Nucleation and growth rates of poly(L-lactic acid) microparticles during precipitation with a compressed-fluid antisolvent

被引:26
作者
Jarmer, DJ
Lengsfeld, CS
Randolph, TW [1 ]
机构
[1] Univ Colorado, Ctr Pharmaceut Biotechnol, Dept Chem & Biol Engn, Boulder, CO 80309 USA
[2] Univ Denver, Dept Engn, Denver, CO 80208 USA
关键词
D O I
10.1021/la049912v
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
We measured nucleation and growth rates of poly(L-lactic acid) (PLLA) microparticles produced during precipitation with a compressed-fluid antisolvent (PCA). The injector/precipitator used in this study satisfied the constraints and assumptions incorporated in the development of the mixed-suspension, mixed-product-removal population balance theory. A semicontinuous operation mode with batch product filtering was developed, and results from product particle size distributions allowed nucleation and growth rates to be determined through the use of population balances. Kinetic data, obtained by operating the precipitator under various degrees of supersaturation and suspension density, were used to generate a nucleation rate model for PLLA. Model results indicate a relative kinetic order of 1 and a linear dependence of the nucleation rate on the suspension density. First-order dependence of the nucleation rate on suspension density suggests secondary nucleation mechanism(s) are operative within this PCA flow system and may explain the relative insensitivity of particle size distributions to changes in PCA operating conditions.
引用
收藏
页码:7254 / 7264
页数:11
相关论文
共 63 条
[1]  
Allen T., 1981, PARTICLE SIZE MEASUR, V3rd
[2]   A FLUID MECHANICAL APPROACH TO TURBULENT MIXING AND CHEMICAL REACTION PART I INADEQUACIES OF AVAILABLE METHODS [J].
Baldyga, J. ;
Bourne, J. R. .
CHEMICAL ENGINEERING COMMUNICATIONS, 1984, 28 (4-6) :231-241
[3]   INTERACTIONS BETWEEN MIXING ON VARIOUS SCALES IN STIRRED TANK REACTORS [J].
BALDYGA, J ;
BOURNE, JR .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (08) :1839-1848
[4]   SIMPLIFICATION OF MICROMIXING CALCULATIONS .1. DERIVATION AND APPLICATION OF NEW MODEL [J].
BALDYGA, J ;
BOURNE, JR .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1989, 42 (02) :83-92
[5]   MIXING-PRECIPITATION MODEL WITH APPLICATION TO DOUBLE FEED SEMIBATCH PRECIPITATION [J].
BALDYGA, J ;
PODGORSKA, W ;
POHORECKI, R .
CHEMICAL ENGINEERING SCIENCE, 1995, 50 (08) :1281-1300
[6]   INVESTIGATION OF MIXING IN JET REACTORS USING FAST, COMPETITIVE CONSECUTIVE REACTIONS [J].
BALDYGA, J ;
BOURNE, JR ;
ZIMMERMANN, B .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (12) :1937-1946
[7]  
Baldyga J., 1999, TURBULENT MIXING CHE
[8]   CONTACT NUCLEATION OF MGSO4.7H2O IN A CONTINUOUS MSMPR CRYSTALLIZER [J].
BAUER, LG ;
LARSON, MA ;
DALLONS, VJ .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (05) :1253-1261
[9]   INFLUENCE OF CRYSTAL SIZE ON RATE OF CONTACT NUCLEATION IN STIRRED-TANK CRYSTALLIZERS [J].
BAUER, LG ;
ROUSSEAU, RW ;
MCCABE, WL .
AICHE JOURNAL, 1974, 20 (04) :653-659
[10]  
BENNETT RC, 1973, CHEM ENG PROG, V69, P86