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Quality by Design in Twin Screw Granulation

机译:双螺杆造粒的设计品质

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摘要

Granulation is often used as a size enlargement unit operation in various solid handling and powder processing industries such as pharmaceuticals, foods, detergents, catalysts, and particulate chemicals. Granulation helps to mitigate issues related to poor flowability, dust hazards, and powder segregation. Traditionally, granulation has been performed in the batch mode of operation. More recently, the United States Food and Drug Administration is encouraging manufacturers to adopt continuous processing due its several advantages over batch manufacturing. Twin screw granulation is therefore becoming increasingly relevant due to its compact size, continuous and robust mode of operation, flexible and customizable design, and flexible production capacity.;Wet granule breakage is reported to be a key rate process in twin screw granulation and is also the main mechanism for controlling granule size within the granulator. This dissertation is the first study to explicitly measure the influence of material properties, process conditions, and screw element geometry on the breakage process in the twin screw granulator (TSG). Novel breakage isolating experiments were performed at various screw speeds and powder feed rates using model granules having a wide range of material dynamic yield strengths (DYSs) in conveying and distributive mixing element screw configurations. The process parameter dependence was quantified using the dimensionless powder feed number. Daughter size distributions and survivor pellet shape visualization was used to infer that the breakage mechanism in conveying elements (CE) is primarily edge chipping whereas in distributive mixing elements (DME), breakage is a combination of chipping and crushing.;Implications for using the results for both optimizing screw element design and calculating kinetic parameters for population balance modeling are discussed. Preliminary breakage rate process models were formulated based on the experimental data obtained from the breakage isolating experiments. A modified Weibull breakage kernel was used to fit the breakage probability data for the 3 mm pellet breakage in CEs and 3 mm and 2 mm pellet breakage in DMEs. Consequently, a piecewise breakage probability model as a function of granule size is proposed for conveying and distributive mixing elements. The daughter size distribution data was fitted by using a one parameter power law model for both CEs and DMEs.;The conclusions from the breakage isolating experiments were validated by performing wet granulation experiments using industrially relevant powder formulations. The influence of pharmaceutical formulation characteristics on granule properties formed using CEs and DMEs in twin screw granulation were examined. High and low drug dose formulations with three different active pharmaceutical ingredients (APIs) were considered. The type and concentration of the API in the formulation significantly affected the dry blend particle size distribution and the wet blend dynamic yield strength. However, despite the differences in blend properties, the granule size distributions in DMEs were not significantly affected by the type of API used.;The granule size distributions in DMEs were solely functions of the liquid-to-solid ratio and the screw element geometry. However, the granule porosities were observed to be dependent on both the liquid-to-solid ratio and the dynamic yield strength of the blends. The granule size distributions in CEs were a strong function of the liquid-to-solid ratio, screw element geometry, and material DYS. A CAD geometry analysis of the free volume in the granulator revealed that there is a direct quantitative correlation between the screw geometry and the maximum size and aspect ratio of the granules obtained using conveying elements. Conveying element geometries with different pitch lengths were 3D printed to generate cost-effective prototypes of the designs. Wet granulation experiments were performed using the 3D printed designs to test the hypothesis that the correlation between the granule shape and maximum granule size and the screw element geometry is predictable a priori. The feasibility of 3D printing method for fabricating new screw element designs is examined. Quality-by-Design strategies and scale-up criteria for twin screw granulation are discussed.;The influence of differences in formulation wettability for CEs and DMEs were studied. High drug dose formulations with and without a hydrophobic additive were considered for wet granulation in the two screw geometries. It was observed that the low shear CEs do not cause significant liquid redistribution, and differences in powder wettability are reflected in the granule properties. However, DMEs cause significant granule breakage resulting in efficient liquid redistribution, and no differences were observed in the granule properties for hydrophilic and hydrophobic formulations. These results suggest that breakage mechanisms strongly influence the effect of the raw material properties on the final critical quality attributes of granules.;The work in this dissertation highlights the importance of rate-process specific fundamental experiments and relevance to real powder formulation behavior in twin screw granulation. (Abstract shortened by ProQuest.).
机译:制粒通常在各种固体处理和粉末加工行业(例如制药,食品,清洁剂,催化剂和颗粒化学品)中用作增大尺寸的装置。制粒有助于减轻与流动性差,粉尘危害和粉末偏析有关的问题。传统上,制粒以间歇操作模式进行。最近,美国食品和药物管理局(FDA)鼓励制造商采用连续加工,因为它比批量生产具有多个优势。因此,双螺杆造粒由于其紧凑的尺寸,连续且鲁棒的操作模式,灵活和可定制的设计以及灵活的生产能力而变得越来越重要。;据报道,湿法制粒破碎是双螺杆造粒的关键过程,并且也是控制制粒机内颗粒大小的主要机制。本文是首次明确测量材料特性,工艺条件和螺杆元件几何形状对双螺杆制粒机(TSG)破损过程的影响的研究。使用在输送和分布式混合元件螺杆配置中具有多种材料动态屈服强度(DYS)的模型颗粒,以各种螺杆速度和粉末进料速率进行了新颖的破损隔离实验。使用无量纲粉末进料数量来量化工艺参数的依赖性。使用子代尺寸分布和幸存的颗粒形状可视化来推断输送元件(CE)的破碎机理主要是边缘碎裂,而在分布式混合元件(DME)中,破碎是破碎和压碎的组合。;使用结果的含义讨论了用于优化螺杆元件设计和计算动力学参数以进行种群平衡建模的方法。根据从破损隔离实验获得的实验数据,建立了初步破损率过程模型。修改后的威布尔破损核用于拟合CE中3 mm颗粒破损以及DME中3 mm和2 mm颗粒破损的破损概率数据。因此,提出了用于输送和分配混合元件的分段破碎概率模型,其作为颗粒尺寸的函数。 CE和DME的单参数幂律模型拟合了子粒尺寸分布数据。通过使用工业上相关的粉末配方进行湿法制粒实验,验证了断裂分离实验的结论。在双螺杆制粒中,研究了药物制剂特性对使用CE和DME形成的颗粒性质的影响。考虑了具有三种不同活性药物成分(API)的高和低药物剂量制剂。制剂中API的类型和浓度显着影响干混物的粒度分布和湿混物的动态屈服强度。然而,尽管共混物性能有所不同,但二甲醚中颗粒尺寸的分布并不受所用API的类型的影响。二甲醚中颗粒尺寸的分布仅是液固比和螺杆元件几何形状的函数。但是,观察到颗粒的孔隙率既取决于液体对固体的比率,也取决于混合物的动态屈服强度。 CE中的颗粒大小分布是液固比,螺杆元件几何形状和材料DYS的强函数。造粒机中自由体积的CAD几何分析表明,螺杆几何形状与使用输送元件获得的颗粒的最大尺寸和长宽比之间存在直接的定量相关性。 3D打印具有不同节距长度的输送元件几何形状,以生成具有成本效益的设计原型。使用3D打印设计进行了湿法制粒实验,以检验以下假设:颗粒形状和最大颗粒尺寸与螺杆元件几何形状之间的相关性是先验可预测的。研究了3D打印方法用于制造新的螺杆元件设计的可行性。讨论了双螺杆造粒的设计质量策略和放大标准。;研究了CE和DMEs的配方润湿性差异的影响。考虑在两种螺杆几何结构中湿法制粒具有和不具有疏水性添加剂的高药物剂量制剂。观察到低剪切CE不会引起显着的液体重新分布,并且粉末润湿性的差异反映在颗粒性质中。但是,DME会导致明显的颗粒破裂,从而导致有效的液体重新分配,并且在亲水性和疏水性制剂的颗粒性质上未观察到差异。这些结果表明,破碎机理对原材料性能的影响极大地影响了颗粒的最终临界质量属性。本论文的工作凸显了速率过程特定的基础实验的重要性以及与双螺杆实际粉末配方行为的相关性。造粒。 (摘要由ProQuest缩短。)。

著录项

  • 作者

    Pradhan, Shankali U.;

  • 作者单位

    Purdue University.;

  • 授予单位 Purdue University.;
  • 学科 Chemical engineering.
  • 学位 Ph.D.
  • 年度 2017
  • 页码 165 p.
  • 总页数 165
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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