Anaerobic treatment method
In an anaerobic treatment method in which contaminated water is introduced into an acidification tank to decompose polymer components in the contaminated water into organic acids, and the effluent from the acidification tank is introduced into a methane production tank containing non-biological fluidized carriers so as to convert the acids into methane, the treatment is carried out stably and continuously by preventing the occurrence of floating of carriers in the methane production tank. The COD Cr concentration of polymer components other than organic acids in the acidification tank effluent to be introduced into the methane production tank is controlled to be not more than 300 mg/L. This control prevents the occurrence of acid production reactions in the methane production tank and the consequent proliferation of microorganisms, and thereby suppresses sticking of carriers as well as the occurrence of floating and blockage by the carriers.
1. An anaerobic treatment method, comprising:
introducing contaminated water into an acidification tank to decompose a polymer component in the contaminated water into an organic acid, and
introducing effluent from the acidification tank into a methane production tank containing non-biological fluidized carriers to convert the organic acid into methane,
wherein a retention time of the contaminated water in the acidification tank is controlled to be not less than 2.5 hours, thereby to control a COD Cr concentration of a polymer component other than the organic acid in the influent to be introduced into the methane production tank so as to be not more than 300 mg/L, and
wherein the polymer component other than the organic acid is sugars, protein, or fats and oils, having 7 or more carbon atoms.
2. The anaerobic treatment method according to claim 1 , wherein a load in the methane production tank per microorganisms attached to the carriers is 1 to 10 kg-COD Cr /kg-VSS/day.
3. The anaerobic treatment method according to claim 1 , wherein a COD Cr concentration in the contaminated water is not less than 300 mg/L and a proportion of the COD Cr of the polymer component other than the organic acid is not less than 30% relative to a total COD Cr in the contaminated water.
4. The anaerobic treatment method according claim 1 , wherein the carriers have a size of 1.0 to 5.0 mm and a settling velocity of 200 to 500 m/hr.
5. The anaerobic treatment method according claim 1 , wherein the COD Cr concentration of the polymer component other than the organic acid not more than 300 mg/L prevents acid production reactions in the methane production tank and heavy proliferation of microorganisms, to thereby suppress sticking of the carriers and occurrence of floating and blockage thereof.
6. An anaerobic treatment method, comprising:
introducing contaminated water into an acidification tank to decompose a polymer component in the contaminated water into an organic acid, and
introducing effluent from the acidification tank into a methane production tank containing non-biological fluidized carriers to convert the organic acid into methane,
wherein the contaminated water to be introduced into the acidification tank is diluted or the effluent from the acidification tank is deleted with a diluting water, thereby to control a COD Cr concentration of a polymer component other than the organic acid in the influent to be introduced into the methane production tank so as to be not more than 300 mg/L, and
wherein the polymer component other than the organic acid is sugars, protein, or fats and oils, having 7 or more carbon atoms.