Method for producing methane through pre-fermenting and strengthening surplus sludge anaerobic digestion
A technology for excess sludge and anaerobic digestion, applied in the field of environmental engineering, can solve the problems of slow acidification rate and low methane production efficiency, and achieve the effect of simple method, shortening digestion residence time, and increasing hydrolysis and acidification rate
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Embodiment 1
[0039] Concentrate the remaining sludge from the sewage plant and adjust the solid content to 20g / L, mix it with the digested sludge in the anaerobic digestion tank with a solid content of 50g / L at a volume ratio of 1:8, adjust the initial pH of the fermentation mixture to 5, The fermentation mixture was mixed with 10 mg of glycine chelated nickel, and after mixing evenly, it was fermented in a hydrolysis fermenter for 5 days. During the process, the pH was controlled at about 5, and the temperature was set at 33°C; After the pH reached 7, it was introduced into the methanation tank, and the final cumulative methane production was 264mL / g·VS.
Embodiment 2
[0041] Concentrate the remaining sludge from the sewage plant to adjust the solid content to 30g / L, mix it with the digested sludge in the anaerobic digestion tank with a solid content of 50g / L at a volume ratio of 1:8, adjust the initial pH of the fermentation mixture to 6, and adjust the initial pH of the fermentation mixture to 6. The fermentation mixture was mixed with 20mg of glycine chelated nickel, and after mixing evenly, it was fermented in a hydrolysis fermenter for 1 day. During the process, the pH was controlled at about 6, and the temperature was set at 35°C; After the pH reached 7, it was introduced into the methanation tank, and the final cumulative methane production was 245mL / g·VS.
Embodiment 3
[0043] Concentrate the remaining sludge from the sewage plant to adjust the solid content to 40g / L, mix it with the digested sludge in the anaerobic digestion tank with a solid content of 50g / L at a volume ratio of 1:8, adjust the initial pH of the fermentation mixture to 5.5, and adjust the initial pH of the fermentation mixture to 5.5. The fermentation mixture was mixed with 30mg of glycine chelated nickel, and after mixing evenly, it was fermented in a hydrolysis fermentation tank for 3 days. During the process, the pH was controlled at about 5.5, and the temperature was set at 37°C; After the pH reached 7, it was introduced into the methanation tank, and the final cumulative methane production was 293mL / g·VS.
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