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Cake filter scale-up, simulation and data acquisition - A new approach

机译:滤饼过滤器的放大,仿真和数据采集-一种新方法

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This paper details a unique, automated filtration apparatus and the newly developed Filter Design Software (FDS) which facilitates equipment selection, scale-up and simulation through an integrated experimental and theoretical approach. By way of example, experimental data were obtained with the apparatus over constant, variable and stepped pressure regimes. Inherent suspension properties were maintained throughout by utilising a computer-controlled pressure regulator and cake formation was monitored by micro-pressure transducers capable of providing up to seven independent measures of liquid pressure within 3.3 mm of the filter medium surface. For constant pressure and moderately compressible tale cakes the liquid pressure increased with cake height in a non-linear manner and generally exhibited a concave profile. When a pressure step was applied following a period of constant pressure filtration, the cake structure typically required up to 30 s to reach a new pseudo-equilibrium state. During this time the reciprocal filtrate flow rate vs. filtrate volume plot was non-linear and the liquid pressures in the cake increased rapidly before remaining nearly constant. When the cake was thicker or the pressure step larger, the liquid pressure measured closer to the filter medium remained either constant following the increase in pressure or increased slowly over the 360 s duration of the pressure step which indicates potential difficulties with the stepped pressure test. The filtration data were analysed using FDS to obtain scale-up coefficients and the impact of using incorrect scale-up coefficients on likely filter performance at the process scale is shown. The simulation capabilities of FDS are also highlighted through a case study in which, by way of example, the influence of crystal formation and other operating parameters on the filter cycle for a pharmaceutical product are shown. Simulations quantify how crystal form can detrimentally influence all phases of a cycle and lead to, for instance, slower filtration and wetter filter cakes. (c) 2008 Published by Elsevier B.V. on behalf of Taiwan Institute of Chemical Engineers.
机译:本文详细介绍了独特的自动化过滤设备和新开发的过滤器设计软件(FDS),该软件通过集成的实验和理论方法来简化设备的选择,放大和仿真。举例来说,使用该设备在恒定,可变和步进压力范围内获得了实验数据。始终通过使用计算机控制的压力调节器来保持固有的悬浮特性,并通过微压传感器监测滤饼的形成,该微压传感器能够提供在过滤介质表面3.3毫米内多达七个独立的液体压力测量值。对于恒定压力和适度可压缩的故事饼,液体压力随着饼高度以非线性方式增加,并且通常表现出凹形轮廓。在一段时间的恒压过滤之后施加压力步骤时,滤饼结构通常需要长达30 s的时间才能达到新的拟平衡状态。在这段时间内,相互的滤液流量与滤液体积的关系是非线性的,滤饼中的液体压力在保持接近恒定之前迅速增加。当滤饼变厚或压力阶跃较大时,在压力阶跃的360 s持续时间内,随着压力的升高,在靠近过滤介质的位置测得的液体压力保持恒定或缓慢升高,这表明逐步压力测试存在潜在的困难。使用FDS分析过滤数据以获得放大系数,并显示了使用错误的放大系数对过程规模下可能的过滤器性能的影响。案例研究还强调了FDS的仿真能力,在该案例研究中,举例说明了晶体形成和其他操作参数对药品过滤周期的影响。模拟量化了晶体形式如何有害地影响循环的所有阶段,并导致例如较慢的过滤和较湿的滤饼。 (c)2008年由Elsevier B.V.代表台湾化学工程师学会出版。

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