1. Hydrogen and Methane Production from Food Residue Biomass Product (FORBI)
- Author
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C. Lytras, D. Mathioudakis, A. Goumenos, Konstantina Papadopoulou, Ioannis Michalopoulos, G. M. Lytras, I. Zacharopoulos, and Gerasimos Lyberatos
- Subjects
0106 biological sciences ,Acidogenesis ,Environmental Engineering ,020209 energy ,02 engineering and technology ,Raw material ,7. Clean energy ,01 natural sciences ,Methane ,Volatile Fatty Acids ,chemistry.chemical_compound ,Biogas ,010608 biotechnology ,Dark Hydrogen Fermentation ,0202 electrical engineering, electronic engineering, information engineering ,Bioreactor ,Waste Management and Disposal ,Hydrogen production ,Renewable Energy, Sustainability and the Environment ,Anaerobic Digestion ,Pulp and paper industry ,6. Clean water ,Food waste ,chemistry ,13. Climate action ,Food Residue Biomass ,Environmental science ,PABR ,Hydrogen ,Mesophile - Abstract
This study concerns the production of hydrogen and methane from a Food Residue Biomass (FORBI) product (Papanikola et al. in 5th international conference on sustainable waste management systems, Athens, 2017), generated from pre-sorted HFW in a CSTR and in a PABR respectively. FORBI is generated by drying and shredding the fermentable fraction of household food waste collected door-to-door in the Municipality of Halandri, Greece. Hydrogen production from FORBI through anaerobic fermentation under acidogenic mesophilic conditions was carried out using a 4 L CSTR, operated at 12 h HRT under an organic loading of 15 g TS L−1. The H2-CSTR was operated for 40 days. During the operation of H2-CSTR the production of biogas reached up to 0.1026 Lbiogas gFORBI−1 and the percentage of hydrogen in the gas up to 48.2%. The conversion of FORBI into methane was carried out through the operation of a 77 L PABR operated under mesophilic methanogenic conditions at various operating parameters (OLR, HRT, T). Two different approaches were adopted for the pre-treatment of the feedstock. For the two first phases of the experimental procedure, a liquid extraction step was carried out before feeding the bioreactor with the separated liquid fraction, while in the subsequent three phases, a whole suspension of FORBI was used as feed. The mean biogas production rate was 0.158 ± 0.02 Lbiogas gFORBI−1 and the mean methane percentage in the biogas was 67.5 ± 2.1%, in the first two phases. The mean biogas production rate was 0.519 ± 0.03 Lbiogas gFORBI−1 and the mean methane percentage in the biogas was 66 ± 2.8%, when a whole suspension of FORBI was fed to the PABR.
- Published
- 2019
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