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. 2021 May 29;14:125. doi: 10.1186/s13068-021-01968-0

Table 2.

Summary of physicochemical parameters characterizing bioreactors operation in Experiments 1 and 2. M1—domination of lactate, M2—domination of butyrate, M3—domination of propionate, M4—domination of acetate

Parameter COD [g/L] Substrate utilization [%] pH Methane content in biogas [%] Methane [dm3/day] Methane [dm3/g C OD reduced] S2- [mg/L] Fe2+/3+ [mg/L] Total nitrogen [mg/L] Redox potential [mV]
Bioreactor Medium Effluent Medium Effluent Medium Effluent Medium Effluent Medium Effluent
Experiment 1
 M1 14.1 3.7±0.7 (3.5) 73.8±5.0 (75.2) 5.00 7.1±0.1 (7.1) 74.6±3.0 (77.8) 2.3±0.7 (2.6) 0.4±0.1 (0.5) <0.05* 0.08±0.02 (0.1) <10* 0.6±0.01 (0.6) 115.0 96.0 − 280
 M2 16.3 5.4±0.5 (5.1) 66.9±3.0 (68.7) 5.40 7.0±0.7 (6.9) 81.5±1.4 (83.4) 3.3±0.3 (3.5) 0.6±0.1 (0.6) <0.05* 0.14±0.05 (0.1) <10* 1.2±0.2 (1.4) 115.0 108.0 − 255
 M3 16.6 5.0±0.5 (5.3) 69.7±2.9 (68.1) 5.50 7.2±0.1 (7.1) 81.3±3.9 (82.8) 2.3±0.5 (2.4) 0.4±0.1 (0.4) <0.05* 0.14±0.01 (0.1) <10* 0.9±0.1 (0.9) 115.0 112.0 − 280
 M4 11.0 2.7±0.5 (3.1) 75.6±4.2 (71.8) 5.60 7.2±0.1 (7.2) 76.2±4.4 (84.1) 1.9±0.1 (2.1) 0.5±0.0 (0.5) <0.05* 0.19±0.06 (0.2) <10* 0.4±0.1 (0.5) 115.0 120.0 − 305
Experiment 2
 M1 12.2 2.2±0.8 (1.3) 82.2±6.7 (89.0) 7.00 7.5±0.2 (7.2) 73.9±3.7 (74.0) 2.5±0.6 (2.9) 0.5±0.1 (0.4) <0.05* 0.08±0.03 (0.1) <10* 0.8±0.06 (0.8) 115.0 110.0 − 400
 M2 16.7 6.1±2.1 (7.5) 63.7±12.6 (55.1) 7.00 7.2±0.4 (6.9) 79.1±2.3 (78.0) 2.4±0.5 (2.0) 0.4±0.1 (0.4) <0.05* 0.12±0.06 (0.1) <10* 1.5±0.6 (1.7) 115.0 110.0 − 363
 M3 14.9 4.4±1.1 (4.7) 70.3±7.5 (68.5) 7.00 7.6±0.1 (7.5) 84.2±2.4 (89.0) 2.2±0.4 (2.4) 0.4±0.1 (0.5) <0.05* 0.12±0.06 (0.2) <10* 0.6±0.1 (0.6) 115.0 90.0 − 333
 M4 9.5 1.9±0.7 (2.5) 80.5±7.4 (73.7) 7.20 7.9±0.2 (7.9) 87.8±2.9 (90.0) 1.5±0.4 (2.5) 0.4±0.1 (0.7) <0.05 0.22±0.21 (0.1) <10* 0.4±0.1 (0.5) 115.0 115.0 − 343

*The limit of quantification

In parenthesis, there are data from the time of sample collection for DNA isolation (day 751, /week 108/ for Experiment 1 and day 884 /week 127/ for Experiment 2). COD utilization and methane production are shown as arithmetic means ± SD