Colonisation of a porous sintered-glass support in anaerobic thermophilic bioreactors

Abstract Biofilm development in an open-pore sintered-glass material (SIRAN) was studied using a laboratory-scale, anaerobic fixed-film reactor under thermophilic conditions. The start-up and performance of this reactor, operating on distillery wastewater feed (vinasses), were also studied. Stepped organic loading during initial reactor start-up reduced the periods of adaptation in the colonisation process and micro-organism attachment, and biofilm formation was accelerated by the surface characteristics of the carrier. The results obtained by operating with stepped organic loading (3.81 kg COD/m3/day) over a period of 75 days suggest that a stable operation of the process (80% COD removal) and high density of biomass immobilised on the support (89.26 g VSatt/m3 SIRAN) was achieved. Epifluorescence microscopy demonstrated that, initially, attached growth developed in crevices where biomass was protected from shear forces and, finally, SIRAN was completely covered and biofilm developed on the entire SIRAN particles. The support, under anaerobic thermophilic conditions, due to its properties of low density, high porosity and specific area, is suitable for the immobilisation of slow-growing micro-organisms (e.g. anaerobic thermophilic organisms), and is especially adequate as a support for anaerobic fluidised beds for the treatment of high-rate organic loads.

[1]  W. Shieh,et al.  Effects of microcarrier pore characteristics on methanogenic fluidized bed performance , 1992 .

[2]  J. Lebrato,et al.  Influence of clay minerals, used as supports in anaerobic digesters, in the precipitation of struvite , 1992 .

[3]  E. Nyns,et al.  Starting-up of An Anaerobic Fixed-film Reactor , 1983 .

[4]  María Carmen Veiga,et al.  Start-Up, Operation, Monitoring and Control of High-Rate Anaerobic Treatment Systems , 1991 .

[5]  G. Vogels,et al.  Separation and quantification of cofactors from methanogenic bacteria by high-performance liquid chromatography: optimum and routine analyses , 1988 .

[6]  W. K. Shieh,et al.  Predicting reactor biomass concentration in a fluidized-bed system , 1981 .

[7]  W. D. Murray,et al.  Effect of Support Material on the Development of Microbial Fixed Films Converting Acetic Acid to Methane , 1981 .

[8]  J. M. Quiroga,et al.  Effect of the feed frequency on the performance of anaerobic filters. , 1995, Anaerobe.

[9]  D. Boone,et al.  Terminal Reactions in the Anaerobic Digestion of Animal Waste , 1982, Applied and environmental microbiology.

[10]  A. Knüpfer,et al.  Open-Pore Sintered Glass as a High-Efficiency Support Medium in Bioreactors: New Results and Long-Term Experiences Achieved in High-Rate Anaerobic Digestion , 1990 .

[11]  J. Bandy,et al.  A comparison of media types in acetate fed expanded-bed anaerobic reactors , 1990 .

[12]  J. Iza,et al.  Fluidized Bed Reactors for Anaerobic Wastewater Treatment , 1991 .