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2016
DOI: 10.1016/j.jclepro.2016.04.008
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Alternative co-digestion scenarios for efficient fixed-dome reactor biomethanation processes

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Cited by 18 publications
(5 citation statements)
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References 44 publications
(45 reference statements)
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“…In the present study, the pH value for both the influent and effluent was 6.1 ± 0.8 and 7.6 ± 0.3 at psychrophilic temperature. The pH range for a healthy and continuous AD process is 6.8-8.2 [11]. The FOS/TAC ratio ranged between 0.72 ± 0.2-0.17 ± 0.1 mg of acetic acid/mg of CaCO 3 for the affluent and effluent, respectively.…”
Section: Chemical Oxygen Demand Concentration For Influent (Blue Rhombuses) and Effluent (Orange Cruxes) During Olr Changesmentioning
confidence: 99%
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“…In the present study, the pH value for both the influent and effluent was 6.1 ± 0.8 and 7.6 ± 0.3 at psychrophilic temperature. The pH range for a healthy and continuous AD process is 6.8-8.2 [11]. The FOS/TAC ratio ranged between 0.72 ± 0.2-0.17 ± 0.1 mg of acetic acid/mg of CaCO 3 for the affluent and effluent, respectively.…”
Section: Chemical Oxygen Demand Concentration For Influent (Blue Rhombuses) and Effluent (Orange Cruxes) During Olr Changesmentioning
confidence: 99%
“…(16-20 • C) reached a specific biogas yield of 0.10 m 3 biogas /kg VS [10]. Therefore, biodigesters operated under psychrophilic conditions may present limitations due to the facts that: (i) microbial activity is slowed because the optimum growth temperature of bacteria and archaea is 37 • C; (ii) the removal of organic matter decreases, as does the concentration of methane in the biogas, and a fraction of this biogas is solubilized in the digestate; and (iii) in view of the above, the digestate contains organic matter that is converted to ammonia (NH 3 ) and methane (CH 4 ) during storage and soil usage [11]. Thus, this can be translated into a loss of energy efficiency and a larger environmental impact due to the aforementioned gaseous emissions [12].…”
Section: Introductionmentioning
confidence: 99%
“…These obstacles can be overcome by adding co-substrate to the reactor. This method is considered to be able to increase biogas production to more than 20% CH4 than predicted [6,12]. Various studies have been carried out related to the use of co-substrates in the production of biogas with biomass substrates.…”
Section: Anaerobic Co-digestionmentioning
confidence: 99%
“…As steady-state was defined a quasi-steady-state (Venkiteshwaran et al, 2016), for at least a period of ten successive days with less than 10 % variation in the methane production, VFA accumulation and pH fluctuation (Fotidis et al, 2016).…”
Section: Steady-statementioning
confidence: 99%
“…1) of 263 mL CH 4 g -1 VS, at steady-state. defined as a period of ten successive days with less than 10 % variation in the methane production, VFA accumulation and pH fluctuation (Fotidis et al, 2016). When ammonia levels increased in the feedstock to 3 g NH 4 + -N L -1 (P-2) and 4 g NH 4 + -N L -1 (P-3) methane production, at inhibitedsteady-state, was decreased in both reactors between 30 and 43 % compared to P-1.…”
Section: Reactors Performancementioning
confidence: 99%