Method for improving methane purity in sludge anaerobic digestion generated biogas
An anaerobic digestion and biogas technology, which is applied in the field of environmental engineering, can solve the problems of low added value of biogas and low efficiency of biogas, and achieve the effects of enhancing destruction, improving acid hydrolysis, and improving methane purity
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Embodiment 1
[0022] This embodiment relates to a method for improving the purity of methane in biogas produced by anaerobic digestion of sludge. The process flow is as follows figure 1 As shown, it specifically includes the following steps:
[0023] A sewage plant in Shanghai, the object is the remaining sludge in the secondary sedimentation tank, and the solid content of the sludge after concentration is 20g / L. During the hydrolysis and acidification stage, the dosage of calcium nitrite is 500mg N / L (that is, 2.36g Ca(NO 2 ) 2 / L), while using 6M HCl solution to gradually adjust the pH of the fermentation mixture to 6.0, and control the temperature at 37±2°C. The sludge retention time is controlled to 3d, and the ORP in the hydrolysis fermentation tank is maintained at -100mV. After hydrolysis and acid production, it is transported to a regulating tank, and the pH is adjusted back to 6.5 with 5M NaOH solution, and then transported to an anaerobic reactor. The abundance of hydrogen-trophic me...
Embodiment 2
[0025] This embodiment relates to a method for improving the purity of methane in biogas produced by anaerobic digestion of sludge, which specifically includes the following steps:
[0026] A domestic sewage plant in Shanghai, the object is the remaining sludge in the secondary sedimentation tank, and the solid content of the sludge after concentration is 40g / L. The dosage of calcium nitrite is 2000mg N / L (that is, 9.43g Ca(NO 2 ) 2 / L), use 6M HCl solution to gradually adjust the pH of the fermentation mixture to 4.0, control the temperature at 37±2°C, and mix well. The sludge residence time in the hydrolysis fermenter is 1d, and the ORP in the hydrolysis fermentor is maintained at -200mV. After hydrolysis and acid production, it is transported to a regulating tank, adjusted to pH 6.3 with 5M NaOH solution, and then transported to an anaerobic reactor. The abundance of the hydrogen-trophic methanogen Methanobacterium reaches 40%. The sludge retention time is 20d, the ORP in the...
Embodiment 3
[0028] This embodiment relates to a method for improving the purity of methane in biogas produced by anaerobic digestion of sludge, which specifically includes the following steps:
[0029] A sewage plant in Shanghai, the object is the thickening tank sludge, the sludge solid rate is 30g / L, the dosage of calcium nitrite is 1300mg N / L (that is, 6.13g Ca(NO 2 ) 2 / L), use 6M HCl solution to gradually adjust the pH of the fermentation mixture to 5.0, control the temperature at 37±2°C, stir continuously and mix well. The retention time of the sludge in the hydrolysis fermenter is 2d, and the ORP in the hydrolysis fermenter is maintained at -300mV. After hydrolysis to produce acid, it is transported to a regulating tank, adjusted back to pH 6.0 with 5M NaOH solution, and then transported to an anaerobic reactor. The abundance of the hydrotrophic methanogen Methanobacterium reaches 50%. The sludge retention time is 30d, the ORP in the tank is -400mV, and the temperature is 37±2℃. The ...
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