2017
DOI: 10.1016/j.envres.2017.02.007
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Anaerobic digestion of sewage sludge with grease trap sludge and municipal solid waste as co-substrates

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Cited by 54 publications
(23 citation statements)
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“…FW is a feedstock mostly treated in AD, and it has a lipid‐rich resource with a lipid concentration of 5.0 g/L . During lipid degradation process, long‐chain fatty acids (LCFA) are mainly composed of oleic acid (C18:1), linoleic acid (C18:2), and palmitoleic acid (C16:0) as the main intermediate by‐products of lipid degradation process . LCFA can also be further converted to hydrogen and acetate by AD acetogenic bacteria through a β‐oxidation process, and finally to methane via methanogenic archaea .…”
Section: Challenges For Treatment and Disposal Of Recalcitrant Organimentioning
confidence: 99%
See 1 more Smart Citation
“…FW is a feedstock mostly treated in AD, and it has a lipid‐rich resource with a lipid concentration of 5.0 g/L . During lipid degradation process, long‐chain fatty acids (LCFA) are mainly composed of oleic acid (C18:1), linoleic acid (C18:2), and palmitoleic acid (C16:0) as the main intermediate by‐products of lipid degradation process . LCFA can also be further converted to hydrogen and acetate by AD acetogenic bacteria through a β‐oxidation process, and finally to methane via methanogenic archaea .…”
Section: Challenges For Treatment and Disposal Of Recalcitrant Organimentioning
confidence: 99%
“…During lipid degradation process, long‐chain fatty acids (LCFA) are mainly composed of oleic acid (C18:1), linoleic acid (C18:2), and palmitoleic acid (C16:0) as the main intermediate by‐products of lipid degradation process . LCFA can also be further converted to hydrogen and acetate by AD acetogenic bacteria through a β‐oxidation process, and finally to methane via methanogenic archaea . VFA accumulation can exist from a high organic load, which can, therefore, influence pH in an AD; hence, their concentrations could be used as an indicator of reactor performance.…”
Section: Challenges For Treatment and Disposal Of Recalcitrant Organimentioning
confidence: 99%
“…Hence, recent research focus is on the co-digestion of OFMSW with other substrates in biodigesters e.g. sewage sludge (Sosnowski et al, 2003;Silvestre et al, 2015;Abudi et al (2016); Grosser et al, 2017); manure (Hartmann and Ahring, 2005;Capela et al, 2008;Macias-Corral et al, 2008;Matheri et al (2017)), fruit and vegetable waste (Pavi et al (2017) and agricultural residue (Negi et al, 2018). The co-digestion of OFMSW with a co-substrate may stabilize AD process conditions such as C/N ratio, macro and micronutrients, pH, total solids, inhibitors/toxic compounds and so increase biogas production (Matheri et al, 2017;Guven et al, 2017;Pavi et al, 2017;Matheri et al, 2017;Negi et al, 2018).…”
Section: Anaerobic Co-digestion Of Ofmsw With Other Substratesmentioning
confidence: 99%
“…Moreover, there exist few publications in which a three-substrate co-digestion is studied, especially applying AB as the third co-substrate. For instance, Grosser et al [16] obtained an improved methane yield up to 82% for co-digestion of sewage sludge, organic fraction of municipal solid waste and grease trap sludge. In turn, Ahmed et al [17] recorded a 179% increase in biogas production for a mixture containing sewage sludge, microalgae and sawdust, while Solé-Bundó et al [18] observed a significant increase in methane yield during the co-digestion process.…”
Section: Introductionmentioning
confidence: 99%