CN208869371U - A kind of micro-nano high-level oxidation technology equipment - Google Patents
A kind of micro-nano high-level oxidation technology equipment Download PDFInfo
- Publication number
- CN208869371U CN208869371U CN201821297764.1U CN201821297764U CN208869371U CN 208869371 U CN208869371 U CN 208869371U CN 201821297764 U CN201821297764 U CN 201821297764U CN 208869371 U CN208869371 U CN 208869371U
- Authority
- CN
- China
- Prior art keywords
- micro
- nano
- connect
- oxidizing tower
- static mixer
- 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.)
- Active
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model relates to a kind of micro-nano high-level oxidation technology equipment, including micro-nano generator, air compressor machine, energy dissipating release, static mixer, micro-nano oxidizing tower, high-pressure hydraulic pump and chemicals dosing plant；Air compressor machine is connect with the air inlet of micro-nano generator, and the gas outlet of micro-nano generator is connect with energy dissipating release, and energy dissipating release is connect with static mixer, and static mixer is connect with micro-nano oxidizing tower, and chemicals dosing plant is connect with static mixer；The top of micro-nano oxidizing tower is equipped with overflow supernatant effluent tank, is equipped with refluxing opening in the middle part of the side wall of micro-nano oxidizing tower, refluxing opening is connect with micro-nano generator by high-pressure hydraulic pump.COD in waste water can be effectively removed according to the COD content in waste water, adjustment and increase and decrease dosage and be reached 50mg/L or less outlet by the utility model.During the reaction, do not increase the coloration in waste water, do not generate floccule body, have the characteristics that the reaction time is short, added amount of chemical is few, high-efficient.
Description
Technical field
The utility model relates to technical field of sewage, especially a kind of micro-nano high-level oxidation technology equipment.
Background technique
Sewage treatment is the water quality requirement for draining a certain water body to reach sewage or reusing, and is purified to it
Process.Environment protection sewage administers industry there are COD contents and is high at present, problem poisonous and harmful, processing difficulty is big difficult to degrade.
Utility model content
The purpose of this utility model is to provide for a kind of micro-nano high-level oxidation technology equipment, to solve in the prior art
The problem that COD of sewage content is high after processing and processing difficulty is big.
The technical solution of the utility model is:
A kind of micro-nano high-level oxidation technology equipment, including micro-nano generator, air compressor machine, energy dissipating release, static state are mixed
Clutch, micro-nano oxidizing tower, high-pressure hydraulic pump and chemicals dosing plant；
The air compressor machine is connect with the air inlet of the micro-nano generator, the gas outlet of the micro-nano generator and institute
The connection of energy dissipating release is stated, the energy dissipating release is connect with the static mixer, the static mixer and the micro-nano
Rice oxidizing tower connection, the chemicals dosing plant are connect with the static mixer；
The top of the micro-nano oxidizing tower is equipped with overflow supernatant effluent tank, the side wall middle part of the micro-nano oxidizing tower
Equipped with refluxing opening, the refluxing opening is connect with the micro-nano generator by the high-pressure hydraulic pump；
The air inlet of the micro-nano generator is equipped with nanoscale diaphragm.
In above-mentioned micro-nano high-level oxidation technology equipment, the chemicals dosing plant includes medicinal liquid agitating machine and diaphragm dosing pump,
The medicinal liquid agitating machine is connect with the diaphragm dosing pump.
In above-mentioned micro-nano high-level oxidation technology equipment, the quantity of the high-pressure hydraulic pump is two.
The beneficial effects of the utility model are: waste water is made during processing using novel micro nanometer rice high-level oxidation technology,
Water body is become the water body of micro/nano level by moment, increases water body specific surface area, is sufficiently mixed, is contacted with oxidant, is improved useless
Electrolyte in water supplements potential difference, decomposes the poisonous and harmful substance in sewage, is removed by oxidation, decomposition, chain-scission degradation useless
The COD of removal difficult to degrade in water, through industrialization with processing, front process drains COD content in 500mg/L or less, root
According to the COD content in waste water, COD in waste water can be effectively removed and be reached 50mg/L or less outlet by adjustment and increase and decrease dosage.
During the reaction, do not increase the coloration in waste water, do not generate floccule body, it has, and the reaction time is short, added amount of chemical is few, effect
The features such as rate is high.The utility model treatment effeciency is high, easy to operate, single set processing 5m3/h—1000m3/h；It is applied widely,
Mark transformation is proposed suitable for all kinds of sewage treatments and sewage plant.
Detailed description of the invention
Fig. 1 is the structural schematic diagram that the utility model shows a kind of micro-nano high-level oxidation technology equipment.
In figure: 1. micro-nano generators, 2. air compressor machines, 3. energy dissipating releases, 4. static mixers, 5. micro-nano oxygen
Change tower, 51. refluxing openings, 52. overflow supernatant effluent tanks, 6. high-pressure hydraulic pumps, 7. chemicals dosing plants, 71. medicinal liquid agitating machines, 72.
Diaphragm dosing pump.
Specific embodiment
In order to more clearly state the utility model, the utility model is further described with reference to the accompanying drawing.
As shown in Figure 1, the utility model provides a kind of micro-nano high-level oxidation technology equipment, including micro-nano generator 1,
Air compressor machine 2, energy dissipating release 3, static mixer 4, micro-nano oxidizing tower 5, high-pressure hydraulic pump 6 and chemicals dosing plant 7；
The air compressor machine 2 is connect with the air inlet of the micro-nano generator 1, the gas outlet of the micro-nano generator 1
Connect with the energy dissipating release 3, the energy dissipating release 3 is connect with the static mixer 4, the static mixer 4 with
The micro-nano oxidizing tower 5 connects, and the chemicals dosing plant 7 is connect with the static mixer 4；
Micro-nano generator 1 is the key component of whole equipment, and the quality which generates nanoscale micro air bubble is direct
Influence system treatment effect.The utility model uses unique mechanism, special structure, and volume only has traditional tank structure
/ 15th (identical equipment treating capacity is compared), but the quality of micro-nano generator 1, operation, maintenance will far superior to pass
System structure.It is added in water in micro-nano generator 1 using compressed air；By air, water is forced into 5.5kg/cm2；Micro-
The nanometer inner water of generator 1 is in 5.0kg/cm210-15 s is stopped under pressure, such air is just dissolved into water, micro-nano efficiency
Up to 99.9% or more；When pressure water passes through novel micro nanometer rice relief valve, micro-nano bubble drops suddenly from the high pressure before relief valve
For normal pressure, water flow section becomes larger suddenly, and micro-nano bubble is by energy dissipating, thus form micro-nano bubble mixing in water, such mistake
The micro-nano bubble that journey is formed is very small, a diameter of nanoscale, and diameter accounts for 95% or more of sum in nanoscale bubble
The top of the micro-nano oxidizing tower 5 is equipped with overflow supernatant effluent tank 52, the side wall of the micro-nano oxidizing tower 5
Middle part is equipped with refluxing opening 51, and the refluxing opening 51 is connect with the micro-nano generator 1 by the high-pressure hydraulic pump 6；
Overflow supernatant effluent tank 52 has handled water up to standard for being discharged.
The air inlet of the micro-nano generator 1 is equipped with nanoscale diaphragm.Nanoscale diaphragm is mainly used to allow high pressure gas
Even into the water body entered with high pressure generates micro-nano misty water body continually by high pressure in micro-nano generator 1
Output.
High-pressure hydraulic pump 6 flows back into treated the certain media pressurization of micro-nano oxidizing tower 5 in micro-nano generator 1,
Reflux ratio is generally the 30-50% for the treatment of capacity, at the same air compressor machine 2 pressure air is entered by special nanoscale diaphragm it is micro-nano
In generator 1, the mixed at high speed both in micro-nano generator 1, being formed, there is the blending agent of about 0.5MPa pressure to pass through pipe
Road enters in energy dissipating release 3, discharges a large amount of intensive nanoscale micro air bubbles in water to be processed in energy dissipating release 3,
And it is quickly sufficiently mixed with the fine media in water, static mixer 4, energy dissipating release can be added in medicament by chemicals dosing plant 7
After treated the raw water of device 3 and medicament are sufficiently mixed, into micro-nano oxidizing tower 5, nanoscale microbubble is in micro-nano oxidation
The rate of climb is very slow in tower 5, and disturbance is smaller, constantly generation oxidation reaction, so that waste water be made to be purified.It is arranged in micro-nano oxygen
Change 5 residence time of tower is 20-30min, and clear water is uniformly collected and is discharged by overflow supernatant effluent tank 52 by outlet water at tail end weir,
Refluxing opening 51 is connected to high-pressure hydraulic pump 6 to flow back for micro-nano generator 1.
In above-mentioned micro-nano high-level oxidation technology equipment, the chemicals dosing plant 7 includes medicinal liquid agitating machine 71 and diaphragm dosing
Pump 72, the medicinal liquid agitating machine 71 is connect with the diaphragm dosing pump 72.Medical fluid can be sufficiently mixed uniformly by medicinal liquid agitating machine 71,
And static mixer 4 is delivered to by diaphragm dosing pump 72.
In above-mentioned micro-nano high-level oxidation technology equipment, the quantity of the high-pressure hydraulic pump 6 is two.Two high-pressure hydraulic pumps 6
Design is the using and the reserved.If being broken one in the process of running, another can star, easy to repair and raising work effect
Rate.
The embodiment created above to the utility model is described in detail, but the content is only the utility model wound
The preferred embodiment made, should not be considered as limiting the scope of the present invention.It is all to create range according to the utility model
Made all the changes and improvements etc., shall still fall within the scope of this patent.
Claims (3)
1. a kind of micro-nano high-level oxidation technology equipment, it is characterised in that: including micro-nano generator (1), air compressor machine (2) disappears
It can release (3), static mixer (4), micro-nano oxidizing tower (5), high-pressure hydraulic pump (6) and chemicals dosing plant (7)；
The air compressor machine (2) connect with the air inlet of the micro-nano generator (1), the outlet of the micro-nano generator (1)
Mouth is connect with the energy dissipating release (3), and the energy dissipating release (3) connect with the static mixer (4), described static mixed
Clutch (4) is connect with the micro-nano oxidizing tower (5), and the chemicals dosing plant (7) connect with the static mixer (4)；
The top of the micro-nano oxidizing tower (5) is equipped with overflow supernatant effluent tank (52), the side of the micro-nano oxidizing tower (5)
Refluxing opening (51) are equipped in the middle part of wall, the refluxing opening (51) and the micro-nano generator (1) are connected by the high-pressure hydraulic pump (6)
It connects；
The air inlet of the micro-nano generator (1) is equipped with nanoscale diaphragm.
2. micro-nano high-level oxidation technology equipment according to claim 1, it is characterised in that: chemicals dosing plant (7) packet
Medicinal liquid agitating machine (71) and diaphragm dosing pump (72) are included, the medicinal liquid agitating machine (71) connect with the diaphragm dosing pump (72).
3. micro-nano high-level oxidation technology equipment according to claim 1, it is characterised in that: the high-pressure hydraulic pump (6)
Quantity is two.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821297764.1U CN208869371U (en) | 2018-08-13 | 2018-08-13 | A kind of micro-nano high-level oxidation technology equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821297764.1U CN208869371U (en) | 2018-08-13 | 2018-08-13 | A kind of micro-nano high-level oxidation technology equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208869371U true CN208869371U (en) | 2019-05-17 |
Family
ID=66464517
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821297764.1U Active CN208869371U (en) | 2018-08-13 | 2018-08-13 | A kind of micro-nano high-level oxidation technology equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208869371U (en) |
-
2018
- 2018-08-13 CN CN201821297764.1U patent/CN208869371U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104710002B (en) | A kind of micro-nano aeration and catalyzing ozonisation waste water treatment system of two-stage | |
| CN102115253B (en) | Novel multi-technology synergetic catalysis advanced micro-bubble ozone oxidation tower | |
| CN109304108B (en) | Micro-nano bubble generation device and method and application of micro-nano bubble generation device and method in dye wastewater treatment | |
| CN203498231U (en) | Supercritical dissolved gas cavitation device for strengthening reduction of sludge | |
| CN104876375A (en) | Deep oxidization water treatment method and deep oxidization water treatment device | |
| CN207581601U (en) | A kind of percolate MBR is discharged full dose processing system | |
| CN104787981A (en) | Low BC ratio wastewater advanced treatment method of DMTO device and treatment plant | |
| JP2001502962A (en) | Method and apparatus for mixing gas and fluid | |
| CN206337111U (en) | A kind of composite catalytic oxidation UF membrane wastewater treatment integrating device | |
| CN208869371U (en) | A kind of micro-nano high-level oxidation technology equipment | |
| CN101708910B (en) | Sewage disposal plant combining coagulation and air flotation | |
| CN108275848A (en) | A kind of wastewater treatment integrating device and method | |
| CN108689480A (en) | A kind of advanced sewage oxidation processing equipment | |
| CN105293832A (en) | Polyformaldehyde production wastewater treatment apparatus and method therefor | |
| CN205258202U (en) | Pharmaceutical chemical engineering effluent treatment plant | |
| CN106145437A (en) | The processing method of a kind of oilfield drilling fracturing outlet liquid and system | |
| CN202124516U (en) | Bypass aerating apparatus | |
| CN205023987U (en) | Take sewage treatment plant in charge device and flocculation air supporting pond | |
| CN208667385U (en) | A kind of wastewater treatment integrating device | |
| KR100904722B1 (en) | Apparatus for generating micro-buble | |
| CN205603384U (en) | Flowing back, flushing fluid , tertiary oil recovery are returned including processing apparatus who gathers waste liquid to fracturing | |
| CN205275404U (en) | Gather formaldehyde production sewage treatment plant | |
| CN211226523U (en) | Catalytic ozonation reactor for wastewater treatment | |
| JPH09290280A (en) | Ozone contact tank and control method therefor | |
| CN108275810A (en) | Drilling waste water deep oxidation processing method containing polysulfonate slurry and its application |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |