CN207413175U - Nanometer microbubble processing system - Google Patents
Nanometer microbubble processing system Download PDFInfo
- Publication number
- CN207413175U CN207413175U CN201721180714.0U CN201721180714U CN207413175U CN 207413175 U CN207413175 U CN 207413175U CN 201721180714 U CN201721180714 U CN 201721180714U CN 207413175 U CN207413175 U CN 207413175U
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- Prior art keywords
- nanometer
- microbubble
- pipeline
- nanometer microbubble
- water
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 79
- 238000003860 storage Methods 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 230000018044 dehydration Effects 0.000 claims description 8
- 238000006297 dehydration reaction Methods 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 8
- 239000008188 pellet Substances 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 2
- 239000002912 waste gas Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 22
- 238000005119 centrifugation Methods 0.000 description 4
- 239000012855 volatile organic compound Substances 0.000 description 4
- 241000209094 Oryza Species 0.000 description 3
- 235000007164 Oryza sativa Nutrition 0.000 description 3
- 235000009566 rice Nutrition 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- -1 hydroxyl radical free radical Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000004941 influx Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000002101 nanobubble Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000007592 spray painting technique Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses nanometer microbubble processing systems, belong to technical field of waste gas treatment, it includes PLC control devices, nanometer microbubble reactor and nanometer micro bubble generation device, nanometer microbubble reactor includes release, the bottom of nanometer microbubble reactor is connected with water tank by pipeline, nanometer micro bubble generation device includes multistage high-pressure centrifugal, the liquid feeding end of multistage high-pressure centrifugal is connected with water pipe, the outlet end of multistage high-pressure centrifugal is connected to nanometer microbubble storage tank and an ejector by pipeline, the dissolved air water outlet side of nanometer microbubble storage tank is connected with release by pipeline, the outlet end of ejector is connected with water pipe by pipeline, the drain side of water tank is connected with water pipe by pipeline.The nanometer microbubble processing system of the utility model can improve the yield of the degree of automation and nanometer microbubble, effectively control the yield of nanometer microbubble.
Description
Technical field
The utility model belongs to technical field of waste gas treatment more particularly to nanometer microbubble processing system.
Background technology
Contain substantial amounts of volatile organic matter in the exhaust gas of industrial production (such as spray painting processing, rubber system are standby) discharge
(Volatile Organic Compound, VOC), these VOC exhaust gas serious threats human health and the ring depended on for existence
Border.At present, nanometer microbubble is a kind of purification effective ways of exhaust gas：High temperature and high pressure is generated after nanometer microbubbles rupture, is discharged
Go out substantial amounts of hydroxyl radical free radical, with capture organic gas, mechanical shearing, pyrolysis, the physical chemistry such as free-radical oxidation occur
Reaction has the function that decomposition, purification VOC exhaust gas.
However, existing nanometer microbubble processing system comes with some shortcomings：1) in dissolved air water nanometer microbubble yield
Low, 2) yield of the dissolved air water containing nanometer microbubble is difficult to be effectively controlled；3) nanometer microbubble processing system is automatic
Change degree is low.
Therefore, it is necessary to a kind of new nanometer microbubble processing system is designed, the degree of automation can be improved and is received
The yield of rice microbubble effectively controls the yield of dissolved air water.
Utility model content
The utility model aim is to overcome the shortcomings of the prior art, and provides nanometer microbubble processing system.
To achieve the above object, the technical solution that the utility model is taken is：Nanometer microbubble processing system, including
PLC control devices (Programmable Logic Controller) and the nanometer being electrically connected with the PLC control devices
Microbubble reactor and nanometer micro bubble generation device, the nanometer microbubble reactor includes air inlet, exhaust outlet, described to receive
The intracavitary of rice microbubble reactor is equipped with release, and the bottom of the nanometer microbubble reactor is connected with water tank by pipeline,
The nanometer micro bubble generation device includes multistage high-pressure centrifugal, and the liquid feeding end of the multistage high-pressure centrifugal is connected with water
Pipe, the outlet end of the multistage high-pressure centrifugal is connected to nanometer microbubble storage tank and an ejector by pipeline, described
Nanometer microbubble storage tank dissolved air water outlet side be connected with the release by pipeline, the outlet end of the ejector and
The water pipe is connected by pipeline, and the drain side of the water tank is connected with the water pipe by pipeline；Nanometer microbubble system
Valve and pump are equipped in system.
First, water is flowed into ejector later through multistage high-pressure centrifugal centrifugation in water pipe, and ejector is by the air of sucking
Mixed at high speed is carried out with the water being passed through, cutting forms the gas-water mixture containing micro air bubble；Then using multistage pressure from
Heart pump is stirred, and is further formed the dissolved air water containing nanometer microbubble, is improved the yield of nanometer microbubble, is then passed through
Tube storage is in nanometer microbubble storage tank；When the air inlet of nanometer microbubble reactor is passed through exhaust gas, by the micro- gas of nanometer
The dissolved air water in storage tank is steeped by pipeline to release, and release uniformly sprays the dissolved air water containing nanometer microbubble
In nanometer microbubble reactor inner cavity, exhaust gas is mixed with dissolved air water, reacted, and purified exhaust gas is anti-from nanometer microbubble
The exhaust outlet of device is answered to discharge；Remaining waste water is floating in water tank by pipeline to water tank in nanometer microbubble reactor
Ball valve is automatically replenished tap water, and waste water is after preliminary sedimentation separates, by pipeline flow-direction water pipe, further recycling.PLC
Control device is electrically connected nanometer microbubble reactor and nanometer micro bubble generation device, realizes the automation control of exhaust-gas treatment；
The dissolved air water that ejector, multistage high-pressure centrifugal generate is storable in nanometer microbubble storage tank, in case institute during exhaust-gas treatment
It needs；During the generation of dissolved air water, dissolved air water can recycle：The part dissolved air water that multistage high-pressure centrifugal generates passes through
In pipeline to ejector, ejector is made to suck air again, mixed afterwards with water in water pipe, re-enter multistage pressure
In centrifugal pump, dissolved air water is regenerated.
As the improvement of above-mentioned technical proposal, the valve of the inlet end installation of the ejector is manually-operated gate, according to need
The influx of accurate control air manually is sought, further controls the yield of dissolved air water.
As being further improved for above-mentioned technical proposal, the nanometer microbubble storage tank is equipped with pressure sensor, described
Pressure sensor is electrically connected with the PLC control devices, the production of dissolved air water in pressure sensor monitoring nanometer microbubble storage tank
Amount.
As being further improved for above-mentioned technical proposal, the water pipe is equipped with the filtering that water tank with strainer isolates waste water
Device；Filter can cross water and the waste water isolated from water tank in filter pipe simultaneously.
As being further improved for above-mentioned technical proposal, the intracavitary upper end of the nanometer microbubble reactor is equipped with dehydration group
Part, the dehydration package is interior to be filled with watered pellets；Dehydration package can be adsorbed, purify remaining impurity and water in exhaust gas.
Preferably, the watered pellets include active carbon particle.
As being further improved for above-mentioned technical proposal, the lower end of the nanometer microbubble reactor is equipped with perforated plate.It is useless
After gas is by perforated plate, exhaust gas is evenly distributed, and is fully reacted with nanometer microbubble.
The beneficial effects of the utility model are：The utility model provides nanometer microbubble processing system, present treatment system
Including PLC control devices, nanometer microbubble reactor and nanometer micro bubble generation device, PLC control devices improve processing system
The degree of automation；Nanometer micro bubble generation device includes the ejector and multistage pressure centrifugation by forming circulation path
Pump, ejector and multistage high-pressure centrifugal can improve the yield and yield of the nano bubble in dissolved air water, better than ejector and
Multistage high-pressure centrifugal is directly connected by single conduit.
Description of the drawings
Fig. 1 is the structure diagram of nanometer microbubble processing system described in the utility model；
In figure, 1, nanometer microbubble reactor, 11, the air inlet of nanometer microbubble reactor, 12, the reaction of nanometer microbubble
The exhaust outlet of device, 13, release, 14, dehydration package, 15, perforated plate, 2, water tank, 3, ejector, 31, manually-operated gate, 4, multistage
High pressure centrifugal pump, 5, nanometer microbubble storage tank, 51, pressure sensor, 6, water pipe, 7, filter.
Specific embodiment
For the purpose of this utility model, technical solution and advantage is better described, below in conjunction with specific embodiment and attached
The utility model is described in further detail for figure.
Embodiment 1
A kind of embodiment of nanometer microbubble processing system described in the utility model, as shown in Figure 1, PLC control devices, with
And the nanometer microbubble reactor 1 and nanometer micro bubble generation device being electrically connected with PLC control devices, nanometer microbubble reactor
1 includes air inlet 11, exhaust outlet 12, and the intracavitary of nanometer microbubble reactor 1 is equipped with release 13, nanometer microbubble reactor 1
Bottom water tank 2 is connected with by pipeline, nanometer micro bubble generation device includes multistage high-pressure centrifugal 4, multistage pressure centrifugation
The liquid feeding end of pump 4 is connected with water pipe 6, and the outlet end of multistage high-pressure centrifugal 4 is connected with respectively by pipeline receives rice microbubble to deposit
Storage tank 5 and ejector 3, the dissolved air water outlet side of nanometer microbubble storage tank 5 are connected with release 13 by pipeline, ejector
3 outlet end is connected with water pipe 6 by pipeline, and the drain side of water tank 2 is connected with water pipe 6 by pipeline；Nanometer microbubble
Valve and pump are equipped in system.
First, water is flowed into ejector 3 later through the centrifugation of multistage high-pressure centrifugal 4 in water pipe 6, and ejector 3 is by sucking
Air and the water being passed through carry out mixed at high speed, and cutting forms the gas-water mixture containing micro air bubble；Then using multistage high
Pressure centrifugal pump 4 is stirred, and is further formed the dissolved air water containing nanometer microbubble, improves the yield of nanometer microbubble, so
Afterwards by tube storage in nanometer microbubble storage tank 5；When the air inlet 11 of nanometer microbubble reactor 1 is passed through exhaust gas,
By the dissolved air water in nanometer microbubble storage tank 5 by pipeline to release 13, release 13 will contain nanometer microbubble
Dissolved air water be uniformly sprayed in nanometer 1 inner cavity of microbubble reactor, exhaust gas is mixed with dissolved air water, reacted, purified
The exhaust outlet 12 of exhaust gas from nanometer microbubble reactor 1 is discharged；Remaining waste water is defeated by pipeline in nanometer microbubble reactor 1
It send to water tank 2, the ball-cock assembly in water tank 2 is automatically replenished tap water, and waste water passes through pipeline flow-direction water after preliminary sedimentation separates
In pipe 6, further recycle.PLC control devices electrical connection nanometer microbubble reactor 1 and nanometer micro bubble generation device,
Realize the automation control of exhaust-gas treatment；The dissolved air water that ejector 3, multistage high-pressure centrifugal 4 generate is storable in the micro- gas of nanometer
It steeps in storage tank 5, in case required during exhaust-gas treatment；During the generation of dissolved air water, dissolved air water can recycle：It is multistage high
The part dissolved air water that centrifugal pump 4 generates is pressed by pipeline to ejector 3, ejector 3 being made to suck air, Zhi Houyu again
Water mixes in water pipe 6, in re-enter multistage high-pressure centrifugal 4, regenerates dissolved air water.
Preferably, in order to which according to demand, accurate to control the air capacity entered in ejector 3, the inlet end of ejector 3 is installed
Valve be manually-operated gate 31.
Preferably, in order to monitor the amount of dissolved air water in nanometer microbubble storage tank 5, nanometer microbubble storage tank 5 is equipped with pressure
Force snesor 51, pressure sensor 51 are electrically connected with PLC control devices.
Preferably, in order to cross water and the waste water isolated from water tank 2 in filter pipe 6, close to the water pipe of 3 liquid feeding end of ejector
6 are equipped with filter 7.
Preferably, for remaining impurity and water in adsorption cleaning exhaust gas, the intracavitary upper end of nanometer microbubble reactor 1 is set
There is dehydration package 14, active carbon particle is filled in dehydration package 14.
Preferably, for abundant mixing nanometer microbubble and exhaust gas, the lower end of nanometer microbubble reactor 1 is equipped with perforated plate
15。
Finally, it should be noted that above example is illustrating the technical solution of the utility model rather than to this practicality
The limitation of novel protected scope, although being explained in detail with reference to preferred embodiment to the utility model, the common skill of this field
Art personnel, which should be appreciated that, can modify to the technical solution of the utility model or replace on an equal basis, without departing from this practicality
The spirit and scope of new technique scheme.
Claims (6)
1. nanometer microbubble processing system, which is characterized in that be electrically connected including PLC control devices and with the PLC control devices
The nanometer microbubble reactor and nanometer micro bubble generation device connect, the nanometer microbubble reactor include air inlet, exhaust
Mouthful, the intracavitary of the nanometer microbubble reactor is equipped with release, and the bottom of the nanometer microbubble reactor is connected by pipeline
Water tank is connected to, the nanometer micro bubble generation device includes multistage high-pressure centrifugal, the liquid feeding end of the multistage high-pressure centrifugal
Water pipe is connected with, the outlet end of the multistage high-pressure centrifugal is connected to nanometer microbubble storage tank and a jet stream by pipeline
Device, the dissolved air water outlet side of the nanometer microbubble storage tank are connected with the release by pipeline, the ejector
Outlet end is connected with the water pipe by pipeline, and the drain side of the water tank is connected with the water pipe by pipeline；Nanometer
Valve and pump are equipped in microbubble system.
2. as described in claim 1 nanometer of microbubble processing system, which is characterized in that the inlet end installation of the ejector
Valve is manually-operated gate.
3. as claimed in claim 1 or 2 nanometer of microbubble processing system, which is characterized in that the nanometer microbubble storage tank
Equipped with pressure sensor, the pressure sensor is electrically connected with the PLC control devices.
4. as claimed in claim 1 or 2 nanometer of microbubble processing system, which is characterized in that the water pipe was equipped with drainage
Case isolates the filter of waste water.
5. as claimed in claim 1 or 2 nanometer of microbubble processing system, which is characterized in that the nanometer microbubble reactor
Intracavitary upper end be equipped with dehydration package, watered pellets are filled in the dehydration package.
6. as claimed in claim 1 or 2 nanometer of microbubble processing system, which is characterized in that the nanometer microbubble reactor
Lower end be equipped with perforated plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721180714.0U CN207413175U (en) | 2017-09-14 | 2017-09-14 | Nanometer microbubble processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721180714.0U CN207413175U (en) | 2017-09-14 | 2017-09-14 | Nanometer microbubble processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207413175U true CN207413175U (en) | 2018-05-29 |
Family
ID=62316379
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721180714.0U Expired - Fee Related CN207413175U (en) | 2017-09-14 | 2017-09-14 | Nanometer microbubble processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207413175U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110523254A (en) * | 2019-08-12 | 2019-12-03 | 深圳市柏志兴环保科技有限公司 | Micro-nano bubble organic waste gas treatment equipment and its organic waste gas treatment method |
| CN111729445A (en) * | 2020-08-06 | 2020-10-02 | 湖南九九智能环保股份有限公司 | Micro-nano bubble water spraying dust fall system |
| CN113877401A (en) * | 2021-10-22 | 2022-01-04 | 江苏远世景环保科技有限公司 | Reinforce microbubble and to towards formula VOCs reaction unit that sprays |
| CN113877450A (en) * | 2021-11-04 | 2022-01-04 | 中国环境科学研究院 | Intelligent micro-nano bubble generation device for black and odorous water treatment |
-
2017
- 2017-09-14 CN CN201721180714.0U patent/CN207413175U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110523254A (en) * | 2019-08-12 | 2019-12-03 | 深圳市柏志兴环保科技有限公司 | Micro-nano bubble organic waste gas treatment equipment and its organic waste gas treatment method |
| CN111729445A (en) * | 2020-08-06 | 2020-10-02 | 湖南九九智能环保股份有限公司 | Micro-nano bubble water spraying dust fall system |
| CN113877401A (en) * | 2021-10-22 | 2022-01-04 | 江苏远世景环保科技有限公司 | Reinforce microbubble and to towards formula VOCs reaction unit that sprays |
| CN113877401B (en) * | 2021-10-22 | 2022-07-12 | 江苏远世景环保科技有限公司 | Reinforce microbubble and to towards formula VOCs reaction unit that sprays |
| CN113877450A (en) * | 2021-11-04 | 2022-01-04 | 中国环境科学研究院 | Intelligent micro-nano bubble generation device for black and odorous water treatment |
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Legal Events
| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 510000 room 1814-1815, 1936 Kaichuang Avenue, Huangpu District, Guangzhou City, Guangdong Province Patentee after: Guangzhou Shangjie Environmental Protection Technology Co.,Ltd. Address before: 510000 room 1814-1815, 1936 Kaichuang Avenue, Huangpu District, Guangzhou City, Guangdong Province Patentee before: GUANGZHOU SHANGJIE ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
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| CP01 | Change in the name or title of a patent holder | ||
| CP03 | Change of name, title or address |
Address after: 510000 room 1814-1815, 1936 Kaichuang Avenue, Huangpu District, Guangzhou City, Guangdong Province Patentee after: GUANGZHOU SHANGJIE ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 510000 Room 203, building 1, No. 728, Kaichuang Avenue, Huangpu District, Guangzhou City, Guangdong Province Patentee before: GUANGZHOU SHANGJIE ENVIRONMETAL PROTECTION ENGINEERING Co.,Ltd. |
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| CP03 | Change of name, title or address | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180529 |
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| CF01 | Termination of patent right due to non-payment of annual fee |