Combined sulfite method for the measurement of the oxygen transfer coefficient kLa in bioreactors

被引:34
作者
Puskeiler, R [1 ]
Weuster-Botz, D [1 ]
机构
[1] Tech Univ Munich, Lehrstuhl Bioverfahrenstech, D-85748 Garching, Germany
关键词
biochemical engineering; bioreactors; mass transfer; scale-up; dynamic sulfite method; steady-state sulfite method;
D O I
10.1016/j.jbiotec.2005.06.016
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 combined sulfite method is proposed for the measurement of oxygen transfer coefficients, k(L)a, in bioreactors. The method consists of a steady-state and a dynamic measurement which are carried out under the same experimental conditions and thus yield data for both methods during one experiment. The applied experimental conditions are shown to avoid chemical enhancement during the steady-state measurement. Moreover, no parallel sulfite oxidation occurs during the oxygen saturation phase of the dynamic measurement. Under the applied experimental conditions, no information about the sulfite oxidation kinetics is required and possible metal ion impurities in sulfite salts do not influence the measurement. The characterization of a laboratory-scale bioreactor aerated with pure oxygen yields k(L)a values during the steady-state and the dynamic measurements that are in good agreement with the dynamic pressure method, the correctness of which is generally accepted. When air is used for absorption, the steady-state measurement yields kLa values that correlate to the correct variant of the standard dynamic method. The dynamic measurement with air absorption yields a k(L)a value which considers the influence of the non-uniform bubble size distribution present in bubble-aerated bioreactors. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:430 / 438
页数:9
相关论文
共 13 条
[1]   Performance of agitated gas-liquid contactors [J].
Cooper, CM ;
Fernstrom, GA ;
Miller, SA .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1944, 36 :504-509
[2]   EFFECT OF SURFACE AERATION ON SCALE-UP PROCEDURES FOR FERMENTATION PROCESSES [J].
FUCHS, R ;
RYU, DDY ;
HUMPHREY, AE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (02) :190-&
[3]   Multiple-impeller systems with a special emphasis on bioreactors: a critical review [J].
Gogate, PR ;
Beenackers, AACM ;
Pandit, AB .
BIOCHEMICAL ENGINEERING JOURNAL, 2000, 6 (02) :109-144
[4]   Chemical dynamic method for measuring kLa in gas-liquid dispersions [J].
Havelka, P ;
Moucha, T ;
Sinkule, J ;
Linek, V .
CHEMICAL ENGINEERING COMMUNICATIONS, 1998, 168 :97-110
[5]   A SIMPLE NA2SO3 FEEDING METHOD FOR KLA MEASUREMENT IN LARGE-SCALE FERMENTERS [J].
IMAI, Y ;
TAKEI, H ;
MATSUMURA, M .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 29 (08) :982-993
[6]   CRITICAL-ASSESSMENT OF THE STEADY-STATE NA2SO3 FEEDING METHOD FOR KLA MEASUREMENT IN FERMENTORS [J].
LINEK, V ;
BENES, P ;
SINKULE, J .
BIOTECHNOLOGY AND BIOENGINEERING, 1990, 35 (08) :766-770
[7]   CHEMICAL-ENGINEERING USE OF CATALYZED SULFITE OXIDATION-KINETICS FOR THE DETERMINATION OF MASS-TRANSFER CHARACTERISTICS OF GAS-LIQUID CONTACTORS [J].
LINEK, V ;
VACEK, V .
CHEMICAL ENGINEERING SCIENCE, 1981, 36 (11) :1747-1768
[8]   A CRITICAL-REVIEW AND EXPERIMENTAL-VERIFICATION OF THE CORRECT USE OF THE DYNAMIC METHOD FOR THE DETERMINATION OF OXYGEN-TRANSFER IN AERATED AGITATED VESSELS TO WATER, ELECTROLYTE-SOLUTIONS AND VISCOUS-LIQUIDS [J].
LINEK, V ;
VACEK, V ;
BENES, P .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1987, 34 (01) :11-34
[9]   DYNAMIC PRESSURE METHOD FOR KLA MEASUREMENT IN LARGE-SCALE BIOREACTORS [J].
LINEK, V ;
BENES, P ;
VACEK, V .
BIOTECHNOLOGY AND BIOENGINEERING, 1989, 33 (11) :1406-1412
[10]   MEASUREMENT OF K(L)A BY DYNAMIC PRESSURE METHOD IN PILOT-PLANT FERMENTOR [J].
LINEK, V ;
MOUCHA, T ;
DOUSOVA, M ;
SINKULE, J .
BIOTECHNOLOGY AND BIOENGINEERING, 1994, 43 (06) :477-482