CN211896223U - Oxidation and air floatation integrated machine - Google Patents
Oxidation and air floatation integrated machine Download PDFInfo
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- CN211896223U CN211896223U CN202020281614.2U CN202020281614U CN211896223U CN 211896223 U CN211896223 U CN 211896223U CN 202020281614 U CN202020281614 U CN 202020281614U CN 211896223 U CN211896223 U CN 211896223U
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- slag discharge
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- 230000003647 oxidation Effects 0.000 title claims abstract description 18
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000002893 slag Substances 0.000 claims abstract description 17
- 239000010802 sludge Substances 0.000 claims abstract description 11
- 238000007790 scraping Methods 0.000 claims abstract description 10
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 4
- 238000005188 flotation Methods 0.000 claims description 19
- 238000012856 packing Methods 0.000 claims description 7
- 238000005516 engineering process Methods 0.000 abstract description 9
- 230000008878 coupling Effects 0.000 abstract description 3
- 238000010168 coupling process Methods 0.000 abstract description 3
- 238000005859 coupling reaction Methods 0.000 abstract description 3
- 239000002245 particle Substances 0.000 description 12
- 239000010865 sewage Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 239000007788 liquid Substances 0.000 description 8
- 239000003344 environmental pollutant Substances 0.000 description 7
- 231100000719 pollutant Toxicity 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 230000002209 hydrophobic effect Effects 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 235000019198 oils Nutrition 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 239000002957 persistent organic pollutant Substances 0.000 description 3
- 150000003254 radicals Chemical class 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000003818 cinder Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000009300 dissolved air flotation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 235000015110 jellies Nutrition 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 238000006864 oxidative decomposition reaction Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000005661 hydrophobic surface Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000003307 slaughter Methods 0.000 description 1
- 239000000375 suspending agent Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
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- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The utility model provides an oxidation air supporting all-in-one, ozone generator's export is linked together through pipeline and air compressor machine, the export of air compressor machine is linked together through pipeline and dissolved gas pitcher, the export of dissolving the gas pitcher is linked together through pipeline and the dissolved gas releaser of installing in air supporting equipment, air supporting equipment upper portion is provided with the water inlet, upper portion is provided with mud scrapping device in the air supporting equipment, mud scrapping device is connected with the mud motor of scraping of installing at air supporting equipment upper surface through speed reducer and shaft coupling, air supporting equipment upper right portion is provided with slag discharge opening and delivery port, last slag discharge opening and delivery port are linked together with the sludge impoundment, the air supporting equipment lower part is provided with the slag discharge opening down, slag discharge opening is linked together with the sludge impoundment, this device combines advanced oxidation technology and air supporting principle together.
Description
Technical Field
The utility model belongs to the technical field of sewage treatment device or apparatus, concretely relates to oxidation air supporting all-in-one.
Background
The air floatation machine is a device for removing solid suspended substances, grease and various jellies in various industrial and municipal sewage. The device is widely applied to the treatment of industrial wastewater and municipal sewage in oil refining, chemical industry, brewing, vegetable oil production and refining, slaughtering, electroplating, printing and dyeing and the like. The air flotation method is a flotation method commonly used in sewage treatment, and is a flotation method by utilizing micro-bubbles formed by air compression and instant release or mechanical shearing. Common methods for forming bubbles can be divided into suction air flotation machines with water suction pipes of water pumps, diffusion plate aeration air flotation, jet air flotation and impeller air flotation machines. An operation for separating and removing hydrophobic contaminant ions contained in a multiphase system of sewage, contaminant substances and air bubbles from water in the form of foam by selectively adsorbing the hydrophobic contaminant ions onto the air bubbles from the sewage. The air floatation method is a water treatment technique in which a large amount of micro-bubbles are injected into water or generated by an electrolysis method, so that the micro-bubbles are adhered to solid or liquid pollutant particles with density close to that of water in waste water to form an air floating body with density lower than that of water, and the air floating body floats to the water surface under the action of buoyancy to form floating slag for solid-liquid or liquid-liquid separation. The air flotation method is mainly used for removing suspended matters, oils and fats with relative density from the wastewater, and can also be used for concentrating high-concentration wastewater and then pressing and drying the wastewater by a belt filter press. The pollutant particles in the wastewater can be stably adsorbed on the bubbles and float upwards along with the bubbles, which is a precondition for air floatation separation, and therefore, the removed pollutant particles have hydrophobic surfaces. In order to improve the separation effect of the air flotation method, the sludge dewatering machine usually adopts measures to change the surface characteristics of solid or liquid pollutant particles, adds a certain amount of suspending agent into water to convert hydrophilic particles into hydrophobic particles, and adds a demulsifier (coagulant) into emulsified oil wastewater to aggregate emulsified oil which is difficult to float into suspended matters to remove. The air flotation machine is divided into two types according to an air dissolving mode, namely a cavitation air flotation machine and an air dissolving air flotation machine, wherein the cavitation air flotation machine efficiently pressurizes and mixes gas or more than two different liquids which are difficult to dissolve in water by utilizing the special stirring function of vortex, and the particle size of generated micro bubbles is 20-50 micrometers. The stirring technology greatly simplifies the traditional stirring process, not only can realize the miniaturization of equipment, but also saves the investment and the running cost. The pressurizing dissolved air flotation machine is a pressurizing dissolved air flotation system adopting a gas-liquid mixing pump, omits complex arrangements of a pressurizing pump, an air compressor, a jet device, a high-pressure dissolved air tank and the like, and only needs simple debugging once.
Ozone has strong oxidizability, so that organic pollutants in water can be degraded, under the condition of existence of a free radical activator or promoter, the ozone can generate a large amount of free radicals in liquid or gas, the free radicals can oxidize organic matters in the liquid or gas into simple organic matters or completely remove carbon dioxide and water in a very short time, and the ozone oxidation technology is an advanced oxidation technology. The utility model discloses an overcome traditional air supporting equipment and just get rid of aquatic suspended solid, grease and various jellies, the not enough of function singleness combines air supporting principle and advanced oxidation technology together, when getting rid of the suspended pollutant, increases the organic matter oxidative decomposition function in to sewage, can get rid of the subsequent processing technology or alleviate the biochemical stage pressure of subsequent handling.
Disclosure of Invention
The utility model aims to solve the technical problem that overcome above-mentioned prior art not enough, provide a reasonable in design, combine advanced oxidation technology and air supporting principle together, increase the oxidation air supporting all-in-one to organic matter oxidative decomposition function in the sewage, improve water quality of water when getting rid of the suspension pollutant.
The technical scheme for solving the technical problems is as follows: ozone generator's export is linked together through pipeline and air compressor machine, the export of air compressor machine is linked together through pipeline and dissolved gas pitcher, the export of dissolving the gas pitcher is linked together through pipeline and the dissolved gas releaser of installing in air supporting equipment, air supporting equipment upper portion is provided with the water inlet, upper portion is provided with scrapes mud device in the air supporting equipment, it is connected with the mud motor of scraping of installing at air supporting equipment upper surface to scrape mud device through speed reducer and shaft coupling, air supporting equipment upper right portion is provided with row's cinder notch and delivery port, it is linked together with the sludge impoundment to go up cinder notch and delivery port, air supporting equipment lower part is provided with slag discharge.
The ozone generator of the utility model adopts a high-voltage discharge type ozone generator.
The utility model discloses a dissolve gas pitcher adopts the ladder ring to pack, and the layer height of packing is 1000 ~ 2100 mm.
The utility model discloses a dissolved air releaser adopts TS, TJ, TV type series dissolved air releaser.
Compared with the prior art, the utility model has the following advantages:
1. the ozone generator adopts a high-voltage discharge type generator, air is used as a gas source, clean and dry compressed air is used as a production raw material, the gas source is sufficient, and ozone has strong oxidizability and can degrade organic pollutants in water;
2. the pressure dissolved air tank adopts stepped ring packing, the height of a packing layer is 1000-2100 mm, the dissolved air efficiency is as high as 98%, the dissolved air efficiency is close to a saturation value (at the water temperature of 30 ℃), the dissolved air tank is about 30% higher than a non-packed dissolved air tank, the release amount is about 90-99% of the theoretical saturated dissolved air amount, and the water flow is large; compared with the foreign advanced level, the gas dissolving efficiency is improved by 5-10%; the water passing density is improved by 1-5 times; the hydraulic retention time of the dissolved air tank is only 51s (originally 3-5 min), so that the volume of the tank is greatly reduced, and the manufacturing cost is reduced.
3. The dissolved air releaser uses the TV type dissolved air releaser which is uniformly distributed and vibrated, the distribution uniformity of water released by the releaser is improved, and the probability of collision and adhesion of micro bubbles and impurities in water to be treated is increased, so that the air floatation water purification effect is further improved.
Drawings
Fig. 1 is a schematic structural diagram of an embodiment of the present invention.
In the figure: 1. an ozone generator; 2. an air compressor; 3. a dissolved air tank; 4. air floatation equipment; 5. a water inlet; 6. a mud scraping device; 7. a mud scraping motor; 8. an upper deslagging port; 9. a sludge tank; 10. a water outlet; 11. a lower slag discharge port; 12. a dissolved air releaser.
Detailed Description
The present invention will be described in further detail with reference to the following drawings and examples, but the present invention is not limited to these examples.
Example 1
In fig. 1, the utility model relates to an oxidation air supporting all-in-one, ozone generator 1's export is linked together through pipeline and air compressor machine 2, and ozone generator 1 adopts high voltage discharge formula ozone generator. Ozone generated by the ozone generator 1 is compressed by the air compressor 2 to obtain compressed gas, air is used as a gas source, clean and dry compressed air is used as a production raw material, the gas source is sufficient, and meanwhile, the ozone has strong oxidizability and can degrade organic pollutants in water. The outlet of the air compressor 2 is communicated with the dissolved air tank 3 through a pipeline, compressed air enters the dissolved air tank 3, stepped ring packing with high dissolved air efficiency is adopted, the height of a packing layer is 1000-2100 mm, the dissolved air efficiency is up to 98%, and a large amount of ozone gas is dissolved in water by the compressed air and pressure water in the dissolved air tank 3 through the processes of diffusion, dissolution, mass transfer and the like. Compressed air stays in the dissolved air tank 3 for 1-3 minutes and then enters the dissolved air releaser 12 in the air flotation equipment 4 through a pipeline, a water inlet 5 is processed at the upper part of the air flotation equipment 4, sewage is added into the air flotation equipment 4 through the water inlet 5, the dissolved air releaser 12 of the utility model adopts TS, TJ and TV type series dissolved air releaser, the TV type dissolved air releaser is preferentially adopted in the embodiment, when the gas is introduced into the dissolved air releaser 12, the pressure is suddenly reduced, the dissolved air water is released by energy dissipation, and redundant gas is released in water, so that small bubbles are naturally formed when passing through the sewage, the bubble diameter is 5-20 mu m, a large amount of ozone gas is fully contacted and reacted with organic matters in the water, and finally decomposed into carbon dioxide and water, the content of the organic matters in the water is greatly reduced, and simultaneously, the bubbles are contacted and adhered with the sewage which is added with flocculating agent to form suspended particles, carrying the suspended particles to the surface. Upper portion is installed on the internal portion of air supporting equipment 4 and is scraped mud device 6, the mud device 6 of this embodiment is the marketing product, can adopt SCP type chain plate formula to scrape mud and scrape the sediment machine, it is connected with the mud motor 7 of scraping installed at 4 upper surfaces of air supporting equipment through speed reducer and shaft coupling to scrape mud device 6, it provides power for scraping mud device to scrape mud motor 7, the processing of 4 upper right portions of air supporting equipment has last slag discharge 8 and delivery port 10, last slag discharge 8 and delivery port 10 are linked together with sludge impoundment 9, the processing of 4 lower parts of air supporting equipment has lower slag discharge 11, lower slag discharge 11 is linked together with sludge impoundment 9. The sludge scraping device 6 scrapes suspended particles on the water surface to an upper slag discharge port 8, the suspended particles are discharged to a sludge tank 9 through the upper slag discharge port 8, and large suspended particles are settled to the bottom of the air floatation device 4 and are discharged to the sludge tank 9 through a lower slag discharge port 11; the purified water of the air floatation device 4 is continuously supplemented into the dissolved air tank 3 through a return pipeline connected with a water outlet, and the purposes of purifying water quality, decomposing organic matters and reducing COD are achieved through air floatation and ozone oxidation. The utility model discloses a combine air supporting principle and advanced oxidation technology together, when getting rid of the suspension pollutant, increase the oxidation decomposition function to organic matter in the sewage, can reduce the processing technology unit or alleviate the biochemical stage pressure of follow-up procedure.
Claims (4)
1. An oxidation air supporting all-in-one machine which is characterized in that: the outlet of an ozone generator (1) is communicated with an air compressor (2) through a pipeline, the outlet of the air compressor (2) is communicated with a dissolved air tank (3) through a pipeline, the outlet of the dissolved air tank (3) is communicated with a dissolved air releaser (12) installed in an air floatation device (4) through a pipeline, the upper part of the air floatation device (4) is provided with a water inlet (5), the upper part of the air floatation device (4) is provided with a mud scraping device (6), the mud scraping device (6) is connected with a mud scraping motor (7) installed on the upper surface of the air floatation device (4) through a speed reducer and a coupler, the upper right part of the air floatation device (4) is provided with an upper slag discharge port (8) and a water outlet (10), the upper slag discharge port (8) and the water outlet (10) are communicated with a sludge tank (9), the lower slag discharge port (11) is arranged on the lower part of the.
2. The integrated oxidation and air flotation machine according to claim 1, characterized in that: the ozone generator (1) adopts a high-voltage discharge type ozone generator.
3. The integrated oxidation and air flotation machine according to claim 1, characterized in that: the gas dissolving tank (3) adopts a stepped ring packing, and the height of a packing layer is 1000-2100 mm.
4. The integrated oxidation and air flotation machine according to claim 1, characterized in that: the dissolved air releaser (12) adopts TS, TJ and TV type series dissolved air releasers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020281614.2U CN211896223U (en) | 2020-03-09 | 2020-03-09 | Oxidation and air floatation integrated machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020281614.2U CN211896223U (en) | 2020-03-09 | 2020-03-09 | Oxidation and air floatation integrated machine |
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| CN211896223U true CN211896223U (en) | 2020-11-10 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN120923013A (en) * | 2025-09-04 | 2025-11-11 | 北京石油化工学院 | Ozone micro-air floatation equipment and combined overflow pollution treatment method |
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2020
- 2020-03-09 CN CN202020281614.2U patent/CN211896223U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN120923013A (en) * | 2025-09-04 | 2025-11-11 | 北京石油化工学院 | Ozone micro-air floatation equipment and combined overflow pollution treatment method |
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