Method for recycling and processing organic sludge as resources
A technology for organic sludge recycling and treatment, applied in sludge treatment, biological sludge treatment, dehydration/drying/concentrated sludge treatment, etc., to achieve the effect of eliminating sludge odor, low aeration, and killing pathogenic bacteria
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Embodiment 1
[0046] The recycling and treatment method of organic sludge in this embodiment deals with sludge in spring and autumn.
[0047] See figure 1 The organic sludge treatment system of this embodiment includes a reactor 1, a thickening device 2, a heat exchanger 3, a mechanical dehydration device 4, a sludge conveying device 5, a membrane treatment device 6, a mud pump 71, a circulating water pump 72, a first The sludge return pump 73, the second sludge return pump 74, and corresponding valves and pipelines, wherein the thickening device 2 used is a thickening tank.
[0048] The reactor 1 is closed, and the reactor 1 is divided into a first reaction zone 11 and a second reaction zone 12, separated by a partition 13 between the two reaction zones, and the height of the partition 13 is lower than the height of the four walls of the reactor. Height, and the volume of the second reaction zone 12 is 4 times of the volume of the first reaction zone 11; the periphery of the reactor 1 is ...
Embodiment 2
[0067] What this embodiment deals with is the sludge in summer, and the COD of the wastewater discharged into the sewage plant in summer is lower than that in other seasons, resulting in less sludge. The difference between the processing system used and the processing system of embodiment 1 is that the concentrator 2 used is a centrifugal dehydration device, and the method adopted is basically the same as that of embodiment 1, except that:
[0068] In step ①, the solid content of the concentrated sludge is 7%, the fresh sludge VSS / TSS (volatile suspended solids / total suspended solids) = 58% to 62%, and the VSS concentration is 35g / L to 37g / L.
[0069] In step ③, the entire organic sludge treatment system is in the normal operation stage, and the first discharge of sludge in the second reaction zone 12 discharges 5 / 48 of the total volume of the second reaction zone. The sludge, that is, the total amount of sludge in the reactor 1 After the sludge is discharged, turn on the deli...
Embodiment 3
[0073] What this embodiment handles is the sludge in winter, and the difference between the processing system used and the processing system of embodiment 1 is that the thickening device 2 used is a centrifugal dehydration device, and the method adopted is basically the same as that of embodiment 1. The difference is:
[0074] In step ①, the solid content of the concentrated sludge is 6% to 7%, the fresh sludge VSS / TSS (volatile suspended solids / total suspended solids) = 65% to 75%, and the VSS concentration is 37g / L to 40g / L.
[0075] In step ②, the two reaction zones are filled and aerated, and continuously mixed evenly. Under the action of microorganisms and stirring, the temperature in the reactor 1 continues to rise, and the temperature in the reactor 1 rises to 45°C on the fifth day , no longer rise on the sixth day, open the vent pipe 11-2 of the first reaction zone and the valve at the vent pipe 12-2 of the second reaction zone, under the effect of gravity, both reac...
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