CN106976951A - The equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water - Google Patents
The equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water Download PDFInfo
- Publication number
- CN106976951A CN106976951A CN201710269192.XA CN201710269192A CN106976951A CN 106976951 A CN106976951 A CN 106976951A CN 201710269192 A CN201710269192 A CN 201710269192A CN 106976951 A CN106976951 A CN 106976951A
- Authority
- CN
- China
- Prior art keywords
- circulated sprinkling
- waste water
- ozone
- sprinkling tower
- ultraviolet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 70
- 239000002351 wastewater Substances 0.000 title claims abstract description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000007921 spray Substances 0.000 claims abstract description 12
- 239000000919 ceramic Substances 0.000 claims abstract description 10
- 238000012856 packing Methods 0.000 claims abstract description 10
- 238000006385 ozonation reaction Methods 0.000 claims abstract description 9
- 238000005273 aeration Methods 0.000 claims abstract description 6
- 239000004973 liquid crystal related substance Substances 0.000 claims description 4
- 239000003595 mist Substances 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 abstract description 12
- 238000007254 oxidation reaction Methods 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 7
- 230000015556 catabolic process Effects 0.000 abstract description 6
- 238000006731 degradation reaction Methods 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract description 4
- 239000010815 organic waste Substances 0.000 abstract description 2
- 238000005507 spraying Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 9
- 239000007789 gas Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000007115 recruitment Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention discloses the equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water, including circulated sprinkling tower and automatic control system, circulated sprinkling tower bottom connects raw water tank and ozone generator, and circulated sprinkling tower bottom is provided with water solenoid valve, circulated sprinkling tower is provided with the ozonation aerated circulatory system and waste water spray system, the ozonation aerated circulatory system includes the circulating fan for being arranged at the aeration head of circulated sprinkling tower bottom and being arranged between circulated sprinkling tower bottom and top, waste water spray system includes being arranged at the shower nozzle of top and the water circulating pump being arranged between circulated sprinkling tower bottom and top in circulated sprinkling tower, ultraviolet lamp tube and ceramic packing are provided with below shower nozzle, sewage treatment equipment disclosed in this invention organically combines ozone and ultraviolet oxidation, using spraying tower structure, using ozone gas and the reverse Two-way Cycle method of operation of organic wastewater, improve ozone utilization ratio, realize ozone plus ultraviolet efficient circulation degradation of organic waste water.
Description
Technical field
The present invention relates to a kind of sewage treatment equipment, more particularly to a kind of ozone and ultraviolet collaboration interior circulation handle waste water
Equipment.
Background technology
Ozone oxidation is as practical, the efficient high-level oxidation technology of one kind, with oxidability is strong, the reaction time is short, nothing
The advantages of secondary pollution, simple equipment, in bio-refractory waste water such as antibiotic waste water, dyeing waste water, petrochemical industry waste water
Be widely used potentiality in processing procedure.Ozonation technology is not by chroma in waste water, waste water colloidal substance, HTHP and tight
Lattice pH limitation, will not also produce substantial amounts of secondary pollution, can be by the oxidation operation of difficult for biological degradation into carbon dioxide, water
Harmless material is oxidized to Deng inorganic matter, or by poisonous and harmful substance, having become high stability, difficult degradation in water removal has
One of key technology of organic pollutants.
But, there are problems that in ozone further treatment technique practice：(1) ozone solubility in water is low,
Utilization rate is low, and short time internal oxidition effect is limited, causes poor processing effect；(2) ozone and waste water time are shorter, cause big
Measure ozone to waste, add operating cost；(3) ozone has strong oxidizing property, there are problems that secondary pollution；(4) general ozone
Oxidized waste water processing equipment, it is poor to there is gas-liquid contact effect, the problem of occupation area of equipment is big.(5) ozone is easier to big point
Unsaturated bond is broken in son, it is decomposed into small-molecule substance, but continues to aoxidize the ability needs of these small-molecule substances of mineralising
Improve, (6) generally require continuous multi-stage oxidation and can be only achieved preferable treatment effect for some difficult oxidized waste waters, it is necessary to
Many complete equipments are used in series, and add cost of investment.
Uviol lamp light degradation can directly degrade organic molecule, can also act on oxygen molecule generation ozone, Oxidative demage
Chemical bond in organic molecule is broken down into the composition not impacted to environment.But, application office of the uviol lamp in water
Limit has higher colourity in sterilizing mainly due to organic wastewater, and light transmittance is relatively low, uviol lamp in water penetration power compared with
It is weak, and oxygen content is low in waste water, and the ozone that uviol lamp effect is produced is few.
The content of the invention
In order to solve the above technical problems, handling setting for waste water the invention provides a kind of ozone and ultraviolet collaboration interior circulation
It is standby, to reach the treatment effect for improving organic wastewater, make full use of the purpose of ozone and ultraviolet light.
To reach above-mentioned purpose, technical scheme is as follows：
The equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water, including circulated sprinkling tower and automatic control system,
The circulated sprinkling tower bottom connection raw water tank and ozone generator, and circulated sprinkling tower bottom is provided with water solenoid valve, it is described
Circulated sprinkling tower is provided with the ozonation aerated circulatory system and waste water spray system, and the ozonation aerated circulatory system includes being arranged at following
The circulating fan that ring spray is drenched the aeration head of tower bottom and is arranged between circulated sprinkling tower bottom and top, the waste water spray system
System includes being arranged at the shower nozzle of top and the water circulating pump being arranged between circulated sprinkling tower bottom and top in circulated sprinkling tower,
Ultraviolet lamp tube and ceramic packing are provided with below the shower nozzle.
In such scheme, the circulated sprinkling top of tower is provided with the pressure sensor one, smelly being connected with automatic control system
Oxygen concentration sensor, pressure-regulating valve and magnetic valve one.
In such scheme, mesh mist eliminator is provided with above the shower nozzle.
In such scheme, the pressure being connected with automatic control system is respectively equipped with the pipeline before and after the circulating fan and is passed
Sensor two and pressure sensor three.
In such scheme, the pipeline between the ozone generator and circulated sprinkling tower is provided with and automatic control system phase
Magnetic valve two even.
In such scheme, the pipeline between the raw water tank and circulated sprinkling tower is provided with what is be connected with automatic control system
Entering water electromagnetic valve.
In such scheme, the circulated sprinkling tower bottom is provided with the chroma in waste water sensor being connected with automatic control system.
In such scheme, the automatic control system includes liquid crystal touch operation screen, controlling switch button and regulation button.
In such scheme, the shower nozzle, ultraviolet lamp tube and ceramic packing include setting up and down two groups.
By above-mentioned technical proposal, ozone that the present invention is provided and the equipment of ultraviolet collaboration interior circulation processing waste water are by ozone
Oxidation and ultraviolet oxidation are organically combined, inverse using ozone gas and organic wastewater using circulated sprinkling tower structure
To the Two-way Cycle method of operation, ozone utilization ratio is improved, ozone plus ultraviolet efficient circulation degradation of organic waste water is realized.
The equipment has advantages below and beneficial effect：
1st, ozone and ultraviolet combination, good waste water treatment effect, ultraviolet utilization rate are high；
2nd, the continuous oxidation to organic wastewater can be realized in monomer spray column；
3rd, the utilization ratio of ozone is high, and it is low to reduce energy consumption, reduces secondary pollution；
4th, equipment automatic control is run, simple and convenient, operation safety；
5th, equipment is totally simple and easy to apply, and manufacture and use cost is low, it is easy to promotes and runs in organic wastewater industry.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
There is the accompanying drawing used required in technology description to be briefly described.
Fig. 1 shows for the device structure of a kind of ozone disclosed in the embodiment of the present invention and ultraviolet collaboration interior circulation processing waste water
It is intended to.
In figure, 1, automatic control system；2nd, pressure sensor two；3rd, circulating fan；4th, pressure sensor three；5th, recirculated water
Pump；6th, chroma in waste water sensor；7th, pressure sensor one；8th, ozone concentration sensor；9th, pressure-regulating valve；10th, magnetic valve one；
11st, mesh mist eliminator；12nd, ultraviolet lamp tube；13rd, shower nozzle；14th, ceramic packing；15th, circulated sprinkling tower；16th, aeration head；17th, water outlet
Magnetic valve；18th, entering water electromagnetic valve；19th, raw water tank；20th, magnetic valve two；21st, ozone generator.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described.
The invention provides the equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water, structure as shown in Figure 1 should
Equipment handles waste water efficiency high.
The equipment that ozone as shown in Figure 1 and ultraviolet collaboration interior circulation handle waste water, including circulated sprinkling tower 15 and automatic
Control system 1, the bottom of circulated sprinkling tower 15 connects raw water tank 19 and ozone generator 21, and the bottom of circulated sprinkling tower 15 is provided with out
Water solenoid valve 17.Circulated sprinkling tower 15 is provided with the ozonation aerated circulatory system and waste water spray system, ozonation aerated circulatory system bag
Include the aeration head 16 for being uniformly arranged on the bottom of circulated sprinkling tower 15 and be arranged at following between the bottom of circulated sprinkling tower 15 and top
Ring blower fan 3, waste water spray system includes being uniformly arranged on the shower nozzle 13 above in circulated sprinkling tower 15 and is arranged at circulated sprinkling
Water circulating pump 5 between the bottom of tower 15 and top, the lower section of shower nozzle 13 is provided with ultraviolet lamp tube 12 and ceramic packing 14.The present embodiment
In, shower nozzle 13, ultraviolet lamp tube 12 and ceramic packing 14 include setting up and down two groups.
The top of circulated sprinkling tower 15 is provided with pressure sensor 1, the ozone concentration sensor being connected with automatic control system 1
8th, pressure-regulating valve 9 and magnetic valve 1.The top of shower nozzle 13 is provided with mesh mist eliminator 11.Automatic control system 1 is touched including liquid crystal
Operator control panel, controlling switch button and regulation button are touched, liquid crystal touch operation screen shows system operational parameters.
The pressure sensor 22 and pressure being connected with automatic control system 1 are respectively equipped with pipeline before and after circulating fan 3
Sensor 34.Pressure difference exceedes warning value scope before and after circulating fan 3, and automatic control system 1 is by alarm, if pressure
Difference exceedes safety value, and automatic control system 1 will control all devices out of service.
Pipeline between ozone generator 21 and circulated sprinkling tower 15 is provided with the magnetic valve being connected with automatic control system 1
2 20.Pipeline between raw water tank 19 and circulated sprinkling tower 15 is provided with the entering water electromagnetic valve 18 being connected with automatic control system 1.
The bottom of circulated sprinkling tower 15 is provided with the chroma in waste water sensor 6 being connected with automatic control system 1.
Operational process is as follows：
The control of automatic control system 1 magnetic valve 1, entering water electromagnetic valve 18 are opened, and the sewage in raw water tank 19 passes through pipeline
Into circulated sprinkling tower 15, when inflow appropriate (time control/Liquid level), entering water electromagnetic valve 18, magnetic valve 1 are closed
Close；The control ozone generator 21 of automatic control system 1 starts, magnetic valve 2 20 is opened, and ozone enters circulated sprinkling tower through pipeline
15, now gas pressure intensity gradually increases in circulated sprinkling tower 15, and when reaching certain numerical value, pressure-regulating valve 9 is touched, discharged
The upper air of circulated sprinkling tower 15, maintains the internal pressure balance of circulated sprinkling tower 15, when ozone amount reaches that certain value (control by the time
System), the control ozone generator 21 of automatic control system 1 stops, magnetic valve 2 20 is closed；Automatic control system 1 controls recirculated water
Pump 5, circulating fan 3, ultraviolet lamp tube 12 start, under ozone and ultraviolet effect, and waste water is in the internal oxidation treatment of circulated sprinkling tower 15；
Through operation after a while, the ozone in circulated sprinkling tower 15 is consumed, when ozone concentration sensor 8 detects ozone concentration
Be reduced to can discharge standard when, the control of automatic control system 1 water circulating pump 5, circulating fan 3, ultraviolet lamp tube 12 stop, and control smelly
Oxygen Generator 21 starts, magnetic valve 2 20 is opened, and ozone enters circulated sprinkling tower 15 through pipeline supplement, in pressure-regulating valve 9
Under regulation, the top light concentration gas discharge of circulated sprinkling tower 15 is automatic to control when ozone magnitude of recruitment reaches certain value (time control)
The control of system 1 ozone generator 21 processed stops, magnetic valve 2 20 is closed；Automatic control system 1 controls water circulating pump 5, followed again
Ring blower fan 3, ultraviolet lamp tube 12, which start ... repeats continuous operation, when the detection chroma in waste water of chroma in waste water sensor 6 is up to standard,
Automatic control system 1 stops the part of all operations, and control magnetic valve 1, water solenoid valve 17 are opened, the dirt handled well
Water is discharged by circulated sprinkling tower 15；The control of automatic control system 1 water solenoid valve 17 is closed after sewage emptying.Again intake, enter
Waste water circulation is handled row next time.
The circulating path of waste water is：
Waste water extracts through water circulating pump 5 in the bottom of circulated sprinkling tower 15 and is transported to the top of circulated sprinkling tower 15, through uniform point
The shower nozzle 13 of cloth is sprayed, and waste water is contacted by light degradation in dropping process with ultraviolet lamp tube 12, is oxidized with ozone contact, waste water
Contacted with ceramic packing 14 so that waste water is uniformly distributed, finally reach the bottom of circulated sprinkling tower 15.
The circulating path of ozone is：
The ozone at the top of circulated sprinkling tower 15, extracts through circulating fan and is transported to the bottom of circulated sprinkling tower 15, through uniform point
The aeration head 16 of cloth is sprayed, and ozone is fully contacted with the bottom waste water of circulated sprinkling tower 15, and oxidation Decomposition is given up Organic substance in water, ozone
Contact, continued oxidation waste water, by ceramic packing 14, contacted with ultraviolet lamp tube 12 with the recirculated water of whereabouts in uphill process,
The partial oxidation for decomposing generation regenerates organic exhaust gas in ozone, gas in ozone and ultraviolet in the presence of uviol lamp
It is decomposed under effect, finally reaches the top of circulated sprinkling tower 15.
For ensure circulated sprinkling tower 15 safe operation carried out unique design, be provided with the top of it pressure sensor 7,
Pressure-regulating valve 9, magnetic valve 1.When ozone air inlet, the internal pressure of circulated sprinkling tower 15 is stepped up, and reaches that pressure is adjusted
When valve 9 sets numerical value, pressure-regulating valve 9 is opened, the internal pressure of balanced recycle spray column 15；If there is failure, pressure reaches
When pressure-regulating valve 9 sets numerical value, and pressure-regulating valve 9 is when being not turned on, and pressure sensor 7 is by data transfer to automatically controlling
System 1, when pressure values exceed warning value scope, automatic control system 1 will control magnetic valve 1 to open, release cycle spray column
15 internal gas.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or using the present invention.
A variety of modifications to these embodiments will be apparent for those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, it is of the invention
The embodiments shown herein is not intended to be limited to, and is to fit to and principles disclosed herein and features of novelty phase one
The most wide scope caused.
Claims (9)
1. the equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water, including circulated sprinkling tower and automatic control system, institute
Circulated sprinkling tower bottom connection raw water tank and ozone generator are stated, and circulated sprinkling tower bottom is provided with water solenoid valve, its feature
It is, the circulated sprinkling tower is provided with the ozonation aerated circulatory system and waste water spray system, the ozonation aerated circulatory system bag
The circulating fan for being arranged at the aeration head of circulated sprinkling tower bottom and being arranged between circulated sprinkling tower bottom and top is included, it is described
Waste water spray system includes being arranged at the shower nozzle above in circulated sprinkling tower and is arranged between circulated sprinkling tower bottom and top
Water circulating pump, be provided with ultraviolet lamp tube and ceramic packing below the shower nozzle.
2. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
State circulated sprinkling top of tower and be provided with the pressure sensor one being connected with automatic control system, ozone concentration sensor, pressure regulation
Valve and magnetic valve one.
3. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
State and mesh mist eliminator is provided with above shower nozzle.
4. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
State and be respectively equipped with the pressure sensor two and pressure sensor three being connected with automatic control system on the pipeline before and after circulating fan.
5. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
State the pipeline between ozone generator and circulated sprinkling tower and be provided with the magnetic valve two being connected with automatic control system.
6. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
State the pipeline between raw water tank and circulated sprinkling tower and be provided with the entering water electromagnetic valve being connected with automatic control system.
7. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
State circulated sprinkling tower bottom and be provided with the chroma in waste water sensor being connected with automatic control system.
8. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
Stating automatic control system includes liquid crystal touch operation screen, controlling switch button and regulation button.
9. the equipment that a kind of ozone according to claim 1 and ultraviolet collaboration interior circulation handle waste water, it is characterised in that institute
Shower nozzle, ultraviolet lamp tube and ceramic packing are stated including setting up and down two groups.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710269192.XA CN106976951A (en) | 2017-04-24 | 2017-04-24 | The equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710269192.XA CN106976951A (en) | 2017-04-24 | 2017-04-24 | The equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106976951A true CN106976951A (en) | 2017-07-25 |
Family
ID=59346024
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710269192.XA Pending CN106976951A (en) | 2017-04-24 | 2017-04-24 | The equipment that a kind of ozone and ultraviolet collaboration interior circulation handle waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106976951A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107459125A (en) * | 2017-09-08 | 2017-12-12 | 水利部交通运输部国家能源局南京水利科学研究院 | A kind of sewage disposal reaction unit |
| CN108557986A (en) * | 2018-06-26 | 2018-09-21 | 苏州他山石环保科技有限公司 | A kind of efficient purifying sewage quickly treating column |
| CN108911113A (en) * | 2018-09-19 | 2018-11-30 | 南京大学盐城环保技术与工程研究院 | A kind of advanced oxidation device of efficient process organic wastewater with difficult degradation thereby |
| CN109319918A (en) * | 2017-08-01 | 2019-02-12 | 王守国 | A kind of ozone high grade oxidation removal COD of sewage device |
| CN114735804A (en) * | 2022-03-22 | 2022-07-12 | 温州大学 | Waste water oxidation decoloration system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005254136A (en) * | 2004-03-11 | 2005-09-22 | Ngk Insulators Ltd | Device for treating organic material-containing water by ozone |
| CN104003504A (en) * | 2014-05-09 | 2014-08-27 | 中国科学院过程工程研究所 | Catalytic ozonation treating apparatus and process for refractory organic wastewater |
| CN104803469A (en) * | 2015-05-15 | 2015-07-29 | 天津理工大学 | Ozone, ultraviolet light and ultrasonic wave synergistic wastewater treatment device and working method thereof |
| CN206666212U (en) * | 2017-04-24 | 2017-11-24 | 青岛蓝皑环保节能有限公司 | The equipment of circular treatment waste water in a kind of ozone and ultraviolet collaboration |
-
2017
- 2017-04-24 CN CN201710269192.XA patent/CN106976951A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005254136A (en) * | 2004-03-11 | 2005-09-22 | Ngk Insulators Ltd | Device for treating organic material-containing water by ozone |
| CN104003504A (en) * | 2014-05-09 | 2014-08-27 | 中国科学院过程工程研究所 | Catalytic ozonation treating apparatus and process for refractory organic wastewater |
| CN104803469A (en) * | 2015-05-15 | 2015-07-29 | 天津理工大学 | Ozone, ultraviolet light and ultrasonic wave synergistic wastewater treatment device and working method thereof |
| CN206666212U (en) * | 2017-04-24 | 2017-11-24 | 青岛蓝皑环保节能有限公司 | The equipment of circular treatment waste water in a kind of ozone and ultraviolet collaboration |
Non-Patent Citations (1)
| Title |
|---|
| 中国化工学会科普工作委员会组织编写；林义英编: "《气体吸收》", 30 September 1986, 化学工业出版社 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109319918A (en) * | 2017-08-01 | 2019-02-12 | 王守国 | A kind of ozone high grade oxidation removal COD of sewage device |
| CN107459125A (en) * | 2017-09-08 | 2017-12-12 | 水利部交通运输部国家能源局南京水利科学研究院 | A kind of sewage disposal reaction unit |
| CN108557986A (en) * | 2018-06-26 | 2018-09-21 | 苏州他山石环保科技有限公司 | A kind of efficient purifying sewage quickly treating column |
| CN108911113A (en) * | 2018-09-19 | 2018-11-30 | 南京大学盐城环保技术与工程研究院 | A kind of advanced oxidation device of efficient process organic wastewater with difficult degradation thereby |
| CN114735804A (en) * | 2022-03-22 | 2022-07-12 | 温州大学 | Waste water oxidation decoloration system |
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