Thin-layer modeling of microwave, microwave-convective, and microwave-vacuum drying of pharmaceutical powders

被引:44
作者
McMinn, WAM [1 ]
McLoughlin, CM [1 ]
Magee, TRA [1 ]
机构
[1] Queens Univ Belfast, Sch Chem Engn, Food Proc Engn Res Grp, Belfast BT9 5AG, Antrim, North Ireland
关键词
convective; drying; thin-layer models; microwave; pharmaceuticals; powders; vacuum;
D O I
10.1081/DRT-200054126
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
Common pharmaceutical excipients and active ingredients, wetted with specific solvents, were dried under selected microwave, microwave-convective, and microwave-vacuum conditions in an experimental drying system (2.45 GHz, 90 W). The generalized drying profile was independent of drying technique and material characteristics, with a constant rate stage and two falling rate periods being observed. Moisture removal rate was, however, dependent on the drying technique (pressure and presence/absence of external heating source), and powder and solvent properties (dielectric, physical and thermal). The experimental moisture loss data were fitted to selected semi-theoretical and empirical thin-layer drying equations. The correlations were compared according to two statistical tests, namely root mean square error and reduced chi-square. The microwave, microwave-convective, and microwave-vacuum drying behaviors were adequately represented by the Page, Logarithmic, Chavez-Mendez et al. and Midilli et al. equations, with the latter providing the best description of the experimental results.
引用
收藏
页码:513 / 532
页数:20
相关论文
共 27 条
[1]
Experimental investigations of occupied volume effect on the microwave heating and drying kinetics of cement powder in a mono-mode cavity [J].
Abdelghani-Idrissi, MA .
APPLIED THERMAL ENGINEERING, 2001, 21 (09) :955-965
[2]
[Anonymous], 1949, THESIS PURDUE U INDI
[3]
[Anonymous], ADV DRYING
[4]
Modeling of drying curves for some foodstuffs using a kinetic equation of high order [J].
ChavezMendez, C ;
SalgadoCervantes, MA ;
GarciaGalindo, HS ;
DelaCruzMedina, J ;
GarciaAlvarado, MA .
DRYING TECHNOLOGY, 1995, 13 (8-9) :2113-2122
[5]
Microwave/vacuum drying of model fruit gels [J].
Drouzas, AE ;
Tsami, E ;
Saravacos, GD .
JOURNAL OF FOOD ENGINEERING, 1999, 39 (02) :117-122
[6]
Drying of eggplant and selection of a suitable thin layer drying model [J].
Ertekin, C ;
Yaldiz, O .
JOURNAL OF FOOD ENGINEERING, 2004, 63 (03) :349-359
[7]
HENDERSON S. M., 1961, Journal of Agricultural Engineering Research, V6, P169
[8]
Determination of water content of dried fruits by drying kinetics [J].
Karathanos, VT .
JOURNAL OF FOOD ENGINEERING, 1999, 39 (04) :337-344
[9]
Comparison of convective, vacuum, and microwave drying chlorpropamide [J].
Kardum, JP ;
Sander, A ;
Skansi, D .
DRYING TECHNOLOGY, 2001, 19 (01) :167-183
[10]
Microwave vacuum drying kinetics of some fruits [J].
Kiranoudis, CT ;
Tsami, E ;
Maroulis, ZB .
DRYING TECHNOLOGY, 1997, 15 (10) :2421-2440