Effects of a gradually increased load of fish waste silage in co-digestion with cow manure on methane production |
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Authors: | Linn Solli Ove Bergersen Roald Sørheim Tormod Briseid |
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Affiliation: | Norwegian Institute for Agricultural and Environmental Research (Bioforsk), Soil and Environment Division, N-1432 Ås, Norway |
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Abstract: | This study examined the effects of an increased load of nitrogen-rich organic material on anaerobic digestion and methane production. Co-digestion of fish waste silage (FWS) and cow manure (CM) was studied in two parallel laboratory-scale (8 L effective volume) semi-continuous stirred tank reactors (designated R1 and R2). A reactor fed with CM only (R0) was used as control. The reactors were operated in the mesophilic range (37 °C) with a hydraulic retention time of 30 days, and the entire experiment lasted for 450 days. The rate of organic loading was raised by increasing the content of FWS in the feed stock. During the experiment, the amount (volume%) of FWS was increased stepwise in the following order: 3% – 6% – 13% – 16%, and 19%. Measurements of methane production, and analysis of volatile fatty acids, ammonium and pH in the effluents were carried out. The highest methane production from co-digestion of FWS and CM was 0.400 L CH4 gVS?1, obtained during the period with loading of 16% FWS in R2. Compared to anaerobic digestion of CM only, the methane production was increased by 100% at most, when FWS was added to the feed stock. The biogas processes failed in R1 and R2 during the periods, with loadings of 16% and 19% FWS, respectively. In both reactors, the biogas processes failed due to overloading and accumulation of ammonia and volatile fatty acids. |
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Keywords: | Methane production Co-digestion Fish waste silage (FWS) Cow manure (CM) Inhibition FWS" },{" #name" :" keyword" ," $" :{" id" :" k0035" }," $$" :[{" #name" :" text" ," _" :" fish waste silage CM" },{" #name" :" keyword" ," $" :{" id" :" k0045" }," $$" :[{" #name" :" text" ," _" :" cow manure sCSTR" },{" #name" :" keyword" ," $" :{" id" :" k0055" }," $$" :[{" #name" :" text" ," _" :" semi-continuously stirred tank reactor OLR" },{" #name" :" keyword" ," $" :{" id" :" k0065" }," $$" :[{" #name" :" text" ," $$" :[{" #name" :" __text__" ," _" :" organic loading rate (g" },{" #name" :" hsp" ," $" :{" sp" :" 0.25" }},{" #name" :" __text__" ," _" :" L" },{" #name" :" sup" ," $" :{" loc" :" post" }," $$" :[{" #name" :" __text__" ," _" :" ?1" },{" #name" :" hsp" ," $" :{" sp" :" 0.25" }}]},{" #name" :" __text__" ," _" :" d" },{" #name" :" sup" ," $" :{" loc" :" post" }," _" :" ?1" },{" #name" :" __text__" ," _" :" ) HRT" },{" #name" :" keyword" ," $" :{" id" :" k0075" }," $$" :[{" #name" :" text" ," _" :" hydraulic retention time (d) VFA" },{" #name" :" keyword" ," $" :{" id" :" k0085" }," $$" :[{" #name" :" text" ," $$" :[{" #name" :" __text__" ," _" :" volatile fatty acids (g" },{" #name" :" hsp" ," $" :{" sp" :" 0.25" }},{" #name" :" __text__" ," _" :" L" },{" #name" :" sup" ," $" :{" loc" :" post" }," _" :" ?1" },{" #name" :" __text__" ," _" :" ) |
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