CN204281397U - Energetic ion Strong oxdiative recirculation reactor - Google Patents
Energetic ion Strong oxdiative recirculation reactor Download PDFInfo
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- CN204281397U CN204281397U CN201420718302.8U CN201420718302U CN204281397U CN 204281397 U CN204281397 U CN 204281397U CN 201420718302 U CN201420718302 U CN 201420718302U CN 204281397 U CN204281397 U CN 204281397U
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- Prior art keywords
- pipeline
- reaction chamber
- ozone
- dividing plate
- room
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Abstract
The utility model relates to environmental protection machinery field, particularly relates to energetic ion Strong oxdiative recirculation reactor.Comprise reaction vessel, described reaction vessel comprises inner dividing plate, reaction vessel is divided into main reaction chamber and side reaction room by dividing plate, comprise connectivity gap below dividing plate main reaction chamber and side reaction room to be linked up, pass into water pipe above described main reaction chamber, below described main reaction chamber, be passed into an ozone pipeline; Described side reaction room comprises circulating line and links up up and down, and it is provided with pump, and this circulating line stretches out pipeline down after stretching into side reaction room, and this pipeline is also communicated with vertical pipe upward, the space above this pipeline communication main reaction chamber and side reaction room.Beneficial effect: change ozone and waste water reaction pattern, improves reaction efficiency, cost declining.
Description
Technical field
The utility model relates to environmental protection machinery field, particularly relates to energetic ion Strong oxdiative recirculation reactor.
Background technology
Energetic ion Strong oxdiative reaction based on ozone is the high-new sewage disposal technology risen in recent years, existing to be added to the water mainly with reliever mode or with aerobic biochemical air mixed greatly, has the following disadvantages:
1. because ozone dissolution rate in water is low, traditional method contact reacts path is short, reacts not thorough;
2. traditional method ozone and the disposable contact reacts of sewage, reaction efficiency is not high;
3. ozone is overflowed very soon in water, and have no second stage employ report at present, ozone utilization rate is low.
Utility model content
The object of utility model: in order to provide a kind of energetic ion Strong oxdiative recirculation reactor of better effects if, specific purposes are shown in multiple substantial technological effects of concrete implementation section.
In order to reach as above object, the utility model takes following technical scheme:
Energetic ion Strong oxdiative recirculation reactor, it is characterized in that, comprise reaction vessel, described reaction vessel comprises inner dividing plate, reaction vessel is divided into main reaction chamber and side reaction room by dividing plate, comprise connectivity gap below dividing plate main reaction chamber and side reaction room to be linked up, pass into water pipe above described main reaction chamber, below described main reaction chamber, be passed into an ozone pipeline; Described side reaction room comprises circulating line and links up up and down, and it is provided with pump, and this circulating line stretches out pipeline down after stretching into side reaction room, and this pipeline is also communicated with vertical pipe upward, the space above this pipeline communication main reaction chamber and side reaction room.
The further technical scheme of the utility model is, described ozone pipe end has ozone releasing device, and this ozone releasing device is a cavity, and this cavity connects ozone pipeline, cavity is dispersed with more than one hole upward.
The further technical scheme of the utility model is, the pipeline that described circulating line stretches out after stretching into side reaction room down connects ejector.
The further technical scheme of the utility model is, described ejector is high-pressure nozzle.
The further technical scheme of the utility model is, described ozone pipeline also separates a subtube, and this subtube is communicated with the cavity of dividing plate, that is, dividing plate is hollow and comprises multiple hole on the side in main reaction chamber.
Adopt the utility model of as above technical scheme, have following beneficial effect relative to prior art: change ozone and waste water reaction pattern, improve reaction efficiency, cost declining.
Accompanying drawing explanation
In order to further illustrate the utility model, be described further below in conjunction with accompanying drawing:
Fig. 1 is utility model structural representation; Wherein: 1. air-intaking exhaust valve; 2. negative tube; 3. ejector; 4. main reaction chamber; 5. side reaction room; 6. dividing plate; 7. sampling valve; 8. reverse checkvalve; 9. stopping valve; 10. recycle pump; 11. ozone releasing devices.
Embodiment
Be described embodiment of the present utility model below in conjunction with accompanying drawing, embodiment does not form restriction of the present utility model:
Energetic ion Strong oxdiative recirculation reactor, it is characterized in that, comprise reaction vessel, described reaction vessel comprises inner dividing plate 6, reaction vessel is divided into main reaction chamber 4 and side reaction room 5 by dividing plate 6, comprise connectivity gap below dividing plate 6 main reaction chamber 4 and side reaction room 5 to be linked up, pass into water pipe above described main reaction chamber, below described main reaction chamber, be passed into an ozone pipeline; Described side reaction room 5 comprises circulating line and links up up and down, and it is provided with pump, and this circulating line stretches out pipeline down after stretching into side reaction room, and this pipeline is also communicated with vertical pipe upward, the space above this pipeline communication main reaction chamber 4 and side reaction room 5.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: ozone (or other strong oxidizers), in main reaction chamber and the abundant contact reacts of sewage, completes Strong oxdiative primary process; Side reaction room is entered in main reaction chamber water outlet, at the exterior circulating pump system of container, recycle pump rising pipe connects side reaction indoor, and fill ejector, the ozone that container top is overflowed by the negative pressure that circulating water flow is formed is sucked ejector mixing section by negative tube again, mixing jetting enters side reaction indoor, completes second time reaction, thus improve ozone utilization rate and reaction efficiency under circulating jet systemic effect.
The comparable traditional Strong oxdiative technique of the technology reduces the strong oxidizers such as ozone and adds cost about 30%, improves reaction efficiency about 30%.
Described ozone pipe end has ozone releasing device, and this ozone releasing device is a cavity, and this cavity connects ozone pipeline, cavity is dispersed with more than one hole upward.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: cavity makes ozone be evenly distributed, and make reaction effect better, because ozone is divided into multiple broken bubble, make overall separating effect better.
The pipeline that described circulating line stretches out after stretching into side reaction room down connects ejector.Described ejector is high-pressure nozzle.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: ejector makes liquids and gases contact better effects if, and contact area is larger, makes and mixed effect is better.
Described ozone pipeline also separates a subtube, and this subtube is communicated with the cavity of dividing plate, that is, dividing plate is hollow and comprises multiple hole on the side in main reaction chamber.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: in a creative way, ozone are directed to each height, then overflow from hole, carry out water purification.
In a creative way, each effect above independently exists, and can also complete the combination of the above results with a nested structure.
It is clear that the technique effect that above structure realizes realizes, if do not consider the technical scheme of adding, this patent title can also be a kind of environmental protecting device.
Not shown part details.
It should be noted that, multiple schemes that this patent provides comprise general planning own, separate, mutually do not restrict, but it also can combine when not conflicting mutually, reaching multiple effect and jointly realizing.
Expansion as nonessential: this patent does not have special component.Interior external member carbon steel lining fluorine is anticorrosion, abrasionproof, or anti-oxidation etc. with stainless steel.
Device height should at 7m, and reaction vessel volume is about about 50% of the process water yield, and strong oxidizer kind and dosage will calculate according to sewage character to be determined.
Establish thief hole at circulating-pump outlet, at the top of reaction vessel dress air inlet-exhaust valve, establish suction opening at injector, bottom main reaction chamber, fill strong oxidizer reliever.
Water inlet connects main reaction chamber top through lift pump, reacts, shell upper water outlet after reaction from main reaction chamber bottom around to the recirculation of side reaction room, recycle pump suction inlet connects bottom, side reaction room, pump water and connect top, side reaction room, jet sprays and forms the agent of negative pressure suction secondary oxidation, completes circulation secondary reaction.
Each reaction container bottom establishes blowdown emptying pipe valve.
Strong oxidizer is prepared separately, connects main reaction chamber bottom reliever.
As used two or more oxygenant, then all can connect main reaction chamber bottom reliever.
Ejector polytetrafluoro material.
more than show and describe ultimate principle of the present utility model, principal character and advantage of the present utility model.Those skilled in the art should understand the utility model and not be restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed scope.
Claims (5)
1. energetic ion Strong oxdiative recirculation reactor, it is characterized in that, comprise reaction vessel, described reaction vessel comprises inner dividing plate (6), reaction vessel is divided into main reaction chamber (4) and side reaction room (5) by dividing plate (6), dividing plate (6) below comprises connectivity gap and main reaction chamber (4) and side reaction room (5) can be linked up, and passes into water pipe, be passed into an ozone pipeline below described main reaction chamber above described main reaction chamber; Described side reaction room (5) comprises a circulating line and links up up and down, it is provided with pump, this circulating line stretches out pipeline down after stretching into side reaction room, and this pipeline is also communicated with vertical pipe upward, the space of this pipeline communication main reaction chamber (4) and side reaction room (5) top.
2. energetic ion Strong oxdiative recirculation reactor as claimed in claim 1, it is characterized in that, described ozone pipe end has ozone releasing device, and this ozone releasing device is a cavity, this cavity connects ozone pipeline, cavity is dispersed with more than one hole upward.
3. energetic ion Strong oxdiative recirculation reactor as claimed in claim 1, is characterized in that, the pipeline that described circulating line stretches out after stretching into side reaction room down connects ejector.
4. energetic ion Strong oxdiative recirculation reactor as claimed in claim 3, it is characterized in that, described ejector is high-pressure nozzle.
5. energetic ion Strong oxdiative recirculation reactor as claimed in claim 1, it is characterized in that, described ozone pipeline also separates a subtube, and this subtube is communicated with the cavity of dividing plate, that is, dividing plate is hollow and comprises multiple hole on the side in main reaction chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420718302.8U CN204281397U (en) | 2014-11-26 | 2014-11-26 | Energetic ion Strong oxdiative recirculation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420718302.8U CN204281397U (en) | 2014-11-26 | 2014-11-26 | Energetic ion Strong oxdiative recirculation reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204281397U true CN204281397U (en) | 2015-04-22 |
Family
ID=52864580
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420718302.8U Expired - Fee Related CN204281397U (en) | 2014-11-26 | 2014-11-26 | Energetic ion Strong oxdiative recirculation reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204281397U (en) |
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2014
- 2014-11-26 CN CN201420718302.8U patent/CN204281397U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150422 Termination date: 20171126 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |