Velocity Field Visualization in USP Dissolution Apparatus 3 Using Particle Image Velocimetry

被引:7
作者
Perivilli, Satish [1 ]
Prevost, Richard [2 ]
Stippler, Erika [1 ]
机构
[1] US Pharmacopeial Convent Inc, 12601 Twinbrook Pkwy, Rockville, MD 20852 USA
[2] LaVision Inc, 211 W Michigan Ave,Suite 100, Ypsilanti, MI 48197 USA
关键词
hydrodynamics; particle image velocimetry; USP dissolution apparatus 3; FLUID; HYDRODYNAMICS; RELEASE;
D O I
10.1007/s11095-017-2151-1
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The hydrodynamics in USP dissolution apparatus 3, at five different dip rates, was characterized by analyzing phase-averaged velocity fields obtained using Particle Image Velocimetry (PIV). Phase locked 2 Component-PIV (2C-PIV) measurements were recorded on a typical dissolution apparatus 3 configuration with a black painted tablet fixed at the center of the bottom porous screen of the reciprocating cylinder. A trigger mechanism was employed to capture data over 12 phase positions for each reciprocation cycle. Data were captured over a fixed number of cycles, based on dip rate, and the resultant images were post-processed to obtain phase-averaged velocity fields at each phase. For all dip rates studied, the sinusoidal nature of the cylinder's reciprocating motion was evident in the images. The phase positions, in which the cylinder was completely submerged, were characterized by recirculation of liquid through the cylinder, top fitting cap, vessel-cylinder annulus, and bottom fitting cap. The direction of recirculation was opposite for phase positions during the up- and downstrokes. The end positions of the up- and downstrokes were characterized by vortices below and above the cylinder respectively. Increasing dip rates led mainly to increasing velocity magnitudes while all flow characteristics, in general, were retained. The hydrodynamics in typical USP dissolution apparatus 3 is characterized by cyclic phase-dependent flow fields. Specifically, the velocity field distribution within dissolution apparatus 3 is greatly influenced by the relative position of the top cap to the liquid level in the cylinder.
引用
收藏
页码:1330 / 1337
页数:8
相关论文
共 19 条
[1]  
ADRIAN RJ, 1991, ANNU REV FLUID MECH, V23, P261, DOI 10.1146/annurev.fluid.23.1.261
[2]  
[Anonymous], 2016, E1116 ASTM
[3]   Hydrodynamic investigation of USP dissolution test apparatus II [J].
Bai, Ge ;
Armenante, Piero M. ;
Plank, Russell V. ;
Gentzler, Michael ;
Ford, Kenneth ;
Harmon, Paul .
JOURNAL OF PHARMACEUTICAL SCIENCES, 2007, 96 (09) :2327-2349
[4]   Velocity profiles and shear strain rate variability in the USP Dissolution Testing Apparatus 2 at different impeller agitation speeds [J].
Bai, Ge ;
Wang, Yimin ;
Armenante, Piero M. .
INTERNATIONAL JOURNAL OF PHARMACEUTICS, 2011, 403 (1-2) :1-14
[5]   FLUID AND PARTICLE LASER DOPPLER VELOCITY-MEASUREMENTS AND MASS-TRANSFER PREDICTIONS FOR THE USP PADDLE METHOD DISSOLUTION APPARATUS [J].
BOCANEGRA, LM ;
MORRIS, GJ ;
JUREWICZ, JT ;
MAUGER, JW .
DRUG DEVELOPMENT AND INDUSTRIAL PHARMACY, 1990, 16 (09) :1441-1464
[6]  
BORST I, 1997, DISSOLUT TECHNOL, V4, P11, DOI DOI 10.14227/DT040197P11
[7]  
Hammad KJ, 2001, P 2001 ASME INT MECH
[8]   The effects of buffer molarity, agitation rate, and mesh size on verapamil release from modified-release mini-tablets using USP apparatus 3 [J].
Khamanga, Sandile M. M. ;
Walker, Roderick B. .
DISSOLUTION TECHNOLOGIES, 2007, 14 (02) :19-23
[9]   Engineering tools for understanding the hydrodynamics of dissolution tests [J].
Kukura, J ;
Arratia, PE ;
Szalai, ES ;
Muzzio, FJ .
DRUG DEVELOPMENT AND INDUSTRIAL PHARMACY, 2003, 29 (02) :231-+
[10]  
Kukura J., 2002, Pharmaceutical Technology North America, V26, P48