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Steady states in granulation of pharmaceutical powders with application to scale-up

机译:药物粉末造粒的稳态及其在放大生产中的应用

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Theoretical and experimental evidence is given to show that steady states can be reached during agglomerate growth and break-up in high-shear granulation of fine powders. An earlier theoretical model [G.I. Tardos, I.M. Khan and P.R. Mort, Critical parameters and limiting conditions in binder granulation of fine powders, Powder Technology, 94, 245-258 (1997).], based on simple energy-dissipation considerations hinted at the existence of these states at the point where growth is counterbalanced by breakage. Further theoretical evidence is obtained from molecular dynamic simulations of wet and dry particles situated in a constant shear field [I. Talu, G.I. Tardos and M.I. Khan, Computer simulation of wet granulation, Powder Technology, 110, 59-75 (2000).], where the size distribution of initially identical particles, shifts in time to reach a dynamic steady state. Under the conditions of this steady state, the number of breaking agglomerates approximately equals the number of forming ones to yield a time independent final-size distribution. Experimental evidence to support the theoretical findings is obtained during the present research by measuring particle size distributions at line at crucial points during granulation of a typical pharmaceutical powder in a high-shear mixer. In order to reach a steady state, binder addition has to be slow enough and wet massing has to be long enough so that neither has an influence on the final properties of the granules. We show experimentally that if binder is spread properly and homogeneously in the powder and continuous shearing of the wet mass ensures homogeneous, equal growth of the granules, the steady state will only be a function of the total amount of fluid added provided that the shear forces in the machine are maintained constant. These findings are important in that they show that under carefully controlled conditions of binder addition and shear in the mixer, the granulation process is robust and controllable and can, in principle, be scaled up with ease once the powder ingredients and the total amount of binder are fixed.
机译:理论和实验证据表明,在细粉的高剪切造粒过程中,团聚体生长和破碎过程中可以达到稳态。较早的理论模型[G.I. Tardos,IM Khan和PR Mort,《细粉粘合剂制粒中的关键参数和极限条件》,《粉末技术》,第94卷,第245-258页(1997)。],基于简单的能量耗散考虑,暗示了这些状态的存在。增长被破坏抵消的点。从位于恒定剪切场中的湿颗粒和干颗粒的分子动力学模拟获得了进一步的理论证据[I.塔卢(Talu) Tardos和M.I. Khan,《湿法制粒的计算机模拟》,《粉末技术》,第110卷,第59-75页(2000年)。],其中最初相同的颗粒的尺寸分布随时间推移而达到动态稳态。在这种稳定状态下,破碎团聚体的数量大约等于成形团聚体的数量,以产生与时间无关的最终尺寸分布。在当前的研究过程中,通过测量高剪切混合机中典型药物粉末造粒过程中关键点在线的粒径分布,获得了支持理论发现的实验证据。为了达到稳定状态,粘合剂的添加必须足够慢并且湿质量必须足够长以使得两者均不影响颗粒的最终性质。我们通过实验证明,如果粘合剂在粉末中适当且均匀地铺展,并且连续剪切湿物料可确保颗粒均匀,均匀地生长,则在剪切力作用下,稳态将仅是流体总量的函数。在机器中保持恒定。这些发现很重要,因为它们表明在精心控制的粘合剂添加和混合机剪切条件下,制粒过程是可靠且可控制的,原则上,一旦粉末成分和粘合剂总量达到上限,就可以轻松扩大规模是固定的。

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