一种污泥厌氧消化液处理系统

By setting up a digester equalization tank and a main reaction tank at the front end of the wastewater treatment plant, precipitates are generated through chemical reactions, reducing ammonia nitrogen concentration. The problem of excessive ammonia nitrogen load in sludge anaerobic digestion liquid treatment is solved through an automated discharge system, achieving efficient and environmentally friendly sludge anaerobic digestion liquid treatment.

CN224513322UActive Publication Date: 2026-07-17MCC TIANGONG GROUP

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
MCC TIANGONG GROUP
Filing Date
2025-05-27
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

In existing technologies, anaerobic digestion liquid from sludge is directly transported to the front end of the wastewater treatment plant, which increases the ammonia nitrogen treatment load of the wastewater treatment plant and easily leads to substandard effluent discharge and secondary pollution.

Method used

A digester conditioning tank, a main reaction tank, and a magnesium sulfate dissolution tank are set up at the front end of the primary treatment of the wastewater treatment plant. The precipitate is generated through chemical reaction, which reduces the ammonia nitrogen concentration in the supernatant and is transported to the front end of the primary treatment through a return pipe. At the same time, a sludge discharge funnel and a stirring device are set up to realize the automated collection and discharge of the precipitate.

Benefits of technology

It significantly reduces the ammonia nitrogen treatment load of wastewater treatment plants, avoids substandard effluent discharge, and achieves efficient and environmentally friendly treatment of sludge anaerobic digestion liquid.

✦ Generated by Eureka AI based on patent content.

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Abstract

本实用新型提供一种污泥厌氧消化液处理系统,该处理系统包括消化液调节池、主反应池和硫酸镁溶解池,消化液调节池通过消化液输送管与主反应池连通;硫酸镁溶解池通过药液输送管与主反应池连通;主反应池通过回流管与污水厂一级处理前端连通;主反应池底部设有排泥孔,排泥孔通过排泥管与污水厂污泥浓缩池连通。本实用新型通过将污泥厌氧消化液处理系统设置在厌氧消化液输送至污水厂一级处理前端之前,通过将药液投放到污泥厌氧消化液中,与污泥厌氧消化液中的高浓度氨氮污染物发生化学反应,最终生成沉淀析出,从而降低了上清液中的氨氮浓度,大幅减轻了污水厂的氨氮处理负荷。
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Claims

1. A system for treatment of sludge anaerobic digestion liquor, characterised in that: It comprises a digestive fluid regulating tank, a main reaction tank and a magnesium sulfate dissolving tank. The digestive fluid regulating tank is communicated with the main reaction tank through a digestive fluid conveying pipe. The magnesium sulfate dissolving tank is communicated with the main reaction tank through a medicine liquid conveying pipe. The main reaction tank is communicated with a front end of a primary treatment of a sewage plant through a backflow pipe. The main reaction tank is provided with a sludge discharge hole at the bottom, which is communicated with a sludge concentration tank of the sewage plant through a sludge discharge pipe.

2. The system for treatment of sludge anaerobic digestion liquor according to claim 1, characterized in that: The main reaction tank is provided with a sludge discharge funnel at the bottom, and the sludge discharge hole is arranged at the lowest position of the sludge discharge funnel, and the distance between the sludge discharge hole and the ground is not less than 1.2 m.

3. The system for treatment of anaerobic digester liquor according to claim 2, wherein: The main reaction tank is provided with a stirring device, which comprises a stirring paddle, and the stirring paddle is inserted into the main reaction tank and is higher than the upper edge of the sludge discharge funnel by at least 0.5 m.

4. The system for treatment of anaerobic digester liquor according to claim 3, wherein: The outlet of the medicine liquid conveying pipe is higher than the highest design liquid level of the main reaction tank by at least 0.2 m.

5. The system for treatment of anaerobic digester liquor of claim 4, wherein: The inlet end of the digestive fluid conveying pipe is provided with a grid, and the grid is higher than the bottom of the digestive fluid regulating tank by not less than 0.3 m, and the outlet end of the digestive fluid conveying pipe is higher than the highest design liquid level of the main reaction tank by at least 0.3 m.

6. The system for treatment of sludge anaerobic digestion liquor according to claim 4 or 5, characterized in that: The inlet end of the backflow pipe is provided with a grid, and the grid is higher than the stirring paddle by 0.5-0.8 m.

7. The system for treatment of anaerobic digester liquid of claim 3, wherein: The sludge discharge funnel is provided with a sludge amount monitoring device.

8. The system for treatment of anaerobic digester liquor of claim 7, wherein: The digestive fluid regulating tank and the main reaction tank are respectively provided with liquid detectors for detecting the water level and water quality in the tanks.

9. The system for treatment of anaerobic digester liquor of claim 8, wherein: It further comprises a control system, the digestive fluid conveying pipe is provided with a conveying pump, the medicine liquid conveying pipe is provided with a medicine adding pump, the backflow pipe is provided with a backflow pump, the sludge discharge pipe is provided with a sludge discharge pump, and the control system is electrically connected with the stirring device, the sludge amount monitoring device, the liquid detectors, the conveying pump, the medicine adding pump, the backflow pump and the sludge discharge pump.