THE SCALE-DOWN OF AN INDUSTRIAL DISK STACK CENTRIFUGE

被引:36
作者
MANNWEILER, K
HOARE, M
机构
[1] UNIV LONDON UNIV COLL,DEPT CHEM & BIOCHEM ENGN,SERC,INTERDISCIPLINARY RES CTR,LONDON WC1E 7JE,ENGLAND
[2] WESTFALIA SEPARATOR AG,FORSCH & ENTWICKLUNG,W-4740 OELDE 1,GERMANY
来源
BIOPROCESS ENGINEERING | 1992年 / 8卷 / 1-2期
关键词
D O I
10.1007/BF00369259
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The means are described whereby a disc stack centrifuge may be scaled-down by up to 10-fold of its separation capacity. The centrifuge separation characteristics so measured are suitable for direct scale-up predictions of centrifuge performance where only small volumes of particle suspension are available for study. Such an ability to scale-down is especially important in the processing of biological particles where for example, in the early stage of process development, there is often insufficient fermentation broth for full-scale studies. Scale-down is achieved by the reduction of the number of discs available for separation purposes and by the careful positioning of these discs in the overall disc stack. A combination of dye tracer and particle separation studies are used to optimise the disc stack configuration. The resulting grade efficiency curve is an accurate reflection of the curve for the full-scale centrifuge especially in the critical design region specifying centrifuge throughput for near complete particle recovery.
引用
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页码:19 / 25
页数:7
相关论文
共 12 条
[1]  
BOHMANN H, 1974, 1ST EUR C MIX CENTR
[2]  
BRUNNER KH, 1979, THESIS U ERLANGEN GE
[3]  
BRUNNER KH, 1979, GER CHEM ENG, V2, P228
[4]  
BRUNNING P, 1987, UNPUB SCALE PROBLEME
[5]  
Daniels W., 1983, KIRK OTHMER ENCY CHE, V23, P817
[6]  
HEMFORT H, 1979, SEPARATOREN TECHNISC
[7]  
HSU HW, 1983, TECHNIQUES CHEM, V16, P380
[8]  
Levenspiel O., 1998, CHEM REACTION ENG
[9]  
Rehm HJ, 1980, IND MIKROBIOLOGIE
[10]  
SOKOLOV VJ, 1972, THEOR F CHEM ENG, V45, P1062