A kind of anaerobic drying treatment method of excess sludge
A treatment method and excess sludge technology, which is applied in the field of anaerobic digestion gas production, cell wall breaking of excess sludge, and drying treatment, can solve the problem of large-scale application of excess sludge, high processing cost, and ultrasonic pretreatment High technical investment costs and other issues, to achieve the effect of accelerating anaerobic digestion rate, increasing gas production, and reducing removal resistance
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Embodiment 1
[0034] The specific embodiment of the present invention will be described by taking the excess sludge of a certain sewage treatment plant as an example. Add 1.2% TS sludge (TS is the total solid content of sludge) sodium perchlorate and 2% TS tributyl phosphate to 200kg of excess sludge with a water content of 98.5% and add 1.25% TS sludge After the polymyxin, the high-speed shear knife was started to perform high-speed shearing and breaking of the sludge wall at a speed of 20000r / min for 2h. The VSS reduction rate of the sludge after breaking the wall was 27.74%, and the SCOD increased by 24.95 times of the original sludge. After the wall is broken, the sludge is passed into an anaerobic fermentation tank, and anaerobic granular sludge of 1 / 8 of the remaining sludge volume is added for anaerobic digestion, and the temperature is controlled at 35°C. After 16 days of anaerobic digestion, the cumulative methane production increased by 44.26% compared with the direct anaerobic d...
Embodiment 2
[0036] Basically the same as Example 1, the difference is that the treatment agent is sodium perchlorate and 0.25% TS tributyl phosphate of 0.18% TS sludge, and colistin is added to 0.15% TS sludge, other process conditions and steps With embodiment 1. After the wall was broken, the VSS reduction rate of the sludge was 26.64%, and the SCOD increased by 23.60 times of the original sludge. After 18 days of anaerobic digestion, the cumulative methane production increased by 41.52% compared with the direct anaerobic digestion of raw mud. The moisture content of the sludge after dehydration is 62.56%. The moisture content of the remaining sludge after drying was reduced to 11.8%.
Embodiment 3
[0038] It is basically the same as Example 1, except that the treatment agent is sodium perchlorate of 0.8% TS sludge and tributyl phosphate of 1% TS sludge, and the polymyxin and 0.5% of TS sludge are added The colistin of %TS sludge, other technological conditions and steps are with embodiment 1. The reduction rate of sludge VSS after wall breaking was 30.03%, and SCOD increased 28.26 times of the original sludge. After 15 days of anaerobic digestion, the cumulative methane production increased by 52.91% compared with direct anaerobic digestion of raw mud. The moisture content of the sludge after dehydration is 60.48%. The moisture content of the remaining sludge after drying is reduced to 9.2%.
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