Method used for increasing sludge anaerobic fermentation production of volatile short-chain fatty acids
A technology for anaerobic fermentation of volatile fatty acids and sludge, which is applied in the fields of environmental protection and resource utilization, and achieves the effects of simple operation, reduced pollution and low cost.
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Embodiment 1
[0030] (1) Fermentation substrate: take the remaining sludge (water content 99.3%, PH=6.7) from the sewage treatment plant and put it into a laboratory container, naturally settle for 24 hours at 4°C, and drain the supernatant to obtain Fermentation base.
[0031] (2) Pretreatment: Add the fermented substrate obtained in step (1) to the reactor, then add calcium peroxide and ammonium chloride, and fill the reactor with nitrogen for 10 minutes to drive away oxygen, at a temperature of 25 ± 0.1 Mechanically stir and mix at 100rmp / min at ℃ for 72 hours, and control the calcium peroxide in the anaerobic reactor to 0.02g CaO 2 / g VSS,NH 4 + -N concentration is 68.21mg NH 4 + -N / L, PH control to 9.0, through NH 4 + The concentration of -N, PH and temperature calculate the concentration of free ammonia to be 60mg NH 3 -N / L.
[0032] (3) Anaerobic fermentation: The temperature of the reactor is controlled at 35±1° C. for anaerobic fermentation, and the content of short-chain v...
Embodiment 2
[0034] (1) Fermentation substrate: take the remaining sludge (water content 99.3%, PH=6.7) from the sewage treatment plant and put it into a laboratory container, naturally settle for 24 hours at 4°C, and drain the supernatant to obtain Fermentation base.
[0035] (2) Pretreatment: Add the fermented substrate obtained in step (1) to the reactor, then add calcium peroxide and ammonium chloride, and fill the reactor with nitrogen for 10 minutes to drive away oxygen, at a temperature of 25 ± 0.1 Mechanically stir and mix at 100rmp / min at ℃ for 72 hours, and control the calcium peroxide in the anaerobic reactor to 0.02g CaO 2 / g VSS,NH 4 + -N concentration is 136.41mg NH 4 + -N / L, PH control to 9.0, through NH 4 + The concentration of -N, PH and temperature calculate the concentration of free ammonia to be 120mg NH 3 -N / L.
[0036] (3) Anaerobic fermentation: The temperature of the reactor is controlled at 35±1° C. for anaerobic fermentation, and the content of short-chain...
Embodiment 3
[0038] (1) Fermentation substrate: take the remaining sludge (water content 99.3%, PH=6.7) from the sewage treatment plant and put it into a laboratory container, naturally settle for 24 hours at 4°C, and drain the supernatant to obtain Fermentation base.
[0039] (2) Pretreatment: Add the fermented substrate obtained in step (1) to the reactor, then add calcium peroxide and ammonium chloride, and fill the reactor with nitrogen for 10 minutes to drive away oxygen, at a temperature of 25 ± 0.1 Mechanically stir and mix at 100rmp / min at ℃ for 72 hours, and control the calcium peroxide in the anaerobic reactor to 0.02g CaO 2 / g VSS, NH 4 + -N concentration is 204.61mg NH 4 + -N / L, PH control to 9.0, through NH 4 + The concentration of -N, PH and temperature calculate the concentration of free ammonia to be 180mg NH 3 -N / L.
[0040] (3) Anaerobic fermentation: The temperature of the reactor is controlled at 35±1° C. for anaerobic fermentation, and the content of short-chai...
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