NON-STATIONARY DRYING KINETICS IN A BATCH PHARMACEUTICAL FLUIDIZED BED COATING PROCESS

REFERENCES

• Adetayo , A. A. , Litster , J. D. , Pratsinis , S. E. , & Ennis , B. J. ( 1995 ). Population balance modelling of drum granulation of materials with wide size distribution. Powder Technol. , 82 . 37 – 49 .
   Web of Science ®Google Scholar
• Becher , R. D. ( 1997 ). Untersuchung der Agglomeration von Partikeln bei der Wirbelschicht-Spruhgranulation. VDI-Forrschrirt-Berichte Reihie , 3 , No. 500 . VDI Verlag, Dusseldorf , Germany .
   Google Scholar
• Ennis , B. J. , Tardos , G. T. , & Pfeffer , R. ( 1991 ). A microlevel-based characterization of granulation phenomena. Powder Technol. , 65 . 257 – 272 .
   Web of Science ®Google Scholar
• Ennis , B. J. , Gabriel , J. L. , Tardos , G. T. , & Pfeffer , R. (1990). The influence of viscosity on the strength of an axially strained pendular liquid bridge. Chem. Eng. Sci. , 45. 3071–3088.
   Web of Science ®Google Scholar
• Groenewold , H. , & Tsotsas , E. ( 1998 ). Predicting apparent Shenvood numbers for fluidized beds. Proceedings of the 11th International Drying Symposium (IDS'98). , 19 – 22 . 8 . 1998, Halkidiki , Greece , vol. A, (pp. 192-199).
   Google Scholar
• Heinrich , S. , & Morl , L. ( 1999 a). Fluidized bed spray granulation - A new model for the description of particle wetting and of temperature and concentration distribution. Chem. Eng. Process. , 38 , 635 – 663 .
   Web of Science ®Google Scholar
• Heinrich , S. , & Morl , L. ( 1999 b). Description of the temperature, humidity and concentration distribution in gas-liquid-solid fluidized beds. Chem. Eng. Technol. , 22 ( 2 ). 118 – 122 .
   Web of Science ®Google Scholar
• Hogekamp , S. ( 1997 ). Uber eine modifizierte Strahlagglomerationsanlage zur Herstellung schnell dispergierbarer Pulver. PhD thesis , Universitat Karlsruhe, Germany .
   Google Scholar
• Kasl , W. , & Klan , H. ( 1994 ). Warmeiibergang durch freie Konvektion an umstromten Korpern. VDI-Warmeatlas (vol 7). Absatz Fal-Fa7 , VD1-Verlag. Dusseldorf . Germany .
   Google Scholar
• Kawei , S. ( 1993 ). Granulation and drying or powdery of liquid materials by fluidized bed technology. Drying Technology. , 4 , 719 – 731 .
   Google Scholar
• Link , K. C. ( 1997 ). Untersuchung der Granulatbildung an einer frei schwebenden Einzelpartikel. VDI-Forrschrill-Bericllte Reihe , 3 . No. 491 , VDI Verlag, Dusseldorf , Germany .
   Google Scholar
• Morl , L. ( 1981 ). Anwendungsmoglichkeiten und Berechnung von Wirbelschicht-granulationstrocknungsanlagen. PhD Thesis B , TH Magdeburg . Germany .
   Google Scholar
• Moseley , J. L. , & O'Brien T. J. ( 1993 ). Model for agglomeration in a fluidized bed. Chem. Eng. Sci. , 17 , 3043 – 3050 .
   Google Scholar
• Seville , J. P. K. , Silomon–Pflug , H. , & Knight , P. C. ( 1998 ). Modelling of sintering in high temperature gas fluidisation. Powder Technol. , 97 . 160 – 169 .
   Google Scholar
• Shi , D. ( 1997 ). Fluiddynamik und Warmeubergang in einer zirkulierenden Wirbelschicht. VDI-For1scliri11-Bericlife Reihe , 3 , 466 . VDI Verlag, Dusseldorf , Germany .
   Google Scholar
• Simons , S. J. R. ( 1996 ). Modelling of agglomerating systems: from spheres to fractals. Powder Technol. , 87 , 29 – 41 .
   Web of Science ®Google Scholar
• Simons , S. J. R. , Seville , J. P. K. , & Adams , M. J. ( 1994 ). An analysis of the rupture energy of pcndular liquid bridges. Chem. Eng. Sci. , 49 , 2331 – 2339 .
   Google Scholar
• Turton , R. , Tardos , G. T. , & Ennis , B. J. (1999). Fluidized bed coating and granulation. Fluidisarion Solid Handling and Processing. , 331–434.
   Google Scholar
• Villadsen , J. , & Michelson , M. L. ( 1978 ). Solutions of differential equation models by polynomial approximation. , Prentice-Hall, Englewood Cliffs .
   Google Scholar