CN215611624U

CN215611624U - Macroporous adsorption material desorption regeneration and aftertreatment system

Info

Publication number: CN215611624U
Application number: CN202122291668.4U
Authority: CN
Inventors: 解静静; 杨淑芝; 亓会永; 刘美玉
Original assignee: Shandong Runyang Environmental Protection Equipment Co ltd
Current assignee: Shandong Runyang Environmental Protection Equipment Co ltd
Priority date: 2021-09-22
Filing date: 2021-09-22
Publication date: 2022-01-25
Anticipated expiration: 2031-09-22

Abstract

The utility model discloses a desorption regeneration and post-treatment system for a macroporous adsorption material, which belongs to the field of desorption post-treatment and comprises a macroporous adsorption material desorption device, an electrocatalytic oxidation device, an ozone oxidation tank, an air floatation tank, an AOO reaction tank, a sedimentation tank and a cloth filter tank; high-pressure steam can be introduced into the macroporous adsorption material desorption device; the AOO reaction tank sequentially comprises an anaerobic tank, an anoxic tank and an aerobic tank, sludge at the bottom of the sedimentation tank returns to the anaerobic tank through a reflux pump after mud-water separation is completed, and mixed liquid in the aerobic tank returns to the anaerobic tank and the anoxic tank through a water pump at the tail end of the aerobic tank. The device can ensure effective desorption of the macroporous adsorption material and rapid degradation and conversion of organic matters.

Description

Macroporous adsorption material desorption regeneration and aftertreatment system

Technical Field

The utility model relates to the field of desorption post-treatment, in particular to a desorption regeneration and post-treatment system for a macroporous adsorption material.

Background

The organic matter in the high-salt wastewater often contains a large amount of toxic and difficultly-degradable substances, and the wastewater cannot be treated by the traditional biochemical method or cannot reach the discharge standard after being treated due to high salt content and high organic matter, so the prior upper evaporation technology is mainly adopted.

With continuous research, the requirement on treatment of the high-salt wastewater can be reduced by removing organic matters in the high-salt wastewater in advance, and at present, most of the high-salt wastewater is concentrated and separated after removing the organic matters by an activated carbon adsorption bed in order to reduce the content of the organic matters in the high-salt wastewater, but the adsorption of the high-salt wastewater to part of large-particle organic pollutants is insufficient due to the limitation of the adsorption pore size of the activated carbon.

After a new large-aperture adsorption material is developed, the organic matter can be more effectively adsorbed, a good desorption regeneration effect is achieved, and the low energy consumption requirement is met for the desorption treatment of the organic matter.

In view of the problems in the prior art, the utility model designs and manufactures a desorption regeneration and post-treatment system of a macroporous adsorption material by combining years of design and use experience in the related field and assisting with over-strong professional knowledge, so as to overcome the defects.

SUMMERY OF THE UTILITY MODEL

In order to solve the existing problems, the utility model provides a desorption regeneration and post-treatment system for a macroporous adsorption material, which can ensure effective desorption of the macroporous adsorption material and rapid degradation and conversion of organic matters.

In order to achieve the purpose, the utility model adopts the following technical scheme: a desorption regeneration and post-treatment system for a macroporous adsorption material comprises a macroporous adsorption material desorption device, an electrocatalytic oxidation device, an ozone oxidation tank, an air floatation tank, an AOO reaction tank, a sedimentation tank and a cloth filter tank;

high-pressure steam can be introduced into the macroporous adsorption material desorption device;

the AOO reaction tank sequentially comprises an anaerobic tank, an anoxic tank and an aerobic tank, sludge at the bottom of the sedimentation tank returns to the anaerobic tank through a reflux pump after mud-water separation is completed, and mixed liquid in the aerobic tank returns to the anaerobic tank and the anoxic tank through a water pump at the tail end of the aerobic tank.

The utility model has the advantages that:

1. the utility model adopts a thermal desorption macroporous adsorption material, is easy to operate and is convenient to treat and recycle the wastewater generated by utilizing high-pressure steam.

2. The electrocatalytic oxidation device can degrade organic matter molecular chains to the anaerobic digestion degree, does not need to directly degrade the organic matters to the discharge standard, can effectively reduce the energy consumption of electrocatalytic oxidation, and can improve the hydrolysis efficiency of macromolecular organic matters and promote the generation and utilization of small molecular organic matters by adopting the arrangement of the anaerobic tank and the anoxic tank.

3. The ozone oxidation pond can oxidize and remove part of small molecular organic matters in advance, and reduce the burden of subsequent treatment.

Drawings

FIG. 1 is a schematic view of a desorption, regeneration and post-treatment system for a macroporous adsorbent material;

FIG. 2 is a schematic view of an AOO reaction tank of a macroporous adsorption material desorption regeneration and post-treatment system.

In the figure: 1-macroporous adsorption material desorption device, 2-electrocatalytic oxidation device, 3-ozone oxidation tank, 4-air floatation tank, 5-AOO reaction tank, 6-sedimentation tank, 7-filter cloth filter tank, 51-anaerobic tank, 52-anoxic tank and 53-aerobic tank.

Detailed Description

In order to facilitate understanding for those skilled in the art, the present invention will be further described with reference to the accompanying drawings.

As shown in fig. 1 and 2, a desorption, regeneration and post-treatment system for macroporous adsorption materials comprises a macroporous adsorption material desorption device 1, an electrocatalytic oxidation device 2, an ozone oxidation tank 3, an air flotation tank 4, an AOO reaction tank 5, a sedimentation tank 6 and a cloth filter 7;

wherein the macroporous adsorption material is macroporous adsorption resin, is a cross-linked polymer containing ion exchange groups, has stable physicochemical properties, is insoluble in acid, alkali and organic solvents, is not influenced by inorganic salts and strong ion low molecular compounds, can adsorb macromolecular organic matters, and can be desorbed when needed, placing the material into a macroporous adsorption material desorption device 1, introducing high-pressure steam into the macroporous adsorption material desorption device 1, regenerating by adopting a thermal method, keeping the temperature at about 60 ℃ for 2-4 hours, then the discharged waste liquid enters an electrocatalytic oxidation device 2, the electrocatalytic oxidation device 2 degrades the molecular chains of the organic matters to the anaerobic digestion degree without directly degrading the organic matters to the discharge standard, the energy consumption of electrocatalytic oxidation can be effectively reduced, and the ozone oxidation tank 3 can oxidize and remove part of small molecular organic matters in advance, so that the burden of subsequent treatment is reduced.

The flotation tank 4 can remove suspended matters with smaller size, a coagulating agent can be added into the tank, water subjected to flotation enters the AOO reaction tank 5, namely sequentially enters the anaerobic tank 51, the anoxic tank 52 and the aerobic tank 53, then enters the sedimentation tank 6 for mud-water separation, sludge at the bottom of the sedimentation tank 6 after mud-water separation returns to the anaerobic tank 51 through a reflux pump, and mixed liquid in the aerobic tank 53 returns to the anaerobic tank 51 and the anoxic tank 52 through a water pump at the tail end of the aerobic tank 53.

It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. Further, it should also be understood that various alterations, modifications and/or variations can be made to the present invention by those skilled in the art after reading the technical content of the present invention, and all such equivalents fall within the protective scope defined by the claims of the present application.

Claims

1. The utility model provides a macroporous adsorption material desorption regeneration and aftertreatment system which characterized in that: comprises a macroporous adsorption material desorption device, an electrocatalytic oxidation device, an ozone oxidation tank, an air floatation tank, an AOO reaction tank, a sedimentation tank and a cloth filter tank;