Table 1.
Substrate | Temperature (°C) | Influent Chemical Oxygen Demand (g/L) | Chemical Oxygen Demand Removal (%) | Hydraulic Retention Time (h) | Organic Loading Rate (g COD/L·d) | Methane Yield | Reference |
---|---|---|---|---|---|---|---|
Glutamate-rich wastewater | 35 | 2.0 | 95.5–96.5 | 4.5–6 | 8.26–10.82 | 0.31 1 | [25] |
Monosodium glutamate | 35 | 7.9 | 97 | 24 | 8 | 2.3 2 | [26] |
Sugarcane bagasse hydrolysate | 20–30 | 1.82 | 86 | 18.4 | 2.4 | 0.27 1 | [27] |
Recycled paper mill wastewater | 37 | 5.7 | 80.6 | 15.14 | 5.18 | 0.89 2 | [28] |
Vinasse | Ambient | 120.2 | 91–93 | 40 | 72.1 | 0.46–0.53 2 | [18] |
Guar | 37 | 1.1 | 79–84 | 10 | 2.78 | 0.15–0.16 3 | [29] |
Synthetic fiber wastewater | 13.9–32.1 | 1.7–30.7 | 75.8 | 24 | 1.3–21.5 | 0.4–2 2 | [30] |
Pistachio wastewater | 35 | 49.8 | 89.8 | 5.4 d | 4.56 | 0.33 1 | [31] |
Perchlorate | 30 | - | 84.7 | 2.2 | 9.96 | - | [32] |
Synthetic slaughterhouse wastewater | 37 | 1.7 | 70 | 10 | 3.94–8.15 | 0.35 2 | [33] |
Chocolate wastewater | 15–30 | 6.2 | 39–94 | 6 | 2–6 | 0.3–1.9 4 | [34] |
Pig slurry | 36 | 21.5 | - | 1.5 d | 14.3–16.4 | 0.25 1 | [35] |
Leachate from waste incineration | 35 | 36.8 | 97.5–99.5 | 1.3–3 d | 1.86–7.43 | - | [36] |
1 L CH4/g COD, 2 L CH4/L·d, 3 L CH4/g COD d, 4 L biogas/L·d.