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首页> 外文期刊>European journal of pharmaceutical sciences >Linking granulation performance with residence time and granulation liquid distributions in twin-screw granulation: An experimental investigation
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Linking granulation performance with residence time and granulation liquid distributions in twin-screw granulation: An experimental investigation

机译:在双螺杆制粒中将制粒性能与停留时间和制粒液体分布联系起来:一项实验研究

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Twin-screw granulation is a promising wet granulation technique for the continuous manufacturing of pharmaceutical solid dosage forms. A twin screw granulator displays a short residence time. Thus, the solid-liquid mixing must be achieved quickly by appropriate arrangement of transport and kneading elements in the granulator screw allowing the production of granules with a size distribution appropriate for tableting. The distribution of residence time and granulation liquid is governed by the field conditions (such as location and length of mixing zones) in the twin-screw granulator, thus contain interesting information on granulation time, mixing and resulting sub-processes such as wetting, aggregation and breakage. In this study, the impact of process (feed rate, screw speed and liquid-to-solid ratio) and equipment parameters (number of kneading discs and stagger angle) on the residence time (distribution), the granulation liquid-powder mixing and the resulting granule size distributions during twin-screw granulation were investigated. Residence time and axial mixing data was extracted from tracer maps and the solid-liquid mixing was quantified from moisture maps, obtained by monitoring the granules at the granulator outlet using near infra-red chemical imaging (NIR-CI). The granule size distribution was measured using the sieving method. An increasing screw speed dominantly reduced the mean residence time. Interaction of material throughput with the screw speed and with the number of kneading discs led to most variation in the studied responses including residence time and mixing capacity. At a high screw speed, granulation yield improved due to high axial mixing. However, increasing material throughput quickly lowers the yield due to insufficient mixing of liquid and powder. Moreover, increasing liquid-to-solid ratio resulted in more oversized granules, and the fraction of oversized granules further increased at higher throughput. Although an increasing number of kneading discs was found to be critical for achieving a uniform distribution of the granulation liquid, the granulation performance was hampered due to insufficient solid-liquid mixing capacity of the current kneading discs which is essential for wet granulation. Thus, a balance between material throughput and screw speed should be strived for in order to achieve a specific granulation time and solid-liquid mixing for high granulation yield. Additionally, more efforts are needed both in modification of the screw configuration as well as the geometry of the mixing elements to improve the mixing capacity of the twin-screw granulator. The results from the current experimental study improved the understanding regarding the interplay between granulation time and the axial and solid-liquid mixing responsible for the granulation performance in twin-screw wet granulation. (C) 2015 Elsevier B.V. All rights reserved.
机译:双螺杆制粒是一种有望连续生产药物固体剂型的湿法制粒技术。双螺杆制粒机的停留时间短。因此,必须通过在造粒机螺杆中适当布置输送和捏合元件来快速实现固液混合,从而允许生产具有适于压片的尺寸分布的颗粒。停留时间和制粒液体的分布受双螺杆制粒机中的现场条件(例如混合区域的位置和长度)的控制,因此包含有关制粒时间,混合以及由此产生的子过程(如润湿,聚集)的有趣信息和破损。在这项研究中,工艺(进料速度,螺杆速度和液固比)和设备参数(捏合盘数和错位角)对停留时间(分布),制粒液-粉混合和分离的影响。研究了双螺杆造粒过程中产生的粒度分布。停留时间和轴向混合数据从示踪图提取,固液混合从水分图定量,通过使用近红外化学成像(NIR-CI)监控制粒机出口处的颗粒获得。使用筛分法测量粒度分布。螺杆速度的提高主要减少了平均停留时间。材料通过量与螺杆速度和捏合盘数量的相互作用导致研究响应的最大变化,包括停留时间和混合能力。在高螺杆速度下,由于高轴向混合,造粒产率得以提高。然而,由于液体和粉末的不充分混合,增加材料通过量迅速降低了产率。此外,增加的液/固比导致更多的超大颗粒,并且更大的颗粒的比例以更高的产量进一步增加。尽管发现增加数量的捏合盘对于实现造粒液体的均匀分布至关重要,但是由于当前捏合盘的固液混合能力不足,造粒性能受到阻碍,这对于湿法制粒是必不可少的。因此,为了达到特定的制粒时间和固液混合以实现高制粒率,应努力在物料通过量和螺杆速度之间取得平衡。另外,在改进螺杆构造以及混合元件的几何形状方面都需要付出更多的努力以提高双螺杆造粒机的混合能力。当前实验研究的结果改善了对制粒时间与轴向和固液混合之间相互作用的理解,而轴向和固液混合是双螺杆湿法制粒的主要性能。 (C)2015 Elsevier B.V.保留所有权利。

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