2018
DOI: 10.1016/j.scitotenv.2018.03.255
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Bioelectrochemically assisted anaerobic digestion system for biogas upgrading and enhanced methane production

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Cited by 84 publications
(25 citation statements)
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“…Addition of food waste produced effluents with lower effluent nitrogen (3.6-7.9.g/L for BNR; 0.6-1.3 mg/L for A2O; 1.0-2.3 mg/L for Bardenpho), reduced operating costs of between 25% and 78% for various processes analyzed, and produced a net energy gain of 3,300-3,700 kWh/ day for a 10 MGD plant. Dou, Dykstra, and Pavlostathis (2018) and Dou, Toth, and Westendorf (2018) indicated that the cost/benefit ratios of wetfeed treatment, dry-feed treatment, composting, and incineration are 2.0, 4.0, 4.9, and 5.1, respectively. The cost/benefit ratio increases to 10.2 and 40.4 for anaerobic digestion for electricity and landfill, respectively.…”
Section: Miscellaneousmentioning
confidence: 99%
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“…Addition of food waste produced effluents with lower effluent nitrogen (3.6-7.9.g/L for BNR; 0.6-1.3 mg/L for A2O; 1.0-2.3 mg/L for Bardenpho), reduced operating costs of between 25% and 78% for various processes analyzed, and produced a net energy gain of 3,300-3,700 kWh/ day for a 10 MGD plant. Dou, Dykstra, and Pavlostathis (2018) and Dou, Toth, and Westendorf (2018) indicated that the cost/benefit ratios of wetfeed treatment, dry-feed treatment, composting, and incineration are 2.0, 4.0, 4.9, and 5.1, respectively. The cost/benefit ratio increases to 10.2 and 40.4 for anaerobic digestion for electricity and landfill, respectively.…”
Section: Miscellaneousmentioning
confidence: 99%
“…Dou, Dykstra, and Pavlostathis (2018) and Dou, Toth, and Westendorf (2018) indicated that the cost/benefit ratios of wet‐feed treatment, dry‐feed treatment, composting, and incineration are 2.0, 4.0, 4.9, and 5.1, respectively. The cost/benefit ratio increases to 10.2 and 40.4 for anaerobic digestion for electricity and landfill, respectively.…”
Section: Miscellaneousmentioning
confidence: 99%
“…Conventional AD has been used for waste treatment, and consists of the following four major processes: hydrolysis, acidogenesis, acetogenesis, and methanogenesis . Integration of AD with BES can enrich exoelectrogens (anode) and hydrogenotrophic methanogens (cathode) . The degradation rate of recalcitrant compounds in wastewater is higher in the integrated MEC‐AD system, and the effluent has been found to have low organics and ammonium contents .…”
Section: Research Advancesmentioning
confidence: 99%
“…The degradation rate of recalcitrant compounds in wastewater is higher in the integrated MEC‐AD system, and the effluent has been found to have low organics and ammonium contents . Dou et al . reported that an MEC‐AD had higher resilience to shock organic loading, and a potential of 2 V resulted in water electrolysis and led to a higher CH 4 production rate (105 mL L −1 day −1 ) and biogas CH 4 content (88.5 + 1.4%).…”
Section: Research Advancesmentioning
confidence: 99%
“…This reveals that the maximum rate of consumption of COD gradually decreased from C1 to C5. According to the Stover-Kincannon model, the relationship between S e , S i and the HRT is described by eqn (9). To further conrm the accuracy of the Stover-Kincannon model, eqn (9) was used to predict the concentration of COD (Fig.…”
Section: Modeling Of Substrate Removal and Methane Productionmentioning
confidence: 99%