FLUID BED TECHNOLOGY: OVERVIEW AND PARAMETERS FOR PROCESS SELECTION

Formulation development is the most emerging and upcoming face of pharmaceutical technology in the current era. It is contemporarily capturing the market leaps and bounds with recent trends and developments with its innovative techniques. The day-to-day advancements in the research have provided an edge to this brilliant branch of pharmaceutical sector for not only uplifting the pharmacy profession but also to conquer the diseased state for nurturing the health and humanity. The fluid-bed technology or air-suspension process is the potential tool to develop newer trends and implications in the sector of formulation development with maximum therapeutic efficacy. The technology is used for granulation/agglomeration, layering and coating of a wide range of particle size. In addition; the technique can be used for the drying process as well. The three patterns of the fluid-bed processes could be characterized by the position/location of the spray nozzle i.e. top spray, bottom spray or tangential spray. This article reviews the three techniques with some innovative fluid bed pelletizing technologies like CPS™, MicroPx™, ProCell™ and discusses their applications, advantages and limitations. These advanced pelletizing technologies are recentely added to complement the actual capabilities of standard fluid bed processing for development of various dosage forms of “Multiple Unit Particulate Systems” (MUPS) with better therapeutic efficacy and economic benefits.

[1]  J. Kristensen Direct pelletization in a rotary processor controlled by torque measurements. III. Investigation of microcrystalline cellulose and lactose grade , 2005, AAPS PharmSciTech.

[2]  P. Kleinebudde,et al.  Direct pelletization in a rotary processor controlled by torque measurements. II: Effects of changes in the content of microcrystalline cellulose , 2000, AAPS PharmSci.

[3]  J. Rantanen,et al.  The characterization of fluidization behavior using a novel multichamber microscale fluid bed. , 2004, Journal of pharmaceutical sciences.

[4]  C. Liew,et al.  Wet Spheronization by Rotary Processing—A Multistage Single‐Pot Process for Producing Spheroids , 2004, Drug development and industrial pharmacy.

[5]  E. Vázquez,et al.  Optimization of Drying-End-Points Measurements for the Automation of a Fluidized-Bed Dryer Using FT-NIR Spectroscopy , 2004 .

[6]  M. Aulton Pharmaceutics : the science of dosage form design , 2002 .

[7]  P. Sojka,et al.  Effervescent Atomization of Aqueous Polymer Solutions and Dispersions , 2001, Pharmaceutical development and technology.

[8]  Peter Kleinebudde,et al.  Direct Pelletization in a Rotary Processor Controlled by Torque Measurements. I. Influence of Process Variables , 2000, Pharmaceutical development and technology.

[9]  R. Kinget,et al.  The influence of five selected processing and formulation variables on the particle size, particle size distribution, and friability of pellets produced in a rotary processor , 1997 .

[10]  D. Parikh,et al.  Application of Powder-Layering Technology and Film Coating for Manufacture of Sustained-Release Pellets Using a Rotary Fluid Bed Processor , 1997 .

[11]  Kei Miyanami,et al.  Scale-Up of Agitation Fluidized Bed Granulation. I. Preliminary Experimental Approach for Optimization of Process Variables , 1995 .

[12]  A. Sakr,et al.  Evaluation of rotary fluidized-red as a wet granulation equipment , 1995 .

[13]  R. G. Hollenbeck,et al.  MANUFACTURE OF SPHERICAL ACETAMINOPHEN PELLETS : COMPARISON OF ROTARY PROCESSING WITH MULTIPLE-STEP EXTRUSION AND SPHERONIZATION , 1991 .

[14]  Banks Michael,et al.  Fluidised-Bed Granulation: A Chronology , 1991 .

[15]  N. G. Popovich,et al.  Pharmaceutical Dosage Forms and Drug Delivery Systems , 1990 .

[16]  S. H. Fox The Theory and Practice of Industrial Pharmacy , 1970 .