CN206494802U - Water body purification apparatus - Google Patents

Water body purification apparatus Download PDF

Info

Publication number
CN206494802U
CN206494802U CN201720145520.0U CN201720145520U CN206494802U CN 206494802 U CN206494802 U CN 206494802U CN 201720145520 U CN201720145520 U CN 201720145520U CN 206494802 U CN206494802 U CN 206494802U
Authority
CN
China
Prior art keywords
tank
ejector
water
purification apparatus
water body
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
Application number
CN201720145520.0U
Other languages
Chinese (zh)
Inventor
王国强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hebei Environmental Protection Equipment Ltd By Share Ltd
Original Assignee
Hebei Environmental Protection Equipment Ltd By Share Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hebei Environmental Protection Equipment Ltd By Share Ltd filed Critical Hebei Environmental Protection Equipment Ltd By Share Ltd
Priority to CN201720145520.0U priority Critical patent/CN206494802U/en
Application granted granted Critical
Publication of CN206494802U publication Critical patent/CN206494802U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Physical Water Treatments (AREA)

Abstract

The utility model is related to water body purification apparatus, it includes the ejector that the water pump that import is connected with accessing pending water and right-hand member import are connected with unit fixed on water pump suction, the outlet of water pump is connected with ejector inlet, the air inlet of ejector is connected with ozone generator, the gas liquid outlet of ejector is connected with the lower end import of blender, the upper end outlet of blender is connected with the lower end import of photocatalyst reaction tank, the upper end outlet of photocatalyst reaction tank is connected with the lower end import of catalysis oxidation tank, and the upper end outlet of catalysis oxidation tank is connected with water after processing;The utility model is reasonable in design, compact conformation and easy to use.

Description

Water body purification apparatus
Technical field
The utility model is related to water body purification apparatus.
Background technology
At present, as economic continues to develop, water pollution is also increasingly severe, harmful in water, Environmental estrogen It is more and more etc. micro harmful chemical.Conventional single method for treating water-physics, chemistry, biology etc., it is handled compared with For difficulty, and it is not thorough.And oxidability is not strong in the presence of hydrogen peroxide or chlorine element oxidation all.How a kind of General Office is improved Reason, with low cost, efficient energy-saving cleaning system turn into the technical problem for being badly in need of solving.
Utility model content
For the above, technical problem to be solved in the utility model be generally speaking to provide it is a kind of it is reasonable in design, With low cost, durable, safe and reliable, simple to operate, time saving and energy saving, saving fund, compact conformation and water easy to use Body cleaning equipment;The technical problem and acquirement beneficial effect solved in detail is in aftermentioned content and combination embodiment Content is specifically described.
To solve the above problems, technical solution adopted in the utility model is:
A kind of water body purification apparatus, including the water pump and ejector that import is connected with accessing pending water, the outlet of water pump with Ejector inlet is connected, and the air inlet of ejector is connected with ozone generator, and the gas liquid outlet of ejector is connected with blender Lower end import, the upper end outlet of blender, which is connected with the lower end import of photocatalyst reaction tank, photocatalyst reaction tank, to be brought out Mouth is connected with the lower end import of catalysis oxidation tank, and the upper end outlet of catalysis oxidation tank is connected with water after processing;
Be provided with photocatalyst reaction tank immersion in a liquid and waterproof sealing ultraviolet light, in photocatalyst reaction tank Titanium dioxide layer is provided with inwall, ultraviolet light is radiated on titanium dioxide layer, oxidation is provided with catalysis oxidation top tank structure Aluminium lamination, alumina layer is alveolate texture.
It is used as the further improvement of above-mentioned technical proposal:
Booster pump is provided between the lower end import of the gas liquid outlet and blender of ejector;In blender and photocatalyst Sequence valve is provided between retort.
Also include cold dry tank and oxygenerator;Oxygenerator is connected through cold dry tank with ozone generator import.
Refrigeration machine, cold dry tank pass sequentially through pipeline with ozone generator and connected.
Second flow valve is provided between refrigeration machine and cold dry tank.
First flow valve is connected between safety valve and ejector.
The gas liquid outlet of ejector is provided with check valve.
Safety valve is connected between water pump and ejector.
The spiral mandrel of spiral structure is vertically arranged with blender, is provided with mixer inner walls and spiral Mandrel rotation direction is identical and pitch identical flight.
A kind of water body purification technique, by means of above-mentioned water body purification apparatus, specifically includes following steps:
A:Gas-liquid mixed step, accessing pending water enters ejector by water pump, and ozone enters ejector through ozone generator, Ejector sends out gas liquid mixture after accessing pending water is mixed with ozone by check valve;
B:Ozone purification step is pressurized, simultaneously superatmospheric is strong for the pressure of setting adjustment sequence valve, gas liquid mixture mixing Hybrid reaction in device, and rise from helical duct inside spin;
C:Photocatalyst purifying step:The liquid of sequence valve outflow enters photocatalyst reaction tank, the purple light of immersion in a liquid Light irradiation titanium dioxide layer, ultraviolet irradiation and Titanium Dioxide double purified liquid;
D:Flow out the liquid after step C and enter catalysis oxidation tank, catalyzing, oxidizing and purifying is carried out by honeycomb-shaped oxidizing aluminium lamination, Finally discharge water into water after processing.
It is using the beneficial effect produced by above-mentioned technical proposal:
1. the organic matter of difficult degradation quickly reacts with hydroxyl radical free radical in sewage, by the high molecular organic matter of macromolecular Reaction forms micromolecular compound until generation carbon dioxide, caused result is the COD indexs or quick in quick reduction water Improve BOD/COD numerical value, so as to improve the biodegradable ability of sewage;
2. the low price phosphonium ion in water is oxidized to high price phosphate anion, phosphate anion and the calcium binding in water Calcium phosphate precipitation is formed, the phosphorus content in water is reduced;
3. high-molecular compound or protein due to influenceing ammonia nitrogen index etc. are equally aoxidized by hydroxyl radical free radical, so as to drop Low amino index;
4. due to causing the sulfur-containing compound of stench to be aoxidized by hydroxyl radical free radical, sulfur sesquioxide or sulfur trioxide are formed, Water formation sulfate or sulphite are dissolved in, so that water body fast deodorization;
5. complex compound or chelate in catalysis oxidation water, hydroxyl radical free radical and heavy metal ion reaction bonded formation indissoluble Heavy metal hydroxide precipitation, it is convenient to reclaim and separate, be conducive to the elimination of heavy metal pollution in water;
6. hydroxyl radical free radical can quickly kill algae, mushroom so that water is nontoxic, innoxious.
The beneficial effects of the utility model not limited to this is described, in order to preferably readily appreciate, in embodiment portion Divide and carried out more preferably detailed description.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Wherein:1st, accessing pending water;2nd, water pump;3rd, safety valve;4th, first flow valve;5th, ejector;6th, blender;7th, light is touched Matchmaker's retort;8th, catalysis oxidation tank;9th, water after handling;10th, ozone generator;11st, second flow valve;12nd, refrigeration machine;13rd, it is cold Dry tank;14th, oxygenerator;15th, booster pump;16th, sequence valve;17th, alumina layer;18th, ultraviolet light;19th, titanium dioxide layer.
Embodiment
As shown in figure 1, the water body purification apparatus of the present embodiment, including import and accessing pending water 1(Polluted river channel, cesspool Deng)The water pump 2 and ejector 5 of connection, the outlet of water pump 2 are connected with the inlet of ejector 5, the air inlet connection of ejector 5 There is ozone generator 10, the gas liquid outlet of ejector 5 is connected with the lower end import of blender 6, the upper end outlet connection of blender 6 There is the lower end import of photocatalyst reaction tank 7, the upper end outlet of photocatalyst reaction tank 7 is connected with the lower end import of catalysis oxidation tank 8, The upper end outlet of catalysis oxidation tank 8 is connected with water 9 after processing(Clean river course, clean water pond);
Be provided with photocatalyst reaction tank 7 immersion in a liquid and waterproof sealing ultraviolet light 18, in photocatalyst reaction Titanium dioxide layer 19 is provided with the inwall of tank 7, ultraviolet light 18 is radiated on titanium dioxide layer 19, in the inwall of catalysis oxidation tank 8 On be provided with alumina layer 17, alumina layer 17 is alveolate texture.
Booster pump 15 is provided between the lower end import of the gas liquid outlet and blender 6 of ejector 5;Blender 6 with Sequence valve 16 is provided between photocatalyst reaction tank 7.
Also include cold dry tank 13 and oxygenerator 14;Oxygenerator 14 is connected through cold dry tank 13 with the import of ozone generator 10.
Refrigeration machine 12, cold dry tank 13 pass sequentially through pipeline with ozone generator 10 and connected.
Second flow valve 11 is provided between refrigeration machine 12 and cold dry tank 13.
First flow valve 4 is connected between safety valve 3 and ejector 5.
The gas liquid outlet of ejector 5 is provided with check valve.
Safety valve 3 is connected between water pump 2 and ejector 5.
The spiral mandrel of spiral structure is vertically arranged with blender 6, is provided with and spiral shell on the inwall of blender 6 Revolve that mandrel rotation direction is identical and pitch identical flight.
The water body purification technique of the present embodiment, by means of above-mentioned water body purification apparatus, specifically includes following steps:
A:Gas-liquid mixed step, accessing pending water 1 enters ejector 5 by water pump 2, and ozone enters incidence through ozone generator 10 Device 5 is flowed, ejector 5 sends out gas liquid mixture after accessing pending water 1 is mixed with ozone by check valve;
B:Ozone purification step is pressurized, by force, gas liquid mixture is mixed for the pressure and superatmospheric of setting adjustment sequence valve 16 Hybrid reaction in clutch 6, and rise from helical duct inside spin;
C:Photocatalyst purifying step:The liquid that sequence valve 16 flows out enters photocatalyst reaction tank 7, the purple of immersion in a liquid Light lamp 18 irradiates titanium dioxide layer 19, ultraviolet irradiation and Titanium Dioxide double purified liquid;
D:Flow out the liquid after step C and enter catalysis oxidation tank 8, it is net to carry out catalysis oxidation by honeycomb-shaped oxidizing aluminium lamination 17 Change, finally discharge water into water 9 after processing.
Avoided and air contact by the ultraviolet light 18 of immersion in a liquid, improve exposure rate, alumina layer 17 is honeycomb Shape structure, increases contact area, booster pump 15 make it that ozone is preferably soluble in water with sequence valve 16, improves dissolved efficiency, prevents Only ozone is excessive, and each certain tank design safety valve, air bleeding valve, clean-up port are obvious common knowledges.Flow valve is adjusted Amount of restriction.Helical structure is convenient to improve reaction speed with producing vortex,
Using technologies such as ultraviolet, ozone, senior mixing, advanced oxidations, in water treatment procedure using hydroxyl radical free radical as The oxidizing process of primary oxidizers, compared with traditional method for treating water, the application has the characteristics that:Product utilization ultraviolet Catalysis technique+efficient the hybrid technology of ozonation technology+ozone, is carried out to the organic matter in water body, microorganism, bacterium germ etc. Thoroughly oxidation Decomposition, in the process, without any chemicals, any harmful accessory substance does not occur.By producing Substantial amounts of hydroxyl radical free radical .HO, its oxidability is high, and it can induce chain reaction below, hydroxyl as the intermediate product of reaction Base free radical differs very little from the reaction rate constant of different organic matters, when there is multiple pollutant in water, will not go out A kind of existing material is degraded and situation that another material is basically unchanged ,-OH can not selectively directly with the pollution in water Thing reaction is degraded to carbon dioxide, water or harmless object, and the intermediate product in oxidizing process can continue same hydroxyl certainly Reacted by base, secondary pollution will not be produced and directly reach complete organics removal, thoroughly remove TOC and COD purpose, reaction Speed is fast, and speed reaches 109mol/ls, and processing requirement can be reached within a very short time;Both can individually it handle, again can be with it He matches at processing procedure, can greatly reduce processing cost, particularly can kill the indelible army of conventional antimicrobial technology Group bacterium, norovirus, Cryptosporidium, giardia lamblia stiles etc.;It can be applied in secondary water supply system, hot water supply system, swimming In the water circulatory system, surface water, landscape water and cooling tower, no medicament addition, no hazard residue, non-secondary pollution are eliminated Residual attachment in pipeline, reduces the probability that pipeline is corroded, and waterside number is changed in reduction.
General chemistry oxidizing process is poor due to oxidability, and reaction has the reasons such as selection, tends not to directly reach completely Organics removal, reduces TOC and COD purpose;Reaction speed is slow.
The utility model is reasonable in design, with low cost, durable, safe and reliable, simple to operate, time saving and energy saving, save Fund, compact conformation and easy to use.
The utility model, which is fully described, to be disclosed in order to more clear, and is not just being enumerated for prior art.
Finally it should be noted that:Above example is only to illustrate the technical solution of the utility model, rather than its limitations; Although the utility model is described in detail with reference to the foregoing embodiments, it will be understood by those within the art that: It can still be modified to the technical scheme described in previous embodiment, or which part technical characteristic is equal Replace;It is obvious that multiple technical schemes of the present utility model, which are combined, as those skilled in the art.And these Modification is replaced, and the essence of appropriate technical solution is departed from the spirit and model of the utility model embodiment technical scheme Enclose.

Claims (9)

1. a kind of water body purification apparatus, it is characterised in that:The water pump (2) that is connected including import with accessing pending water (1), catalysis oxidation Tank (8), photocatalyst reaction tank (7), blender (6) and ejector (5),
The outlet of water pump (2) is connected with ejector (5) inlet, and the air inlet of ejector (5) is connected with ozone generator (10), The gas liquid outlet of ejector (5) is connected with the lower end import of blender (6), the upper end outlet and photocatalyst reaction of blender (6) The lower end import connection of tank (7), the upper end outlet of photocatalyst reaction tank (7) is connected with the lower end import of catalysis oxidation tank (8), The upper end outlet of catalysis oxidation tank (8) is connected with water (9) after processing;
Be provided with the photocatalyst reaction tank (7) immersion in a liquid and waterproof sealing ultraviolet light(18), in photocatalyst reaction Titanium dioxide layer is provided with the inwall of tank (7)(19), ultraviolet light(18)It is radiated at titanium dioxide layer(19)On, in catalysis oxidation Alumina layer is provided with tank (8) inwall(17), alumina layer(17)For alveolate texture.
2. water body purification apparatus according to claim 1, it is characterised in that:Ejector (5) gas liquid outlet with mixing Booster pump (15) is provided between the lower end import of device (6);It is provided between blender (6) and photocatalyst reaction tank (7) suitable Sequence valve (16).
3. water body purification apparatus according to claim 2, it is characterised in that:Also include cold dry tank (13) and oxygenerator (14);Oxygenerator (14) is connected through cold dry tank (13) with ozone generator (10) import.
4. water body purification apparatus according to claim 3, it is characterised in that:Refrigeration machine (12), cold dry tank (13) and ozone Generator (10) passes sequentially through pipeline series connection.
5. water body purification apparatus according to claim 4, it is characterised in that:Between refrigeration machine (12) and cold dry tank (13) It is provided with second flow valve (11).
6. water body purification apparatus according to claim 5, it is characterised in that:Pacify between water pump (2) and ejector (5) Equipped with safety valve (3).
7. water body purification apparatus according to claim 6, it is characterised in that:It is provided with the gas liquid outlet of ejector (5) Check valve.
8. water body purification apparatus according to claim 7, it is characterised in that:Between safety valve (3) and ejector (5) It is connected with first flow valve (4).
9. water body purification apparatus according to claim 8, it is characterised in that:Spiral is vertically arranged with blender (6) The spiral mandrel of lift structure, is provided with and pitch identical spiral identical with spiral mandrel rotation direction on blender (6) inwall Piece.
CN201720145520.0U 2017-02-17 2017-02-17 Water body purification apparatus Active CN206494802U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720145520.0U CN206494802U (en) 2017-02-17 2017-02-17 Water body purification apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720145520.0U CN206494802U (en) 2017-02-17 2017-02-17 Water body purification apparatus

Publications (1)

Publication Number Publication Date
CN206494802U true CN206494802U (en) 2017-09-15

Family

ID=59805158

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720145520.0U Active CN206494802U (en) 2017-02-17 2017-02-17 Water body purification apparatus

Country Status (1)

Country Link
CN (1) CN206494802U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113087245A (en) * 2021-04-22 2021-07-09 广西科学院 Urban sewage treatment device
CN115259495A (en) * 2022-07-28 2022-11-01 中国航天汽车有限责任公司 Nutrient solution blending and purifying treatment device and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113087245A (en) * 2021-04-22 2021-07-09 广西科学院 Urban sewage treatment device
CN115259495A (en) * 2022-07-28 2022-11-01 中国航天汽车有限责任公司 Nutrient solution blending and purifying treatment device and method

Similar Documents

Publication Publication Date Title
CN104016511B (en) Ozone / photocatalysis oxidation-membrane separation integrated method and integrated set for advanced wastewater treatment
CN203890163U (en) Ozone/photocatalytic oxidation-membrane separation integrated device for advanced treatment of wastewater
CN204874211U (en) A synthesize processing apparatus for high salt industrial waste water that contains
CN104609500A (en) Ozone-photocatalysis reactor and water treatment method
CN204874213U (en) Petrochemical industry waste water is with synthesizing water treatment facilities
CN204897660U (en) A dark treatment facility of environment -friendly that is used for high salt industry sewage that contains
CN104150698A (en) Device and method for advanced treatment of rural domestic water through M type constructed wetland
CN212151749U (en) High-efficient ozone catalytic oxidation processing apparatus of high salt waste water
CN217780957U (en) Ultraviolet and ozone catalytic oxidation water treatment device based on quality-divided treatment
CN206494802U (en) Water body purification apparatus
CN110526527A (en) A kind of biomembrane biochemistry reaction system and process for purifying waste water based on ozone
CN208562075U (en) Ozone oxidation-BAC filtering-composite catalytic oxidation advanced treatment on coking wastewater system
CN205368041U (en) Ultraviolet -ozone catalytic oxidation wastewater treatment device
CN108585367A (en) A kind of UV ozone combined type aeration biological filter device and the method using device progress sewage disposal
CN113003850A (en) Advanced oxidation method and device
CN112520923A (en) Wastewater treatment method for urea-formaldehyde resin and phenolic resin production enterprises
CN210085058U (en) Novel three-phase ozone catalytic vulcanization tower
CN104193077A (en) Device for degrading organic wastewater by utilizing carrousel oxidation ditch and method for treating wastewater by using device
CN106145309A (en) A kind of economic benefits and social benefits catalytic ozonation wastewater treatment equipment and method
CN105217871A (en) The treatment process of the processing wastewater of synthesis dinitrodiazophenol and application thereof
CN109293176A (en) DMF low-pressure distillation recycling column overhead wastewater treatment method and system in film production
CN208916894U (en) The online back washing device of catalyst, catalytic ozonation pond and catalytic ozonation tower
CN109455796B (en) Industrial wastewater treatment process of zero-valent iron internal electrolysis coupling internal circulating fluidized bed Fenton
CN210595626U (en) Industrial waste water ultrasonic wave is catalytic oxidation device in coordination
CN206635100U (en) A kind of integral type gradient ozone catalytic fluidized bed plant

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant