Method for accelerating sludge anaerobic digest speed rate of sewage plant
An anaerobic digestion and sewage treatment plant technology, applied in sludge treatment, biological sludge treatment, etc., can solve the problems of long residence time of sludge anaerobic digestion, troublesome sludge disposal work, and huge sludge digestion equipment, etc., to achieve The effect of reducing the capacity of digestion equipment, reducing the toxicity of pollutants, good economic benefits and environmental benefits
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Embodiment 1
[0025] Example 1: The test sludge is excess sludge from a municipal sewage plant, with a water content of about 98% and an average particle size of 85 μm. After the sludge is mixed, pass through a 50mm sieve to remove impurities with large particle size (such as plastic bags, branches, rotten leaves, bricks, etc.) in the sludge. through 60 Co source (source intensity is 500,000Ci), the sludge is irradiated at a lower irradiation dose (2.48kGy), the soluble chemical oxygen demand increases by 79% after irradiation, and the average particle size decreases to 59.22μm. The irradiated sludge and inoculated sludge enter the mesophilic anaerobic static digestion reactor at a ratio of 1:1, and the volume of the reactor is 500ml. The temperature and stirring intensity of the anaerobic reaction are controlled by a constant temperature water bath oscillator, the reaction temperature is 35±1°C, and the stirring speed is 80±10 rpm. The anaerobic reaction cycle is 20 days, during which in...
Embodiment 2
[0026] Embodiment 2: Change the irradiation intensity in Embodiment 1 to 6.51 kGy, and keep other operating conditions unchanged. The soluble COD increased by 277%, and the average particle size decreased to 60.64μm. After the reaction, compared with the control experiment (0kGy), the gas production increase rates on the 2nd, 5th, 10th, 14th, and 20th day were 21%, 18%, 23%, 19%, and 20%, respectively.
Embodiment 3
[0027] Embodiment 3: Change the irradiation intensity in Embodiment 1 to 11.24kGy, and keep other operating conditions unchanged. The soluble COD increased by 423%, and the average particle size decreased to 55.61 μm. After the reaction, compared with the control experiment (0kGy), the gas production rate of the 2nd, 3rd, 5th, 10th, 14th, 16th, and 20th days were respectively 33%, 40%, 38%, 41%, 35%, 34%, 36%.
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