Microagglomeration of pulverized pharmaceutical powders using the Wurster process I. Preparation of highly drug-incorporated, subsieve-sized core particles for subsequent microencapsulation by film-coating

被引:17
作者
Ichikawa, H [1 ]
Fukumori, Y [1 ]
机构
[1] Kobe Gakuin Univ, Fac Pharmaceut Sci, Nishi Ku, Kobe 6512180, Japan
关键词
acrylic polymer; agglomeration; core particle; Eudragit (R) RS30D; film-coating; Wurster process; microencapsulation;
D O I
10.1016/S0378-5173(99)00006-X
中图分类号
R9 [药学];
学科分类号
1007 ;
摘要
A novel agglomeration process of pulverized pharmaceutical powders into subsieve-sized agglomerates (microagglomeration) was designed for manufacturing highly drug-incorporated core particles for subsequent microencapsulation by film-coating. The microagglomeration of pulverized phenacetin powder, whose mass median diameter was 9 mu m, was performed by spraying an aqueous colloidal dispersion of acrylic polymer, Eudragit(R) RS30D, as a binding/coating agent using a spouted bed assisted with a draft tube (the Wurster process), and the effect of process variables was examined. An appropriate spray liquid flow rate made it possible to produce microagglomerates of 20-50 mu m with 60% yield. However, 10% of the product still survived as particles smaller than 10 mu m even at the elevated liquid flow rate. In contrast, the survived particles smaller than 10 mu m tended to be predominantly reduced to 2%, while coarse agglomerates larger than 53 mu m were not excessively produced, by additionally setting a fixed bed of glass beads in the spouted bed apparatus. The length of the draft tube influenced compaction of the agglomerates as well as their surface-smoothening. Equipping the fixed bed of the glass beads and the long draft tube in the spouted bed allowed us to prepare microagglomerates of 20-50 mu m at yield of 55% applicable as highly drug-incorporated, free-flowing, surface-smoothed, narrowly size-distributed core particles for subsequent microencapsulation by film-coating. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:195 / 210
页数:16
相关论文
共 46 条
[11]  
GHEBRESELLASSIE I, 1989, PHARM PELLETIZATION
[12]  
ICHIKAWA H, 1993, CHEM PHARM BULL, V41, P1132
[13]  
ICHIKAWA H, 1994, CHEM PHARM BULL, V42, P1308
[14]  
IJICHI K, 1996, J SOC POWDER TECHNOL, V33, P706
[15]   THE FLOW OF SOLID PARTICLES IN AN AERATED INCLINED CHANNEL [J].
ISHIDA, M ;
HATANO, H ;
SHIRAI, T .
POWDER TECHNOLOGY, 1980, 27 (01) :7-12
[16]   AIR SUSPENSION COATING FOR MULTIPARTICULATES [J].
JONES, D .
DRUG DEVELOPMENT AND INDUSTRIAL PHARMACY, 1994, 20 (20) :3175-3206
[17]   RESIDENCE TIME DISTRIBUTION OF FINE PARTICLES IN A POWDER-PARTICLE FLUIDIZED-BED [J].
KATO, K ;
TAKARADA, T ;
MATSUO, N ;
SUTO, T ;
NAKAGAWA, N .
KAGAKU KOGAKU RONBUNSHU, 1991, 17 (05) :970-975
[18]   GRANULATION - A REVIEW OF PHARMACEUTICAL WET-GRANULATION [J].
KRISTENSEN, HG ;
SCHAEFER, T .
DRUG DEVELOPMENT AND INDUSTRIAL PHARMACY, 1987, 13 (4-5) :803-872
[19]  
LEU LP, 1994, AICHE S SER, V90, P124
[20]  
LIU CH, 1994, DRUG DEV IND PHARM, V20, P1911