Using experimental design to optimize the process parameters in fluidized bed granulation

被引:44
作者
Rambali, B
Baert, L
Thoné, D
Massart, DL
机构
[1] Free Univ Brussels, Farmaceut Inst, B-1090 Brussels, Belgium
[2] Janssen Res Fdn, B-2340 Beerse, Belgium
关键词
granulation process; fluid bed; geometric mean granule diameter; experimental design; Plackett Burman design; fractional factorial design;
D O I
10.1081/DDC-100000127
中图分类号
R914 [药物化学];
学科分类号
100701 ;
摘要
In this study many parameters were screened for a small-scale granulation process for their effect on the yield of granules between 75 and 500 mum and the geometrical granule mean size (d50). First a Plackett-Burman design was applied to screen the inlet air temperature, the inlet flow rate, the spray rate, the nozzle air pressure, the nozzle spray diameter; and the nozzle position. The Plackett-Burman design showed that the key process parameters were the inlet flow rate and the spray rate and probably also the inlet air temperature. Afterward a fractional factorial design (2(5-2)) was applied to screen the remaining parameters plus the nozzle aircap position and the spraying time interval. The functional factorial design showed that the nozzle air pressure was also important As the target values for the granule yield (between 75 and 500 mum) and the geometric mean granule size (between 300 and 500 mum) were reached during the screening experiments, further optimization was not considered necessary.
引用
收藏
页码:47 / 55
页数:9
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