2012
DOI: 10.1002/elsc.201100062
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The influence of the temperature regime on the formation of methane in a two‐phase anaerobic digestion process

Abstract: The influence of different temperature levels on the formation of methane in a two‐phase anaerobic digestion process using rye silage and barley straw as feedstocks was investigated in this study. This process comprised a leach‐bed reactor (LBR), a reservoir for leachate from the LBR, and a separate downstream fixed‐film anaerobic filter (AF), with immobilized micro biocoenosises. The degree of degradation of the volatile solids was similar in both studies and was almost equal at 75 Ma.‐%VS. When both reactor … Show more

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Cited by 26 publications
(9 citation statements)
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“…For each reactor system and for each process temperature, two replicates were conducted in parallel, denominated further as biological replicates. Further process details were as previously published by [3].…”
Section: Reactor Set-up and Samplingmentioning
confidence: 99%
See 1 more Smart Citation
“…For each reactor system and for each process temperature, two replicates were conducted in parallel, denominated further as biological replicates. Further process details were as previously published by [3].…”
Section: Reactor Set-up and Samplingmentioning
confidence: 99%
“…To digest crop biomass as sole substrate and at high organic loading rates (OLRs), specially designed biogas reactors are advantageous such as staged degradation step ('phase') separated reactor systems consisting of a cellulolysis / hydrolysis fermenter and a downstream methanogenesis reactor. Compared to single phase reactors, these two-stage two-phase reactors possess several advantages, for example, the more stable operation (under particular process conditions) combined with higher bioenergy yields [2][3][4][5][6].…”
Section: Introductionmentioning
confidence: 99%
“…Partner A operated two mesophilic (37 °C) and two thermophilic (55 °C) two-stage two-phase biogas fermenter systems. The principle of the reactor set up was described in detail by Schönberg and Linke [ 20 ]. Each system consisted of one hydrolysis reactor (HR), one percolate (process fluid) storage tank and one anaerobic filter compartment.…”
Section: Methodsmentioning
confidence: 99%
“…The pH value was measured prior to feeding. The contents of total solids (TS), volatile solids (VS), volatile fatty acids (VFA, acetic, propionic, (i)-butyric, (i)-valeric, and caproic acids), total Kjeldahl nitrogen (TKN), and total ammonium nitrogen (TAN) were analyzed according to Schönberg and Linke [24].…”
Section: Chemical Analysesmentioning
confidence: 99%