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Sludge ozone oxidation and reduction device and use method thereof

A technology for ozone oxidation and sludge, which is applied in chemical instruments and methods, oxidation treatment of sludge, water/sludge/sewage treatment, etc., can solve the problems of insufficient utilization of resources, insufficient reaction of ozone and sludge, and ozone Low utilization rate and other problems, to achieve the effect of maximizing the utilization of resources, reducing the amount of ozone dosage, and improving the utilization rate

Active Publication Date: 2014-12-24
SHANGHAI MUNICIPAL WATER RESOURCES DEV & UTILIZATION NAT ENG CENT
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The currently used ozone oxidation methods are all continuous, and there are problems such as insufficient control of the reaction process, low utilization rate of ozone, large dosage, high cost, insufficient reaction of ozone and sludge, and failure to maximize the use of resources.

Method used

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  • Sludge ozone oxidation and reduction device and use method thereof
  • Sludge ozone oxidation and reduction device and use method thereof
  • Sludge ozone oxidation and reduction device and use method thereof

Examples

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Effect test

Embodiment 1

[0048] Pass the sewage into the anaerobic tank through the water inlet pipe, make it stay in the anaerobic tank for 1 hour, then flow into the anoxic tank through the pipeline, stay in the anoxic tank for 2 hours, then flow into the aerobic tank through the pipeline, and pass through the aeration tube Aeration is performed continuously for 8 hours; after the aeration treatment, the water in the aerobic tank enters the secondary sedimentation tank through the pipeline for mud-water separation treatment, and the supernatant flows into the first storage tank through the pipeline, and the activated sludge after sedimentation One part is returned to the anaerobic tank by the return pump through the return pipe, and the other part of the remaining activated sludge enters the ozone reactor through the remaining activated sludge pipe; the ozone generated by the ozone generator is introduced into the ozone reactor through the ozone dosing pipe, specifically Introduce 0.01g / g MLSS each t...

Embodiment 2

[0050] Pass the sewage into the anaerobic tank through the water inlet pipe, make it stay in the anaerobic tank for 1 hour, then flow into the anoxic tank through the pipeline, stay in the anoxic tank for 2 hours, then flow into the aerobic tank through the pipeline, and pass through the aeration tube Aeration is carried out continuously for 6 hours; after the aeration treatment, the water in the aerobic tank enters the secondary sedimentation tank through the pipeline for mud-water separation treatment, and the supernatant flows into the first storage tank through the pipeline, and the activated sludge after sedimentation One part is returned to the anaerobic tank by the return pump through the return pipe, and the other part of the remaining activated sludge enters the ozone reactor through the remaining activated sludge pipe; the ozone generated by the ozone generator is introduced into the ozone reactor through the ozone dosing pipe, specifically Introduce 0.05g / g MLSS each...

Embodiment 3

[0052] Pass the sewage into the anaerobic tank through the water inlet pipe, make it stay in the anaerobic tank for 1 hour, then flow into the anoxic tank through the pipeline, stay in the anoxic tank for 2 hours, then flow into the aerobic tank through the pipeline, and pass through the aeration tube Aeration is performed continuously for 8 hours; after the aeration treatment, the water in the aerobic tank enters the secondary sedimentation tank through the pipeline for mud-water separation treatment, and the supernatant flows into the first storage tank through the pipeline, and the activated sludge after sedimentation One part is returned to the anaerobic tank by the return pump through the return pipe, and the other part of the remaining activated sludge enters the ozone reactor through the remaining activated sludge pipe; the ozone generated by the ozone generator is introduced into the ozone reactor through the ozone dosing pipe, specifically Introduce 0.02g / g MLSS each t...

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Abstract

The invention belongs to the technical field of environmental engineering sludge treatment, and provides a sludge ozone oxidation and reduction device and a use method thereof. The sludge ozone oxidation and reduction device comprises a water inlet pipe, an anaerobic tank, an anoxic tank, an aerobic tank and a secondary settling tank, and further comprises a first regulating and storage tank, an ozone reaction kettle, a second regulating and storage tank and a backflow pipe, wherein an automatic control switch is arranged below the first regulating and storage tank, the first regulating and storage tank is connected with the ozone reaction kettle through the automatic control switch and a pipeline, one side of the first regulating and storage tank is connected with the secondary settling tank through the pipeline, and the other side of the first storage tank is connected with a water outlet pipe; a stirrer is arranged inside the ozone reaction kettle, one side of the ozone reaction kettle is connected with the second regulating and storage tank through a residual activated sludge pipe, and the other side of the ozone reaction kettle is connected with an ozone generator through an ozone dosing pipe; the second regulating and storage tank is respectively connected with the anaerobic tank and the ozone reaction kettle through the pipeline; the backflow pipe is provided with a backflow pump, one end of the backflow pipe is connected with the anaerobic tank, and the other end of the backflow pipe is connected with the residual activated sludge pipe. The sludge ozone oxidation and reduction device and the use method thereof have the advantages of full reaction between ozone and sludge, easiness in process control, small sludge dosage, low cost, high ozone utilization rate and maximum utilization of resources.

Description

technical field [0001] The invention belongs to the technical field of environmental engineering sludge treatment, and in particular relates to a sludge ozone oxidation reduction device and a use method. Background technique [0002] At present, the activated sludge method is a treatment method commonly used in urban domestic sewage plants, and it has a history of nearly a hundred years. A large amount of sludge will be generated during the activated sludge treatment process. The sewage plant needs to concentrate, dehydrate and digest the generated sludge. The treated sludge needs to be landfilled, composted or incinerated later. , such a cumbersome sludge treatment and disposal process requires very high costs as a support, which can account for 25%-60% of the total operating costs of the entire sewage treatment plant, and the cost is very high. However, if the post-treatment cost is reduced in the existing technology, The sludge will not be effectively treated, causing se...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F11/06
Inventor 张鑫周维奇马艳周新宇崔杰
Owner SHANGHAI MUNICIPAL WATER RESOURCES DEV & UTILIZATION NAT ENG CENT
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