):199-207. doi: 10.1016/j.colsurfb.2007.08.011. Epub 2007 Aug 26.
Uniformly sized microparticles of poly(D,L-lactic-co-glycolic) (PLGA) acid, with controllable median diameters within the size range 40-140 microm, were successfully prepared by membrane emulsification of an oil phase injected into an aqueous phase, followed by solvent removal. Initially, simple particles were produced as an oil in water emulsion, where dichloromethane (DCM) and PLGA were the oil phase and water with stabiliser was the continuous phase. The oil was injected into the aqueous phase through an array type microporous membrane, which has very regular pores equally spaced apart, and two different pore sizes were used: 20 and 40 microm in diameter. Shear was provided at the membrane surface, causing the drops to detach, by a simple paddle stirrer rotating above the membrane. Further tests involved the production of a primary water in oil emulsion, using a mechanical homogeniser, which was then subsequently injected into a water phase through the microporous membrane to form a water in oil in water emulsion. These tests used a water-soluble model drug (blue dextran) and encapsulation efficiencies of up to 100% were obtained for concentrations of 15% PLGA dissolved in the DCM and injected through a 40 microm membrane. Solidification of the PLGA particles was followed by removal of the DCM through the surrounding aqueous continuous phase. Different PLGA concentrations, particle size and osmotic pressures were considered in order to find their effect on encapsulation efficiency. Osmotic pressure was varied by changing the salt concentration in the external aqueous phase whilst maintaining a constant internal aqueous phase salt concentration. Osmotic pressure was found to be a significant factor on the resulting particle structure, for the tests conducted at lower PLGA concentrations (10% and 5% PLGA). The PLGA concentration and particle size distribution influence the time to complete the solidification stage and a slow solidification, formed by stirring gently overnight, provided the most monosized particles and highest encapsulation efficiency.
通过将油相注入水相进行膜乳化,随后去除溶剂,成功制备了尺寸均匀的聚(D,L-乳酸-乙醇酸)(PLGA)酸微粒,其可控的中位直径在40-140微米范围内。最初,简单的颗粒以水包油乳液的形式产生,其中二氯甲烷(DCM)和PLGA为油相,含有稳定剂的水为连续相。油通过具有非常规则且等距排列孔隙的阵列式微孔膜注入水相,使用了两种不同的孔径:直径20微米和40微米。通过在膜上方旋转的简单桨式搅拌器在膜表面提供剪切力,使液滴分离。进一步的试验涉及使用机械匀浆器制备初级油包水乳液,然后将其通过微孔膜注入水相以形成水包油包水乳液。这些试验使用了一种水溶性模型药物(蓝色葡聚糖),对于溶解在DCM中并通过40微米膜注入的15%PLGA浓度,获得了高达100%的包封效率。PLGA颗粒固化后,通过周围的水连续相去除DCM。考虑了不同的PLGA浓度、粒径和渗透压,以确定它们对包封效率的影响。通过改变外部水相中的盐浓度,同时保持内部水相盐浓度恒定来改变渗透压。对于在较低PLGA浓度(10%和5%PLGA)下进行的试验,发现渗透压是影响所得颗粒结构的一个重要因素。PLGA浓度和粒径分布影响完成固化阶段的时间,通过轻轻搅拌过夜形成的缓慢固化提供了最单分散的颗粒和最高的包封效率。