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. 2019 Dec 31;17(1):283. doi: 10.3390/ijerph17010283

Table 2.

Startup strategy of conventional and the modified UASB reactors.

Fixed Parameters Units Value
Temperature °C 36 ± 1
HRT d 1
Experimental run Day Feed COD concentration (g L−1) Corresponding OLR (g L−1d−1) Dilution factor Influent volume/flow rate
Stage I 1–15 3.5 1.75 9.2 6 L/d
Stage II 15–29 6.0 3 5.4 6 L/d
Stage III 29–47 10 5 3.2 6 L/d
Stage IV 47–63 20 10 1.6 6 L/d
Stage V 63–79 28 14 1.2 6 L/d
Stage VI 79–95 32 16 1 6 L/d