Fluidized Bed Spray Granulation: Nucleation Studies with Steady-State Experiments

Fluidized bed spray granulation is a technology for the production and formulation of coarse-grained granules from solutions, suspensions, or melts. In order to run the process continuously and stable, product particles removed from the process have to be replaced by new small granules. The nucleation rates have to be within certain limits; otherwise, the process behavior becomes unstable. In this work, steady-state experiments with a bottom-spray configuration were carried out to determine the influence of process parameters on internal nucleation rates. These investigations help to understand the nonlinear dependency of internal nucleation on process parameters and provide quantitative data of internal nucleation rates. It is shown that internal nucleation and dust integration are competitive mechanisms. Internal nucleation is enhanced by conditions that increase dust and drop concentrations in the spray resulting in agglomeration of the two disperse phases. On the other hand, parameters, for example, high binder concentration in the liquid or large granule holdup, that favor drop deposition on granules and dust integration of wet particles reduce the drop and dust concentrations and thus the internal nucleation.

[1]  Achim Kienle,et al.  A numerical bifurcation analysis of continuous fluidized bed spray granulation with external product classification , 2006 .

[2]  Michael J. Hounslow,et al.  DIRECT EVIDENCE OF HETEROGENEITY DURING HIGH-SHEAR GRANULATION , 2000 .

[3]  E. Schlünder,et al.  PARTICLE GROWTH IN A CONTINUOUSLY OPERATED FLUIDIZED BED GRANULATOR , 2001 .

[4]  E. Schlünder,et al.  Fluidized bed granulation—the importance of a drying zone for the particle growth mechanism , 1998 .

[5]  S. Rocha,et al.  Influence of Polymeric Suspension Characteristics on the Particle Coating in a Spouted Bed , 2005 .

[6]  S. Heinrich,et al.  Analysis of the start-up process in continuous fluidized bed spray granulation by population balance modelling , 2002 .

[7]  B. Köhn Elektronisches Modell zur Untersuchung mikrorechnergesteuerter Antriebe , 1985 .

[8]  George Skillas,et al.  Simulation model deployment for particulate processes in an industrial environment , 2006 .

[9]  B. J. Ennis,et al.  Nucleation, growth and breakage phenomena in agitated wet granulation processes: a review , 2001 .

[10]  Michael J. Hounslow,et al.  Studies of fluid bed granulation in an industrial R&D context , 2005 .

[11]  H. Uhlemann Kontinuierliche Wirbelschicht‐Sprühgranulation , 1990 .

[12]  James D. Litster,et al.  Growth regime map for liquid-bound granules: further development and experimental validation , 2001 .

[13]  P. Vonk,et al.  A model for the spray zone in early-stage fluidized bed granulation , 2006 .

[15]  K. Dewettinck,et al.  Numerical Spray Model of the Fluidized Bed Coating Process , 2007 .

[16]  James D. Litster,et al.  Nucleation regime map for liquid bound granules , 2003 .

[17]  Jörg Drechsler,et al.  Investigating the dynamic behaviour of fluidized bed spray granulation processes applying numerical simulation tools , 2005 .