Liquid mixing and solid segregation in high-solid anaerobic digesters.

An experimental procedure (Residence Time Distribution technique) was used to characterize the macro-mixing of both liquid and solid phases of a laboratory-scale dry anaerobic digester using appropriate tracers. The effects of the waste origin and total solid content were studied. An increase in TS content from 22% to 30% TS (w/w) induced a macro-mixing mode closer to a theoretical Plug Flow Reactor. The segregation of particles having different densities was investigated regarding the RTD of the solid phase. Segregation of dense particles occurred at low TS content. By using different TS content and waste origins, it was also determined that the yield stress was a key parameter in the mechanism of segregation. At high yield stress, dense particles were more stable and thus less subjected to settling. As a consequence, operating at high TS content may permit to prevent the sedimentation of the denser particles.

[1]  Renaud Escudié,et al.  Liquid mixing and gas–liquid mass transfer in a three-phase inverse turbulent bed reactor , 2005 .

[2]  Hiroshi Takahashi,et al.  CFD simulation of mixing in anaerobic digesters. , 2009, Bioresource technology.

[3]  A. D. Martin,et al.  Interpretation of residence time distribution data , 2000 .

[4]  Renaud Escudié,et al.  Hydrodynamic and biokinetic models of an anaerobic fixed-bed reactor , 2005 .

[5]  Joan Mata-Álvarez,et al.  Anaerobic digestion of organic solid wastes. An overview of research achievements and perspectives , 2000 .

[6]  R. Escudié,et al.  Influence of moisture content on the specific methanogenic activity of dry mesophilic municipal solid waste digestate , 2012 .

[7]  Chettiyappan Visvanathan,et al.  Bio-energy recovery from high-solid organic substrates by dry anaerobic bio-conversion processes: a review , 2013, Reviews in Environmental Science and Bio/Technology.

[8]  P. Battistoni Pre-treatment, measurement execution procedure and waste characteristics in the rheology of sewage sludges and the digested organic fraction of municipal solid wastes , 1997 .

[9]  É. Latrille,et al.  Water distribution in biowastes and digestates of dry anaerobic digestion technology , 2011 .

[10]  L. Nies,et al.  Research advances in dry anaerobic digestion process of solid organic wastes. , 2011 .

[11]  Yebo Li,et al.  Solid-state anaerobic digestion for methane production from organic waste , 2011 .

[12]  J. Bollon Etude des mécanismes physiques et de leur influence sur la cinétique de méthanisation en voie sèche : essais expérimentaux et modélisation , 2012 .

[13]  P. Rossi,et al.  Contribution of granular interactions to self compacting concrete stability: Development of a new device , 2009 .

[14]  Binxin Wu,et al.  CFD simulation of mixing for high‐solids anaerobic digestion , 2012, Biotechnology and bioengineering.

[15]  Renaud Escudié,et al.  Total solids content drives high solid anaerobic digestion via mass transfer limitation. , 2012, Bioresource technology.

[16]  J. Steyer,et al.  Rapid measurement of the yield stress of anaerobically-digested solid waste using slump tests. , 2011, Waste management.

[17]  O. Levenspiel Chemical Reaction Engineering , 1972 .

[18]  R. Escudié,et al.  Influence of substrate concentration and moisture content on the specific methanogenic activity of dry mesophilic municipal solid waste digestate spiked with propionate. , 2011, Bioresource technology.

[19]  Paolo Battistoni,et al.  Feed Characteristics and Digester Operative Conditions as Parameters Affecting the Rheology of Digested Municipal Solid Wastes , 1993 .

[20]  P. Buffière,et al.  Measurement of diffusion coefficients in dry anaerobic digestion media , 2013 .