CN209685364U - The catalyzing integrated reactor of up-flow ozone-ultraviolet - Google Patents
The catalyzing integrated reactor of up-flow ozone-ultraviolet Download PDFInfo
- Publication number
- CN209685364U CN209685364U CN201920128614.6U CN201920128614U CN209685364U CN 209685364 U CN209685364 U CN 209685364U CN 201920128614 U CN201920128614 U CN 201920128614U CN 209685364 U CN209685364 U CN 209685364U
- Authority
- CN
- China
- Prior art keywords
- ultraviolet
- ozone
- rectification
- shell
- integrated reactor
- 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)
- Physical Water Treatments (AREA)
Abstract
The utility model discloses a kind of catalyzing integrated reactors of up-flow ozone-ultraviolet in sewage treatment field.This kind of catalyzing integrated reactor of up-flow ozone-ultraviolet, shell including inner hollow, it is set to the rectification casing at interior of shell center, it is set to the ultraviolet component of rectification inside pipe casing and is set to the gas release device of rectification sleeve bottom, side wall of outer shell lower part is respectively arranged with inlet and ozone interface, ozone interface is connected to gas release device, side wall of outer shell top is provided with liquid outlet, cover top portion is provided with blow vent, side wall of outer shell bottom is additionally provided with drain, rectification sleeve upper end and lower end pass through sleeve bearing and cage connection respectively, rectification sleeve upper end is connected to interior of shell respectively with lower end.The catalyzing integrated reactor resource utilization height of this kind of up-flow ozone-ultraviolet, high treating effect, low energy consumption, environmentally protective, wide adaptation range, use flexibly are high.
Description
Technical field
The utility model relates to technical field of sewage, in particular to a kind of catalyzing integrated reaction of up-flow ozone-ultraviolet
Device.
Background technique
With the development of sewage disposal technology, high-level oxidation technology obtains biggish development, based on the exploitation of OH theory
All kinds of reactors mainly have Fenton, class Fenton reactor and photooxidation reaction device two major classes, the former is reacted by chemical catalysis,
Free electron and hole of the latter by ultraviolet light excitation generation, generate OH and superoxide ion by water, oxygen capture, thus
By direct mineralization of organic material, photooxidation reaction device mostly uses mercury lamp to make ultraviolet lamp.
There is energy consumption height in existing Fenton and class Fenton advanced oxidation reaction device, dosage is big, system complex, generate chemistry
Sludge causes the disadvantages of secondary pollution, that there are oxidation efficiencies is low for photooxidation reaction device, oxidation not exclusively, the disadvantages of energy consumption is high.
Utility model content
The purpose of the utility model is to provide a kind of resource utilization height, the liter that high treating effect, low energy consumption, environmentally protective
The catalyzing integrated reactor of streaming ozone-ultraviolet.
In order to realize above-mentioned purpose of utility model, the catalyzing integrated reactor of the utility model up-flow ozone-ultraviolet is used
Following technical solution:
A kind of catalyzing integrated reactor of up-flow ozone-ultraviolet, shell including inner hollow are set in interior of shell
The rectification casing of the heart, the ultraviolet component for being set to rectification inside pipe casing and the gas release device for being set to rectification sleeve bottom,
The side wall of outer shell lower part is respectively arranged with inlet and ozone interface, and the ozone interface is connected to gas release device, described
Side wall of outer shell top is provided with liquid outlet, and the cover top portion is provided with blow vent, and the side wall of outer shell bottom, which is additionally provided with, puts
It eats dishes without rice or wine, the rectification sleeve upper end and lower end pass through sleeve bearing and cage connection, the rectification sleeve upper end and lower end respectively
It is connected to respectively with interior of shell.The ozone interface other end is connected with ozone generator, through gas generator in rectification casing
It is passed through ozone, rectifying lower part in casing becomes gas-water mixing zone, and density becomes smaller risings, forms negative pressuren zone, generation force of circulation is whole
Flow jacket exterior liquid from rectification sleeve bottom sucking, to form circulation, the organic pollutant in sewage is in ozone and ultraviolet
Mineralising is eliminated or degrades under the collective effect of light.
The rectification casing is the quartz socket tube of both ends sealing, and the quartz socket tube side wall is provided with to ultraviolet assembly power supply
Power interface one, the shell is provided with power interface two corresponding with power interface one.Quartz socket tube make ultraviolet component with
Ultraviolet component is isolated with sewage, avoids ultraviolet component by corrosion in water by the isolating device of sewage.
The ultraviolet component is combined into annular lamp bracket using LED ultraviolet lamp belt.Ultraviolet component uses LED ultraviolet lamp belt, body
Product is small, light weight and cost is low, and low energy consumption, high reliablity；Single failure lamp bead can be replaced, compare existing mercury lamp, safeguarded
It is at low cost, and do not cause mercury pollution；Component uses circular lamp band longitudinal direction multi-tier arrangement, and individual lamp beads or light bar failure are to reactor
Influence on system operation very little, therefore high reliablity.
The shell and rectification casing are cylindrical shape.Sewage circulation is more evenly.
The inlet, liquid outlet, drain and ozone interface are connected separately with solenoid valve, the solenoid valve with control
Device connection.It is controlled by controller setting program, realizes automatic running.
Compared with prior art, the utility model has the beneficial effects that: ozone and ultraviolet light are concentrated on the confined space
It is interior, space self-energy density is greatly improved, to increase the collision probability of ozone and ultraviolet light and object processed, improves oxidation
Efficiency improves ozone and utilization rate of ultraviolet light, while the mechanical energy that ozone gas carries is used for gas lift circulation, strengthens to spreading
Matter, improve oxidation effectiveness, thus the effect that ozone can play is performed to it is ultimate attainment, to greatest extent will production ozone generation
Energy consumption is for aoxidizing organic pollutant.
The utility model can be improved according to the difference of processing sewage by additional Fenton or class Fenton medicament or catalyst
Wastewater treatment efficiency can also flexibly use air as force of circulation operation.
To sum up, have the advantages of the utility model: resource utilization height, high reliablity, high treating effect, low energy consumption, green
Environmental protection, wide adaptation range, use flexibly are high.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Wherein, 1 shell, 11 power interfaces one, 12 power interfaces two, 2 quartz socket tubes, 21 sleeve bearings, 3 ultraviolet components, 4
Gas release device, 5 inlets, 6 ozone interfaces, 7 liquid outlets, 8 blow vents, 9 drains.
Specific embodiment
With reference to embodiment, the utility model is furtherd elucidate, it should be understood that these embodiments are only used for
Bright the utility model rather than limitation the scope of the utility model, after having read the utility model, those skilled in the art
Member falls within the application range as defined in the appended claims to the modification of the various equivalent forms of the utility model.
It should also be noted that similar label and letter indicate similar terms in following attached drawing, therefore, once a certain Xiang Yi
It is defined in a attached drawing, does not then need that it is further defined and explained in subsequent attached drawing.
In the description of the present invention, it should be noted that the orientation or position of the instructions such as term "vertical", " outer peripheral surface "
Set relationship be based on the orientation or positional relationship shown in the drawings or the utility model product using when the orientation usually put
Or positional relationship, be merely for convenience of describing the present invention and simplifying the description, rather than the device of indication or suggestion meaning or
Element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as the limit to the utility model
System.In addition, term " first ", " second ", " third " etc. are only used for distinguishing description, it is not understood to indicate or imply relatively heavy
The property wanted.
In addition, the terms such as term "vertical" are not offered as requiring component abswolute level or pendency, but can be slightly tilted.
It is not to indicate that the structure is had to fully horizontally if "horizontal" only refers to that its direction is more horizontal with respect to for "vertical",
But it can be slightly tilted.
In the description of the present invention, it should also be noted that, unless otherwise clearly defined and limited, term " is set
Set ", " installation ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection,
Or it is integrally connected；It can be mechanical connection, be also possible to be electrically connected；It can be directly connected, intermediary can also be passed through
It is indirectly connected, can be the connection inside two elements.For the ordinary skill in the art, it can be managed with concrete condition
Solve the concrete meaning of above-mentioned term in the present invention.
As shown in Figure 1, a kind of catalyzing integrated reactor of up-flow ozone-ultraviolet, cylinder-like shell 1 including inner hollow,
It is set to the cylindric rectification casing of 1 inside center of shell, the ultraviolet component 3 of rectification inside pipe casing is set to and is set to whole
The gas release device 4 of sleeve bottom, the quartz socket tube 2 that rectification casing seals between the casing of both ends are flowed, 2 side wall of quartz socket tube is set
It is equipped with the power interface 1 powered to ultraviolet component 3, shell 1 is provided with power interface two corresponding with power interface 1
12,1 lower sidewall of shell is respectively arranged with inlet 5 and ozone interface 6, and ozone interface 6 is connected to gas release device 4, shell 1
Side wall upper part is provided with liquid outlet 7, and blow vent 8 is provided at the top of shell 1, and 1 sidewall bottom of shell is additionally provided with drain 9, stone
2 top and bottom of English casing pass through sleeve bearing 21 respectively and shell 1 is affixed, 2 top and bottom of quartz socket tube respectively with shell 1
Inside connection, ultraviolet component 3 are combined into annular lamp bracket using LED ultraviolet lamp belt.
The specific work process and principle of the utility model:
It when sequence batch operation, intakes from inlet, until stopping water inlet after liquid outlet water outlet, ultraviolet component is powered, and passes through gas
Generator is passed through ozone in rectification casing, and rectifying lower part in casing becomes gas-water mixing zone, and density becomes smaller risings, formation negative pressure
Area generates force of circulation, and rectification jacket exterior liquid is from rectification sleeve bottom sucking, so that circulation is formed, it is organic in sewage
Pollutant mineralising under the collective effect of ozone and ultraviolet light is eliminated or degradation, and after the reaction was completed, stopping is passed through ozone, closes purple
Outer component releases treated sewage from drain.
When continuous operation, inlet water inlet, liquid outlet water outlet controls gas-water ratio by control ozone intake to control
Circulation processed reaches sewage continuous processing effect.
Ozone oxidation ability is limited, in conjunction with ultraviolet light irradiation, after ultraviolet photodestruciton macromolecule organic, then by smelly
The thorough mineralising of oxygen, ozone are blended with water, under the irradiation of ultraviolet light, generate the more oxidizing species such as OH and superoxide ion,
To improve oxidability, pass through the more efficient processing dirt organic pollutants of ozone and ultraviolet cooperating effect energy.
Although the embodiments of the present invention have been shown and described above, it is to be understood that above-described embodiment is
Illustratively, it should not be understood as limiting the present invention, those skilled in the art are in the scope of the utility model
Inside it can make changes, modifications, alterations, and variations to the above described embodiments.
Claims (5)
1. a kind of catalyzing integrated reactor of up-flow ozone-ultraviolet, it is characterised in that: shell including inner hollow, be set to it is outer
The rectification casing of shell inside center, the ultraviolet component for being set to rectification inside pipe casing and the gas for being set to rectification sleeve bottom
Release, the side wall of outer shell lower part are respectively arranged with inlet and ozone interface, and the ozone interface and gas release device connect
Logical, the side wall of outer shell top is provided with liquid outlet, and the cover top portion is provided with blow vent, and the side wall of outer shell bottom is also set
It is equipped with drain, the rectification sleeve upper end and lower end pass through sleeve bearing and cage connection, the rectification sleeve upper end respectively
It is connected to respectively with interior of shell with lower end.
2. a kind of catalyzing integrated reactor of up-flow ozone-ultraviolet according to claim 1, it is characterised in that: the rectification
Casing is the quartz socket tube of both ends sealing, and quartz socket tube makees the isolating device of ultraviolet component and sewage.
3. a kind of catalyzing integrated reactor of up-flow ozone-ultraviolet according to claim 1, it is characterised in that: described ultraviolet
Component is combined into annular lamp bracket using LED ultraviolet lamp belt.
4. a kind of catalyzing integrated reactor of up-flow ozone-ultraviolet according to claim 1, it is characterised in that: the shell
It is cylindrical shape with rectification casing.
5. a kind of catalyzing integrated reactor of up-flow ozone-ultraviolet according to claim 1, it is characterised in that: the feed liquor
Mouth, liquid outlet, drain and ozone interface are connected separately with solenoid valve, and the solenoid valve is connect with controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920128614.6U CN209685364U (en) | 2019-01-25 | 2019-01-25 | The catalyzing integrated reactor of up-flow ozone-ultraviolet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920128614.6U CN209685364U (en) | 2019-01-25 | 2019-01-25 | The catalyzing integrated reactor of up-flow ozone-ultraviolet |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209685364U true CN209685364U (en) | 2019-11-26 |
Family
ID=68600213
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920128614.6U Active CN209685364U (en) | 2019-01-25 | 2019-01-25 | The catalyzing integrated reactor of up-flow ozone-ultraviolet |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209685364U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111620486A (en) * | 2020-04-22 | 2020-09-04 | 山东大学 | UV-LED/O3Method for treating hexazinone pesticide wastewater in combined mode |
-
2019
- 2019-01-25 CN CN201920128614.6U patent/CN209685364U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111620486A (en) * | 2020-04-22 | 2020-09-04 | 山东大学 | UV-LED/O3Method for treating hexazinone pesticide wastewater in combined mode |
| CN111620486B (en) * | 2020-04-22 | 2021-09-28 | 山东大学 | UV-LED/O3Method for treating hexazinone pesticide wastewater in combined mode |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201473358U (en) | Vortex photocatalysis sewage pretreatment device | |
| CN101875001B (en) | Photocatalytic oxidation-membrane separation circulating fluid bed reaction device | |
| CN203284223U (en) | Jet type ozone photocatalysis-membrane treatment device for organic wastewater | |
| CN108911023B (en) | Circulation type heterogeneous photocatalytic oxidation treatment system and treatment method | |
| CN102874994B (en) | Double-internal circulating water treatment device capable of combining photocatalysis and aerobe, and working method thereof | |
| CN103739039B (en) | A kind of multi-dimensional electro-catalytic equipment | |
| CN110316819A (en) | A kind of high concentrated organic wastewater treatment reactor | |
| CN100444945C (en) | Integrated photo-catalytic oxidation membrane-separation fluidized bed reactor | |
| CN105481051A (en) | Integrated photoelectrocatalysis-membrane separation fluidized bed reaction device | |
| CN103755006B (en) | Integrated heterogeneous deflection plate Fenton flow reactor | |
| CN209685364U (en) | The catalyzing integrated reactor of up-flow ozone-ultraviolet | |
| CN212894039U (en) | Iron-carbon micro-electrolysis wastewater pretreatment device | |
| CN205099517U (en) | Integral type light catalytic oxidation - membrane separation three -phase fluidized bed reaction device | |
| CN205556157U (en) | Industrial waste water advanced treatment unit based on nanometer titanium dioxide takes photocatalysis | |
| CN204625249U (en) | The reactive agent device of photocatalytic waste water treatment | |
| CN114790057B (en) | Photocatalytic sewage double-circulation treatment filtering device | |
| CN104150709B (en) | A kind of embedded preoxidation BAF deep treatment method | |
| CN106277279A (en) | A kind of wastewater treatment equipment being beneficial to magnetic nano-catalyst separation and recovery | |
| CN207072839U (en) | Catalytic ozonation pilot-plant | |
| CN115504562A (en) | Catalytic ozonation reactor | |
| CN214880751U (en) | Device for treating wastewater by microbubble ozone catalytic oxidation coupled hydrogel | |
| CN105060391B (en) | Outer circulation photocatalysis spinning liquid UF membrane coupled reactor for handling organic wastewater | |
| CN108423795A (en) | Efficiently catalyzing and oxidizing device | |
| CN105174361B (en) | Integrated photo-catalytic oxidation-UF membrane three-phase fluidization bed reaction device | |
| CN206368053U (en) | A kind of ultraviolet Fenton advanced oxidation reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |