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. 2022 Dec 14;13:1079136. doi: 10.3389/fmicb.2022.1079136

Table 2.

Selected studies that investigated long-term microbial dynamics during anaerobic digestion of municipal sewage sludge from a search on the Web of Science database (Clarivate Web of Science Core Collection).

Feed types Scale Reactor size Reactor qty Temp °C Days SRT/HRT OLR Aim Findings Location Year
Digested sludge Full-scale 3,300 m3 2 33 315 19 1.75 a Investigate microbial dynamics during start-up phase Waste activated sludge was suitable inoculum, clear shifts observed, enrichment of acetoclastic methanogens Venice, Italy 2021A
PS and (T)WAS Pilot-scale 2 m3 4 35 160 51.5, 25.9 1.1, 1.5 a Effect of phenylacetic acid on performance Mixed sludge was less affected compared to PS Santiago, Chile 2015B
PS/WAS mix Lab-scale 2 l various 37 93 20 3.7–9.4 b Study effect of mixing Increased mixing inhibited syntrophic oxidation of VFAs Urbana, USA 2001C
PS Lab-scale 4 l 6 36 42 - 3.4–5 b Study effect of OLR Increased loading promoted methane production; the community was unaffected Wooster, USA 2011D
PS/WAS mix Lab-scale 0.5 l 6 55 319 5–30 1–2 b Study effect of biochar Cornstove biochar increased methane content and flow rate Lemont, USA 2017E
PS/WAS mix Lab-scale 3w L 6 35 130 15 3 b Study effect of antibiotics Reduced methane production, increased risk of AMR Changsha, China 2019F
(T)WAS Lab-scale 1.5w L 4 37 155 15 2.7 c Study effect of synthetic musk Synthetic musk inhibited hydrolysis Sydney, Australia 2020G
Food/WAS mix Lab-scale 10 l 2 36 100 20 0.8–1.7 b Understanding instability Mixing WAS with Foodwaste increased stability, related to trace elements and microbes Monterotondo, Italy 2020H
(T)WAS Lab-scale 1.3 l 4 35 300 12 1.4 a Study effect of nitrous acid pre-treatment Free nitrous acid pre-treatment improved methane yields but also increased pathogens St Lucia, Australia 2021I
(T)WAS Lab-scale 0.5 l 2 35 60 5 - Study effect of contaminants on stability Cell lysis by plastic additive, but process was stable Changsha, China 2021J

Refer to Supplementary materials for search criteria; Reactor size = total volume unless marked `w` for working volume.

a

kgVS m3 day-2.

b

gVS L-1 day-2.

c

gCOD L-1 day-2; SRT, sludge retention time; HRT, hydraulic retention time; OLR, organic loading rate; PS, primary sludge; WAS, waste activated sludge; TWAS, thickened waste activated sludge. References: A (Tonanzi et al., 2021); B (Cabrol et al., 2015); C (McMahon et al., 2001); D (Gómez et al., 2011); E (Shen et al., 2017); F (Xu et al., 2019); G (Wei et al., 2020); H (Tonanzi et al., 2020); I (Calderon et al., 2021); J (Tang et al., 2021).