Stability of Combined Continuous Granulation and Agglomeration Processes in a Fluidized Bed with Sieve-Mill-Recycle

被引:1
|
作者
Otto, Eric [1 ]
Duerr, Robert [2 ]
Kienle, Achim [1 ,3 ]
机构
[1] Otto von Guericke Univ, Automat Modelling, Univ Pl 2, D-39106 Magdeburg, Germany
[2] Magdeburg Stendal Univ Appl Sci, Engn Math, Breitscheidstr 2, D-39114 Magdeburg, Germany
[3] Max Planck Inst Dynam Complex Tech Syst, Proc Synth & Proc Dynam, Sandtorstr 1, D-39106 Magdeburg, Germany
关键词
fluidized bed; granulation; agglomeration; layering growth; bifurcation analysis; LAYERING GRANULATION; SPRAY GRANULATION; PARAMETERS; BEHAVIOR; MODEL;
D O I
10.3390/pr11020473
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Particle formation in fluidized beds is widely applied in an industrial context for the solidification of liquids and size enlargement of granular materials. The two main size-enlargement mechanisms are layering growth and agglomeration. For continuous process configurations with sieve-mill-recycle and layering growth only, the occurrence of undesired self-sustained oscillations in the particle size distribution under certain process conditions is well-known. This contribution investigates the stability of the practically relevant process with additional particle agglomeration by means of a model-based numerical bifurcation analysis. It is shown that the occurrence of stable limit cycles is inhibited by an increased rate of particle agglomeration for a variety of different process conditions and different agglomeration kinetics. These results enhance the understanding of the agglomeration and layering growth dynamics and are relevant for the process design and operation.
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页数:13
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