Affiliation:
1. Department of Chemical Technology and Biotechnological Centre, University of Amsterdam, 1018 WV Amsterdam, The Netherlands
Abstract
Anaerobic mixed-culture aggregates, which converted glucose to acetic, propionic, butyric, and valeric acids, were formed under controlled conditions of substrate feed (carbon limitation) and hydraulic regimen. The continuous-flow system used (anaerobic gas-lift reactor) was designed to retain bacterial aggregates in a well-mixed reactor. Carrier availability (i.e., liquid-suspended sand grains) proved necessary for bacterial aggregate formation from individual cells during reactor start-up. Electron microscopic examination revealed that incipient colonization of sand grains by bacteria from the bulk liquid occurred in surface irregularities, conceivably reflecting local quiescence. Subsequent confluent biofilm formation on sand grains proved to be unstable, however. Substrate depletion in the bulk liquid is assumed to weaken deeper parts of the biofilm due to cellular lysis, after which production of gas bubbles and liquid shearing forces cause sloughing. The resulting fragments, although sand free, were nevertheless large enough to be retained in the reactor and gradually grew larger through bacterial growth and by clumping together with other fragments. In the final steady state, high cell densities were maintained in the form of aggregates, while sand had virtually disappeared due to sampling losses and wash-out. Numerical cell densities within aggregates ranged from 10
12
/ml at the periphery to very low values in the center. The cells were enmeshed in a polymer matrix containing polysaccharides; nevertheless, carbon sufficiency was not a prerequisite to sustain high hold-up ratios.
Publisher
American Society for Microbiology
Subject
Ecology,Applied Microbiology and Biotechnology,Food Science,Biotechnology
Reference34 articles.
1. Scanning electron microscope evaluation of rotating biological contactor biofilm;Afleman J. E.;Water Res.,1982
2. Atkinson B 1981. Immobilized biomass-a basis for process development in wastewater treatment p. 22-34. In P. F. Cooper and B. Atkinson (ed.) Biological fluidised bed treatment of water and wastewater. Ellis Horwood Chichester U.K.
3. Biological particles of given size, shape, and density for use in biological reactors;Atkinson B.;Biotechnol. Bioeng.,1979
4. Biofilms and microbial fouling;Characklis W. G.;Adv. Appl. Microbiol.,1983
5. Influence of phase separation on the anaerobic digestion of glucose. I. Maximum COD-turnover rate during continuous operation;Cohen A.;Water Res.,1980
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