CN204824489U - Ozone microbubble reaction sewage treatment device - Google Patents
Ozone microbubble reaction sewage treatment device Download PDFInfo
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- CN204824489U CN204824489U CN201520556217.0U CN201520556217U CN204824489U CN 204824489 U CN204824489 U CN 204824489U CN 201520556217 U CN201520556217 U CN 201520556217U CN 204824489 U CN204824489 U CN 204824489U
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- gas
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 76
- 239000010865 sewage Substances 0.000 title claims abstract description 33
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 239000000203 mixture Substances 0.000 claims description 65
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 239000007789 gas Substances 0.000 claims description 14
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 9
- 230000000994 depressogenic effect Effects 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 3
- 238000002386 leaching Methods 0.000 claims description 3
- 230000035939 shock Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 15
- 239000002699 waste material Substances 0.000 abstract description 5
- 230000008569 process Effects 0.000 description 8
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 5
- 239000000126 substance Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000149 chemical water pollutant Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- -1 hydroxyl radical free radical Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000000452 restraining effect Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The utility model discloses an ozone microbubble reaction sewage treatment device, mix broken bubble device and reaction tank including inlet tube, intake pipe, aqueous vapor mixing arrangement, aqueous vapor, inlet tube and intake pipe pass through aqueous vapor mixing arrangement and connect, aqueous vapor mixing arrangement mixes to break through high -pressure gas - liquid mixing pump and aqueous vapor and steeps the device and be connected, the aqueous vapor mix broken bubble device and reaction tank connection, three continuous reacting chamber is separated into through two training walls to the inner chamber of reaction tank initial response room, second reacting chamber and third response room, the indoor ultrasonic oscillator that is equipped with of initial response, be equipped with ultraviolet lamp in the second reacting chamber, at the sewage treatment in -process, can make ozone and sewage intensive mixing, improved sewage treatment's efficiency, reduce the loss and the waste of the ozone body, popularization with low costs easy.
Description
Technical field
The utility model relates to technical field of sewage, specifically relates to a kind of ozone microbubble reaction sewage disposal device.
Background technology
Along with the acceleration with urbanization process that improves constantly of living standards of the people, the output of municipal wastes is also improving year by year, current municipal wastes just with annual 9% ~ 10% speed increment.The supporting processing demands of the percolate brought thus is also in continuous amplification.
Percolate is different with general sewage, has following several feature.
(1) COD concentration is high especially.Concentration is not from mg/L up to ten thousand to tens0000 mg/L etc.Containing the carcinogenic hazardous and noxious substances of stench, difficult degradation chemical combination organic substances such as more carboxyl benzene, heterocyclic and santowax macromolecular cpds in brown sewage.Containing certain heavy metal ion.
(2) ammonia nitrogen concentration in percolate is high.Concentration from tens of to several thousand mg/L not etc.Along with the prolongation of landfill time, the ammonia nitrogen in percolate has the trend constantly raised.Ammonia nitrogen in high density has restraining effect to microorganism in percolate biochemical treatment process, causes the biochemical treatment system of percolate can not steady running.And ammonia nitrogen in high density process itself is also a great problem.
(3) the microbial nutrition material serious disproportion in percolate, biodegradability is poor with biological nitration.Except ammonia nitrogen is high especially, B/C, C/N are lower, and especially " middle old-age group " percolate utilizes routine biochemistry difficult treatment.
(4) water quantity and quality change greatly, needs the treatment process adopting capacity of resisting impact load strong.
Because the difficulty of landfill leachate treatment is large, technical development is slower.So far, although occurred as techniques such as leachate recirculation, land treatment systems, materializing strategy, reverse osmosis, evaporation process, Advanced oxidation technologies and bioreactor landfills, mature equipment and technique little.Do not have consecutive production technique, ozone dosage is large, utilization ratio is low, and technique is loaded down with trivial details, and cost too high failing is popularized; And easily overflow ozone and affect Working environment, the too many benefit of area occupied is low, and the time is oversize reacts again instability.
Utility model content
The purpose of this utility model is to provide a kind of ozone microbubble reaction sewage disposal device, improves the efficiency of sewage disposal, reduces loss and the waste of ozone gas, and cost is low easily universal.
The utility model solves the technical scheme that its technical problem adopts: a kind of ozone microbubble reaction sewage disposal device, comprise water inlet pipe, inlet pipe, gas-vapor mix device, gas-vapor mix breaks bulb apparatus and reaction tank, described water inlet pipe is connected by gas-vapor mix device with inlet pipe, gas-vapor mix device breaks bulb apparatus by high-pressure gas-liquid mixing pump and gas-vapor mix and is connected, described gas-vapor mix is broken bulb apparatus and is connected with reaction tank, the inner chamber of described reaction tank is separated into three connected reaction chambers by two training walls, comprise the first reaction chamber, second reaction chamber and the 3rd reaction chamber, ultrasonic oscillator is provided with in the first described reaction chamber, UV-lamp is provided with in second reaction chamber.
As preferably, the first described reaction chamber and the connected entrance of the second reaction chamber are located at the top of reaction tank, and the connected entrance of the second reaction chamber and the 3rd reaction chamber is located at the bottom of reaction tank.
Further, described ultrasonic oscillator to be located at above the first reaction chamber and graceful on the water surface, and described UV-lamp vertically arrives bottom from top to bottom and is located in the second reaction chamber.
Further, described ultrasonic oscillator is frequency is 25khz power 60W ultrasonic oscillator; Described UV-lamp is the leaching end formula fluorescent tube of 40W.
Preferably, described water inlet pipe is connected with hydrogen peroxide supply-pipe.
Preferably, described gas-vapor mix device comprises mixing device main body and gas fittings, described mixing device main body is provided with water-in, air-water mixture outlet and inlet mouth, described gas fittings is connected with inlet mouth perpendicular to mixing device main body, described water-in and air-water mixture outlet straight line communicate, one section of lug boss is provided with between water-in and air-water mixture outlet, depressed part is provided with between lug boss and water-in, the ring cavity being communicated with inlet mouth and water-in is formed between lug boss with mixing device main body inner wall, gas crosses at depressed part from inlet mouth through ring cavity and water.
Preferably, described gas-vapor mix breaks bulb apparatus, comprise gas-vapor mix pipe and the broken bulb apparatus being located at gas-vapor mix pipe inside, described gas-vapor mix pipe two ends are respectively air-water mixture import and outlet, described broken bulb apparatus comprises fixed block and broken bubble cylindrical shell, the oral area of described broken bubble cylindrical shell is provided with several outside vertically extending lug bosses, broken bubble cylindrical shell is placed in gas-vapor mix pipe by lug boss, and form gap between the oral area of broken bubble cylindrical shell and gas-vapor mix inside pipe wall, broken bubble cylindrical shell is fixed in gas-vapor mix pipe by fixed block, described fixed block is provided with through hole, end face is provided with groove, air-water mixture enters brokenly in bubble cylindrical shell, groove is entered after shock, flowed out by gap again.
The beneficial effects of the utility model are: have consecutive production technique, in sewage treatment process, ozone can be made fully to mix with sewage, improve the efficiency of sewage disposal, reduce loss and the waste of ozone gas, and cost is low easily universal.
Accompanying drawing explanation
Fig. 1 is ozone microbubble reaction sewage disposal device structure iron.
Fig. 2 is the structural representation of gas-vapor mix device.
Fig. 3 is the structural representation that gas-vapor mix breaks bulb apparatus.
Fig. 4 is the sectional view at A-A place in Fig. 3.
Embodiment
The technical problem solved to make the utility model, technical scheme and beneficial effect are clearly understood, below in conjunction with accompanying drawing and embodiment, are further described the utility model.Should be appreciated that embodiment described herein only for explaining the utility model, and be not used in restriction the utility model.
As shown in Figure 1, a kind of ozone microbubble reaction of the utility model sewage disposal device, comprise water inlet pipe 1, inlet pipe 2, gas-vapor mix device 3, gas-vapor mix breaks bulb apparatus 5 and reaction tank 6, water inlet pipe 1 is crossed gas-vapor mix device 3 with inlet pipe logical 2 and is connected, gas-vapor mix device 3 breaks bulb apparatus 5 by high-pressure gas-liquid mixing pump 4 and gas-vapor mix and is connected, gas-vapor mix is broken bulb apparatus 5 and is connected with reaction tank 6, the inner chamber of reaction tank 6 is separated into three connected reaction chambers by two training walls 64, comprise the first reaction chamber 61, second reaction chamber 62 and the 3rd reaction chamber 63, ultrasonic oscillator 611 is provided with in first reaction chamber 61, UV-lamp 621 is provided with in second reaction chamber 62, the connected entrance 65 of the first reaction chamber 61 and the second reaction chamber 62 is located at the top of reaction tank 6, the connected entrance 66 of the second reaction chamber 62 and the 3rd reaction chamber 63 is located at the bottom of reaction tank 6, ultrasonic oscillator 611 to be located at above the first reaction chamber 61 and graceful on the water surface, UV-lamp 621 vertically arrives bottom from top to bottom and is located in the second reaction chamber 62, ultrasonic oscillator 611 is frequencies is 25khz power 60W ultrasonic oscillator, UV-lamp 621 is the leaching end formula fluorescent tube of 40W.
As preferred embodiment, water inlet pipe 1 is connected with hydrogen peroxide supply-pipe 7.
As shown in Figure 2, gas-vapor mix device 3 comprises mixing device main body 31 and gas fittings 32, mixing device main body 31 is provided with water-in 33, air-water mixture outlet 34 and inlet mouth 35, gas fittings 32 is connected with inlet mouth 35 perpendicular to mixing device main body 1, water-in 33 and air-water mixture export 34 straight lines and communicate, one section of lug boss 36 is provided with between water-in 33 and air-water mixture outlet 34, depressed part 37 is provided with between lug boss 36 and water-in 33, the ring cavity 38 being communicated with inlet mouth 35 and water-in 33 is formed between lug boss 36 with mixing device main body 1 inwall, gas crosses at depressed part 37 from inlet mouth 35 through ring cavity 38 and water.
As shown in Figure 3-4, gas-vapor mix breaks bulb apparatus 5, comprise gas-vapor mix pipe 51 and the broken bulb apparatus being located at gas-vapor mix pipe inside, gas-vapor mix pipe 1 two ends are respectively air-water mixture import 52 and outlet 53, broken bulb apparatus comprises fixed block 54 and broken bubble cylindrical shell 55, the oral area of broken bubble cylindrical shell 55 is provided with several outside vertically extending lug bosses 56, broken bubble cylindrical shell 55 is placed in gas-vapor mix pipe 51 by lug boss 56, and form gap 57 between the oral area of broken bubble cylindrical shell 55 and gas-vapor mix pipe 51 inwall, broken bubble cylindrical shell 55 is fixed in gas-vapor mix pipe 51 by fixed block 54, fixed block 54 is provided with through hole 58, end face is provided with groove 59, air-water mixture enters brokenly in bubble cylindrical shell 55, groove 59 is entered after shock, flowed out by gap 57 again.
Ozone microbubble reaction sewage water treatment method, comprise the following steps: sewage and ozone cross in gas-vapor mix device 3 respectively by water inlet pipe 1 and inlet pipe 2, and mixed by gas-vapor mix device 3, ozone dissolves in sewage, mixed air-water mixture pumps to gas-vapor mix by high-pressure gas-liquid mixing pump 4 and breaks bulb apparatus 5, bubble process is carried out brokenly to air-water mixture, the gas do not mixed with sewage is formed bubble in sewage break, gas is fully mixed with sewage, treated water gas mixture enters reaction tank 6, successively through the first reaction chamber 61, second reaction chamber 62 and the 3rd reaction chamber 63, after reaction tank 6 processes, standard water discharge is discharged.
Further, by the hydrogen oxide supply-pipe 7 that sewage water inlet pipe 1 is arranged, in sewage, add hydrogen peroxide generate hydroxyl radical free radical with ozone reaction.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all any amendment, on an equal basis replacement and improvement etc. done within spirit of the present utility model and principle, all should drop within protection domain of the present utility model.
Claims (7)
1. an ozone microbubble reaction sewage disposal device, it is characterized in that: comprise water inlet pipe, inlet pipe, gas-vapor mix device, gas-vapor mix breaks bulb apparatus and reaction tank, described water inlet pipe is connected by gas-vapor mix device with inlet pipe, gas-vapor mix device breaks bulb apparatus by high-pressure gas-liquid mixing pump and gas-vapor mix and is connected, described gas-vapor mix is broken bulb apparatus and is connected with reaction tank, the inner chamber of described reaction tank is separated into three connected reaction chambers by two training walls, comprise the first reaction chamber, second reaction chamber and the 3rd reaction chamber, ultrasonic oscillator is provided with in the first described reaction chamber, UV-lamp is provided with in second reaction chamber.
2. ozone microbubble reaction sewage disposal device according to claim 1, it is characterized in that: the first described reaction chamber and the connected entrance of the second reaction chamber are located at the top of reaction tank, the connected entrance of the second reaction chamber and the 3rd reaction chamber is located at the bottom of reaction tank.
3. ozone microbubble according to claim 2 reaction sewage disposal device, is characterized in that: described ultrasonic oscillator to be located at above the first reaction chamber and graceful on the water surface, and described UV-lamp vertically arrives bottom from top to bottom and is located in the second reaction chamber.
4. ozone microbubble reaction sewage disposal device according to claim 3, is characterized in that: described ultrasonic oscillator is frequency is 25khz power 60W ultrasonic oscillator; Described UV-lamp is the leaching end formula fluorescent tube of 40W.
5. ozone microbubble reaction sewage disposal device according to claim 1, is characterized in that: described water inlet pipe is connected with hydrogen peroxide supply-pipe.
6. ozone microbubble reaction sewage disposal device according to claim 1, it is characterized in that: described gas-vapor mix device comprises mixing device main body and gas fittings, described mixing device main body is provided with water-in, air-water mixture outlet and inlet mouth, described gas fittings is connected with inlet mouth perpendicular to mixing device main body, described water-in and air-water mixture outlet straight line communicate, one section of lug boss is provided with between water-in and air-water mixture outlet, depressed part is provided with between lug boss and water-in, the ring cavity being communicated with inlet mouth and water-in is formed between lug boss with mixing device main body inner wall, gas crosses at depressed part from inlet mouth through ring cavity and water.
7. ozone microbubble reaction sewage disposal device according to claim 1, it is characterized in that: described gas-vapor mix breaks bulb apparatus, comprise gas-vapor mix pipe and the broken bulb apparatus being located at gas-vapor mix pipe inside, described gas-vapor mix pipe two ends are respectively air-water mixture import and outlet, described broken bulb apparatus comprises fixed block and broken bubble cylindrical shell, the oral area of described broken bubble cylindrical shell is provided with several outside vertically extending lug bosses, broken bubble cylindrical shell is placed in gas-vapor mix pipe by lug boss, and form gap between the oral area of broken bubble cylindrical shell and gas-vapor mix inside pipe wall, broken bubble cylindrical shell is fixed in gas-vapor mix pipe by fixed block, described fixed block is provided with through hole, end face is provided with groove, air-water mixture enters brokenly in bubble cylindrical shell, groove is entered after shock, flowed out by gap again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520556217.0U CN204824489U (en) | 2015-07-29 | 2015-07-29 | Ozone microbubble reaction sewage treatment device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520556217.0U CN204824489U (en) | 2015-07-29 | 2015-07-29 | Ozone microbubble reaction sewage treatment device |
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| Publication Number | Publication Date |
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| CN204824489U true CN204824489U (en) | 2015-12-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520556217.0U Expired - Fee Related CN204824489U (en) | 2015-07-29 | 2015-07-29 | Ozone microbubble reaction sewage treatment device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104986904A (en) * | 2015-07-29 | 2015-10-21 | 广州藤昌环保科技有限公司 | Ozone microbubble reaction sewage treatment equipment and method |
| CN105836872A (en) * | 2016-05-20 | 2016-08-10 | 泸州市聚源电力设备有限公司 | Corona plasma activation method capable of improving mass transfer efficiency of ozone micro bubbles in water body |
-
2015
- 2015-07-29 CN CN201520556217.0U patent/CN204824489U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104986904A (en) * | 2015-07-29 | 2015-10-21 | 广州藤昌环保科技有限公司 | Ozone microbubble reaction sewage treatment equipment and method |
| CN105836872A (en) * | 2016-05-20 | 2016-08-10 | 泸州市聚源电力设备有限公司 | Corona plasma activation method capable of improving mass transfer efficiency of ozone micro bubbles in water body |
| CN105836872B (en) * | 2016-05-20 | 2018-12-25 | 泸州市聚源电力设备有限公司 | The corona plasma activation method of water body ozone microbubble mass-transfer efficiency can be improved |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151202 |
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| CF01 | Termination of patent right due to non-payment of annual fee |