CN211419933U - Application system for treating sludge - Google Patents

Application system for treating sludge Download PDF

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Publication number
CN211419933U
CN211419933U CN201922266161.6U CN201922266161U CN211419933U CN 211419933 U CN211419933 U CN 211419933U CN 201922266161 U CN201922266161 U CN 201922266161U CN 211419933 U CN211419933 U CN 211419933U
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mud
pipeline
biochemical
cold plasma
row
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潘庆智
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Abstract

The utility model provides an application system for processing mud, it includes biochemical row's mud facility, biochemical row's mud facility passes through row mud pipeline and is connected with oxidation aeration tank, be equipped with cold plasma equipment, the one end of cold plasma equipment is connected with the intake stack, the other end and the fan of cold plasma equipment are connected, the fan other end passes through the supply-air duct and is connected with oxidation aeration tank, oxidation aeration tank and sedimentation tank are connected, sedimentation tank one side passes through the pipeline and is connected with biochemical system inlet channel, the bottom of sedimentation tank passes through the pipeline and is connected with the pressure filter or dries the platform, the utility model discloses utilize extra-nuclear electron to peel off the technique, under the interact of chemical reaction and physical effort, kill the bacterium, break open the cell membrane, release the cytoplasm, make inorganic matter, organic matter, water effectively separate, inorganic matter after the processing, no foul gas produces, has stopped the secondary pollution of mud, produced cell piece backward flow, saves the feeding of carbon source and indirectly reduces the sewage treatment cost.

Description

Application system for treating sludge
Technical Field
The utility model relates to an application system for treating sludge, belonging to the environmental protection industry.
Background
The sewage treatment plant can produce a certain amount of biochemical sludge in the sewage treatment process, has the characteristics of high organic matter content, volatile malodorous gas and secondary pollution, and needs to treat the sludge according to national regulations.
The existing sludge treatment technology at home and abroad comprises: the technologies of making fertilizer by sludge, burning, sanitary landfill, land utilization, building material utilization and the like all have certain defects, and the technology has the problems of low cost, no public hazard and no pollution.
For example: part of sludge in countries such as Europe and America is used as farmland fertilizer, if the sludge is used as fertilizer throughout the year, heavy metal ions can be accumulated in soil, so that the heavy metal in the soil exceeds the standard, crops absorb the heavy metal ions, and the food safety is endangered.
Also, the sludge incineration process inevitably produces a large amount of pollutants, such as fine dust particles, acid gases, heavy metals, dioxin, and the like.
For years, in island countries in Japan, the incineration process has been preferred as a process for treating sludge, and the incineration cost is more than 500 yuan per ton of sludge with water content of 80% accounting for 66.9% of the total amount of sludge. Annual sludge production in Japan is about 896 million tons (water content is 80%), and the treatment cost is 450.4 hundred million yen (about 27.52 hundred million yuan RMB). The defects of the incineration process bring huge resource waste.
Disclosure of Invention
The utility model aims to overcome the defects in the prior art, and provides an application system for treating sludge, which is dedicated to solving the difficult problem of sludge treatment by using a low-cost, pollution-free and pollution-free method.
The technical scheme of the utility model is that: the utility model provides an application system for handle mud, the characteristics are, it includes biochemical row's mud facility, biochemical row's mud facility passes through row mud pipeline and is connected with oxidation aeration tank, be equipped with cold plasma equipment, cold plasma equipment's one end is connected with the intake stack, cold plasma equipment's the other end and fan are connected, the fan other end passes through the supply-air duct and is connected with oxidation aeration tank, oxidation aeration tank and sedimentation tank are connected, sedimentation tank one side is passed through the pipeline and is connected with biochemical system inlet channel, the bottom of sedimentation tank is passed through the pipeline and is connected with the pressure filter or dry the platform.
The utility model designs a sludge treatment application system by using the extranuclear electron stripping technology (ZL 201010586363X, a method and a device for stripping the extranuclear electrons). The air is excited into a plasma state in the cold plasma equipment, oxygen molecules are ionized and cracked into oxygen atoms, the extra-nuclear electrons of the atoms are separated from the constraint of atomic nuclei under the action of continuous high-voltage electric energy to obtain free electrons (-e), the oxygen atoms and the oxygen molecules are combined to form ozone (O3), water molecules contained in the air are cracked into hydroxyl radicals (OH), independent hydrogen atoms are combined with independent oxygen atoms, and the hydroxyl radicals (OH) are generated again. Inputting the obtained mixed gas containing ozone, hydroxyl free radicals and free electrons into an aeration tank filled with pretreated biochemical sludge, carrying out aeration oxidation treatment on the biochemical sludge contained in the water body, wherein the oxidation potential of the ozone is 2.07v, the oxidation potential of the hydroxyl free radicals is as high as 2.8v, under the alkaline condition of the water body, the mixed gas can kill biochemical bacteria contained in the water body and break cell membranes to release cytoplasm, the cytoplasm belongs to a liquid state and can be oxidized and reduced into carbon dioxide and water, and under the action of the free electrons, inorganic matters and organic matters contained in the water body are effectively separated, and the settlement ratio is increased. Discharging the mud-water mixture subjected to oxidation and reduction into a settling tank for precipitation separation, wherein inorganic matters settle at the bottom of the tank, organic matters and water are discharged into the front end of a biochemical tank of a sewage treatment plant as carbon sources for biochemical treatment again, the inorganic matters are discharged into a filter press or a drying table after the precipitation separation, and the dried inorganic matters can be used for making bricks or burying and the like.
The technology can reduce the sludge (absolute dry) by more than 60-90 percent, reduce the sludge yield, and simultaneously reduce the sludge treatment cost, the inorganic substance after treatment does not generate malodorous gas, thereby avoiding the secondary pollution of the sludge, saving the throwing of carbon sources after the generated cell debris flows back, and indirectly reducing the sewage treatment cost.
The present invention will be described in detail with reference to the accompanying drawings and embodiments.
Drawings
Fig. 1 is a schematic structural diagram of an application system of the present invention.
Fig. 2 is a schematic structural diagram of a cold plasma device according to the present invention.
The drawings illustrate:
1 biochemical sludge discharge facility, 2 alkaline substances, 3 oxidation aeration tank, 4 air, 5 cold plasma equipment, 6 hydroxyl radicals, ozone and free electrons, 7 sedimentation tank, 8 inorganic substance, 9 filter press or airing platform, 10 brick making factory or landfill site, 11 organic substance and water, 12 biochemical system water inlet pipeline, 2-2 air inlet pipeline, 2-3 conductor electrode, 2-4 ionization cavity, 2-5 medium electrode, 2-6 induced air pipeline (air containing hydroxyl radicals, ozone and free electrons), 2-7 fan, 2-8 air supply pipeline and 2-9 aeration pipeline.
Detailed Description
Referring to fig. 1, an application system for treating sludge comprises a biochemical sludge discharge facility 1, wherein the biochemical sludge discharge facility 1 is connected with an oxidation aeration tank 3 through a sludge discharge pipeline, the oxidation aeration tank 3 is connected with a sedimentation tank 7, one side of the sedimentation tank 7 is connected with a biochemical system water inlet pipeline 12 through a pipeline, and the bottom of the sedimentation tank 7 is connected with a filter press or an airing table 9 through a pipeline.
A pipeline is arranged in the oxidation aeration tank 3 and connected with a cold plasma device 5, as shown in figure 2, an outer nuclear electron stripping bin consisting of a conductor electrode 2-3, a medium electrode 2-5 and an ionization cavity 2-4 is arranged in the cold plasma device 5, one end of an air inlet of the outer nuclear electron stripping bin is communicated with the outside air 4 through an air inlet pipeline 2-2, an air outlet of the other end of the outer nuclear electron stripping bin is connected with a fan 2-7 through an air guide pipeline 2-6, and the other end of the fan 2-7 is connected with an aeration pipeline 2-9 in the oxidation aeration tank 3 through an air supply pipeline 2-8.
The working principle is briefly described.
The biochemical sludge discharge facility 1 discharges sludge with the water content of more than 95 percent into an oxidation aeration tank 3 through a sludge discharge pipeline, alkaline substances 2 (such as caustic soda, calcium oxide and calcium hydroxide) are added into the oxidation aeration tank 3, the pH value of the sludge is adjusted to be more than 9, air 4 enters an ionization cavity 2-4 between a conductor electrode 2-3 and a medium electrode 2-5 in cold plasma equipment 5 through an air inlet pipeline 2-2 under the induced air action of a fan 2-7 to ionize the air 4 to obtain hydroxyl radicals, ozone and free electrons 6, the air containing the hydroxyl radicals, the ozone and the free electrons 6 enters the fan 2-7 through the air inlet pipeline 2-6, and then enters an aeration pipeline 2-9 in the oxidation aeration tank 3 through an air supply pipeline 2-8 to ensure that the air containing the hydroxyl radicals, the ozone and the free electrons 6 enters the fan 2-7 through the air inlet pipeline 2-9, The air of free electrons 6 is released in the sludge to sterilize the bacteria in the sludge, the cell membranes of the bacteria are broken, cytoplasm is released, the inorganic substances 8, the organic substances and the water 11 are subjected to open-loop chain breaking decomposition through continuous oxidation, then the mixed solution is discharged into a sedimentation tank 7 for sedimentation and separation, the organic substances and the water 11 with small specific gravity flow back into a water inlet pipeline 12 of a biochemical system, the inorganic substances 8 with the specific gravity larger than 1.0 are settled at the bottom of the sedimentation tank 7, then the inorganic substances 8 are discharged into a filter press or an air drying platform 9 through a pipeline for filter pressing dehydration or natural air drying, and finally the pollution-free inorganic substances can be used for brick making or landfill and the like.
The utility model discloses utilize the outer electron of nuclear to peel off the technique, adopt ozone, hydroxyl free radical, free electron, under the interact of chemical reaction and physical effort, exterminate the bacterium, break open the cell membrane, release the cytoplasm, make inorganic matter, organic matter, water effective separation, then flow back organic matter to biochemical system front end as the carbon source, the input cost of carbon source has been saved, inorganic matter that produces after the processing is after filter-pressing or sunning, become pollution-free sand, can be used for the brickmaking or landfill. The utility model provides a defect that current sludge treatment technique exists, stopped the secondary pollution that sludge incineration or landfill lead to.

Claims (1)

1. The utility model provides an application system for handle mud, characterized by, it includes biochemical row's mud facility (1), biochemical row's mud facility (1) is connected with oxidation aeration tank (3) through row's mud pipeline, be equipped with cold plasma equipment (5), the one end of cold plasma equipment (5) is connected with air inlet pipe (2-2), the other end and the fan (2-7) of cold plasma equipment (5) are connected, the fan (2-7) other end is connected with oxidation aeration tank (3) through supply-air duct (2-8), oxidation aeration tank (3) are connected with sedimentation tank (7), sedimentation tank (7) one side is connected with biochemical system inlet channel (12) through the pipeline, the bottom of sedimentation tank (7) is passed through the pipeline and is connected with the pressure filter or dries platform (9).
CN201922266161.6U 2019-12-17 2019-12-17 Application system for treating sludge Active CN211419933U (en)

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CN201922266161.6U CN211419933U (en) 2019-12-17 2019-12-17 Application system for treating sludge

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114057363A (en) * 2022-01-17 2022-02-18 南京智感环境科技有限公司 Physical and biological combined enhanced automatic control module and tail water treatment method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114057363A (en) * 2022-01-17 2022-02-18 南京智感环境科技有限公司 Physical and biological combined enhanced automatic control module and tail water treatment method

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