DETERMINATION OF VOLUMETRIC OXYGEN-TRANSFER COEFFICIENT BY OFF-GAS ANALYSIS

Citation
K. Fujie et al., DETERMINATION OF VOLUMETRIC OXYGEN-TRANSFER COEFFICIENT BY OFF-GAS ANALYSIS, Journal of fermentation and bioengineering, 77(5), 1994, pp. 522-527
Citations number
13
Categorie Soggetti
Food Science & Tenology","Biothechnology & Applied Migrobiology
ISSN journal
0922338X
Volume
77
Issue
5
Year of publication
1994
Pages
522 - 527
Database
ISI
SICI code
0922-338X(1994)77:5<522:DOVOCB>2.0.ZU;2-3
Abstract
In various aerobic bioreactors including activated sludge aeration tan ks, the volumetric mass transfer coefficient K(L)a is frequently used as an estimate of the rate of oxygen dissolution into the liquid phase . The K(L)a measurement in such-bioreactors is widely applied with the aid of sodium sulfite (Na2SO3) as an oxygen-consuming substance used to maintain low dissolved oxygen concentration. In the present study, the effect of the addition of Na2SO3 on K(L)a, determined by an off-ga s analysis, was investigated specifically from the viewpoint of variat ions in the size of air bubbles and the enhancement factor associated with the change in sulfite concentration. Experiments were conducted i n a draft-tube bubble column, using a zirconia electrode oxygen analyz er for measurement of the O2 mole fraction in the exhaust gas and a du al electrical resistivity probe for measurement of the bubble size. It was found that the increase in the specific gas-liquid interfacial ar ea, resulting from bubble size reduction effected by Na2SO3 functionin g as an electrolyte, is more pronounced than the enhancement of the ab sorption rate through the interface. The upper limit of Na2SO3 concent ration for sustaining physical absorption, in the absence of any catal yst, ranges from 30 to 70 mol/m3, while that for preventing the averag e bubble size from decreasing is about 15 mol/m3. Furthermore, to secu re a reliable K(L)a measurement, the K(L)a value should not exceed 50 h-1 for the liquid depth of 3 m even when the limiting conditions are not exceeded. The off-gas analysis proposed in this study for K(L)a de termination is expected to be extremely useful provided that the above conditions are fulfilled, since it only requires moderate addition of the sulfite as the oxygen-consuming substance and will not interrupt the reactor operation as long as oxygen uptake occurs in the system.