Methane yield as a monitoring parameter for the start-up of anaerobic fixed film reactors.

This paper describes the variation of the methane yield during the start-up period of an anaerobic fluidized bed reactor. After a lag phase, with acclimatized sludge, the methane yield increased with time during biofilm development up to the theoretical steady yield value, reported to be around 0.351 CH4/g CODdeg. The establishment of the biofilm required a high consumption of organic material through the microbial synthesis (anabolism), thereby reducing the proportion of substrate converted to methane. As a result, this yield could be an indirect metabolic parameter for evaluating a start-up operation. It could provide vital information about bacterial fixation processes and is easy to be applied to any biofilm reactor, such as anaerobic filters, where biomass sampling is impracticable. Monitoring this parameter could also give useful dynamic information about the different steps of colonization and biomass attachment, which could be used to improve the start-up performance.

[1]  G. Zellner,et al.  Start-up and operation of a propionate-degrading fluidized-bed reactor , 1992, Applied Microbiology and Biotechnology.

[2]  Shui-Jen Chen,et al.  Performance evaluation of the anaerobic fluidised bed system: I. Substrate utilisation and gas production , 1985 .

[3]  R. Moletta,et al.  THE INVERSE TURBULENT BED: A NOVEL BIOREACTOR FOR ANAEROBIC TREATMENT , 2000 .

[5]  Attilio Converti,et al.  Semi-continuous anaerobic digestion of a food industry wastewater in an anaerobic filter , 2000 .

[6]  L. Gorris,et al.  Early stages in biofilm development in methanogenic fluidized-bed reactors , 1990, Applied Microbiology and Biotechnology.

[7]  G. Vogels,et al.  Influence of waste water composition on biofilm development in laboratory methanogenic fluidized bed reactors , 1988, Applied Microbiology and Biotechnology.

[8]  Rafael Borja,et al.  Kinetics of methane production from wine distillery wastewater in an immobilised cell bioreactor using sepiolite as support medium , 1994 .

[9]  M. Moo-young,et al.  Biotechnology and renewable energy , 1986 .

[10]  M. Balaguer,et al.  A Comparison of Different Support Materials in Anaerobic Fluidized Bed Reactors for the Treatment of Vinasse , 1997 .

[11]  C. Banks,et al.  Kinetics of anaerobic digestion of soft drink wastewater in immobilized cell bioreactors. , 1994, Journal of chemical technology and biotechnology.

[12]  R. Moletta,et al.  Some hydrodynamic characteristics of inverse three phase fluidized-bed reactors , 1999 .

[13]  D. nd,et al.  Anaerobic filter treatment of pharmaceutical waste. , 1975 .

[14]  Shui-Jen Chen,et al.  Anaerobic fluidized bed treatment of an industrial wastewater , 1988 .

[15]  J. Audic,et al.  Influence of Seeding Conditions on Initial Biofilm Development during the Startup of Anaerobic Fluidized Bed Reactors , 1989 .

[16]  William G. Characklis,et al.  Dynamics of biofilm processes , 1982 .

[17]  R. Chamy,et al.  Design and Startup of an Anaerobic Fluidized Bed Reactor , 1999 .

[18]  Diego Sales,et al.  Colonisation of a porous sintered-glass support in anaerobic thermophilic bioreactors , 1997 .

[19]  W. Shieh,et al.  Startup of anaerobic fluidized bed reactors with acetic acid as the substrate , 1993, Biotechnology and bioengineering.

[20]  A. Lauwers,et al.  Fast start-up of methanogenic fluidized bed reactors by control of organic load and composition. , 1990 .