CN203794624U - Ozonator in water - Google Patents

Ozonator in water Download PDF

Info

Publication number
CN203794624U
CN203794624U CN201420220281.7U CN201420220281U CN203794624U CN 203794624 U CN203794624 U CN 203794624U CN 201420220281 U CN201420220281 U CN 201420220281U CN 203794624 U CN203794624 U CN 203794624U
Authority
CN
China
Prior art keywords
nozzle
reactor body
ozone
water
electrode
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.)
Withdrawn - After Issue
Application number
CN201420220281.7U
Other languages
Chinese (zh)
Inventor
吴良春
廖振方
邓清玉
廖俊峰
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.)
Chongqing You Kai Science And Technology Ltd
Original Assignee
Chongqing You Kai Science And Technology 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 Chongqing You Kai Science And Technology Ltd filed Critical Chongqing You Kai Science And Technology Ltd
Priority to CN201420220281.7U priority Critical patent/CN203794624U/en
Application granted granted Critical
Publication of CN203794624U publication Critical patent/CN203794624U/en
Anticipated expiration legal-status Critical
Withdrawn - After Issue legal-status Critical Current

Links

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Abstract

The utility model discloses an ozonator in water. The ozonator comprises a reactor body which is detachably connected with plate-type electrodes and nozzle electrodes in pairs in a sealed mode, wherein the plate ends of the plate-type electrodes and the nozzle ends of the nozzle electrodes are located in the reactor body, the nozzle electrodes located in the reactor body are sleeved with insulation sleeves, the bottom of one end of the reactor body is provided with a water inlet, the other end of the reactor body is provided with an ozone water chamber communicated with the lower portion of the reactor body, the size of the ozone water chamber is smaller that of the reactor body, the bottom of the ozone water chamber is provided with a water outlet, the nozzle of each nozzle electrode is provided with a spacer sleeve, and the top end of each spacer sleeve is provided with a gas outlet. According to the ozonator, the spacer sleeves are additionally arranged on the nozzles of the nozzle electrodes, the gas production rate of ozone is increased by 30%, the ozone water chamber is additionally arranged so that ozone water can be accelerated before flowing out, ozone and water are mixed adequately, the ozone water flowing out is high in speed, and adequate mixing of the ozone water and sewage in a centrifugation fluidizing device is facilitated.

Description

Ozonizer in water body
Technical field
The utility model relates to a kind of ozonizer, particularly relates to ozonizer in a kind of water body.
Background technology
Along with the development of industrialization and urbanization, water environment pollution, water scarcity are day by day serious, water pollution control, and water environment protection is very urgent.
Obtain now the favor of brainstrust by the technology of ozonize sewage, ozone is made up of three Sauerstoffatoms, because it has higher redox potential, so have extremely strong oxidation capacity, can degradation water in plurality of impurities and kill various pathogens, mould, virus and kill such as Shi Bei section mollusk larva (reaching 98%) and aquatic organism as Cyclop, few mao annelid, water flea wheel animalcule etc.
Ozone water processes why obtain significant progress in the world, not just due to its effective impurity elimination and sterilizing ability, and be in water, not produce secondary pollution (residual hazard) after it is processed, unnecessary ozone also can comparatively fast be decomposed into oxygen and in water, not form the carcinogenic substances such as chlorine ammonia, chloroform like chlorine agent, thus by universally acknowledged be safest sterilizing agent.
At present, ozonizer is all producer waterborne, produces after ozone, and ozone, by supercharging, is then transported in water body by transport pipe, mixes with water.Energy consumption is high, noise is large, and running cost is high.Also may cause ozone to reveal the generation of event.
Contriver's earlier application patent, the patent No. is ZL200610054528, discloses a kind of plasma ozone generator, comprises reactor, powerstat, high-tension transformer, high voltage silicon rectifier stack air switch, reactor, current-limiting resistance, isolator, the live wire of this generator power line is connected with one end of a reactor, the other end of this reactor is connected with an output terminal of powerstat, the zero line of supply lead is connected Ei with another input terminus of powerstat, two output terminals of powerstat connect respectively at two input terminuss of high-tension transformer, the negative pole with output terminal and a high voltage silicon rectifier stack of high-tension transformer, one end of an air switch, one end of another reactor, ground connection after one end of each plate type electrode on reactor connects, after connecting with one end of an electrical condenser in one end of a current-limiting resistance, the other end of a current-limiting resistance is connected with another output terminal of high-tension transformer, and the other end of electrical condenser is connected with one end of Gree switch ...On reactor, be provided with water-in and water outlet, in the time that each plate type electrode and injector electrode carry out impulsive discharge in reactor, produce shockwave, intensive ultraviolet, high temperature, high pressure, cavitation stream and a large amount of free radical, because air or oxygen sprays into (in plasma channel) between plate type electrode and injector electrode, produce a large amount of ozone, under their moment combined action, complete and kill bacterium and to organic degraded, can reduce energy consumption and noise compared with existing ozone treating system simultaneously.Through contriver's long-term practice, although this device can be by increasing electricity level in reactor to increasing the gas production rate of ozone, large with regard to energy consumption like this, that is to say that this device also exists such defect that ozone generation rate is lower.
Utility model content
Because the above-mentioned defect of prior art, technical problem to be solved in the utility model is to provide ozonizer in the water body that a kind of gas production rate is larger.
For achieving the above object, the utility model provides ozonizer in a kind of water body, comprise reactor body, on reactor body, sealing is detachably connected with plate type electrode and injector electrode in pairs, each injector electrode comprises the conducting metal nozzle that conductive metal pipe and this conductive metal pipe one end are sealedly and fixedly connected, the plate end of described plate type electrode and the nozzle end of injector electrode are all positioned at reactor body, the plate end of each plate type electrode is corresponding with the nozzle of an injector electrode, be positioned at cover on the injector electrode of reactor body and have insulation covering, it is characterized in that: the bottom of one end of described reactor body is provided with water-in, the other end of described reactor body is provided with the ozone hydroecium communicating with reactor body bottom, the volume of described ozone hydroecium is less than the volume of reactor, the bottom of described ozone hydroecium is provided with water outlet, the nozzle of each described injector electrode is provided with spacer, the top of described spacer is provided with air outlet.
Adopt technique scheme, on the basis that is ZL200610054528 in the patent No., on injector electrode, increase a spacer, reduce the amount that enters the water in spacer, more be conducive to the ejection of gas, find through practice, after such improvement, under the electrode of identical logarithm, the gas production rate of ozone is than having improved 30% before.Set up at the other end of reactor body the ozone hydroecium that a volume is less than reactor body, make ozone water flow out preacceleration, on the one hand ozone is mixed more uniformly with water, on the other hand, the ozone water of this acceleration is mixed to get more abundant, more even with sewage after going out in centrifugal fluidic device.
As preferably: the external diameter of the conductive metal pipe of described injector electrode is 10-15mm, internal diameter is 1.5-2.5mm, the through hole that the taper hole that is 10 °-26 ° by a coaxial circular hole and cone angle in described nozzle forms, the taper hole end of described nozzle forms cone table outward, the area of the conductive metal sheet of each plate type electrode be the nozzle of the injector electrode corresponding with it cone table face area 80-120 doubly, the thickness of the conductive metal sheet of described plate type electrode is 5-8mm.
As preferably: the air outlet of described spacer is arranged on the middle part on spacer top.
The beneficial effects of the utility model are: the utility model increases spacer on the nozzle of injector electrode, the gas production rate of ozone has improved 30%, and set up ozone hydroecium, ozone water was raised speed before going out, ozone is fully mixed with water, ozone water speed after going out is fast, is conducive to ozone water and sewage fully mixing in centrifugal fluidic device.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model one embodiment;
Fig. 2 is electrical schematic diagram of the present utility model;
Fig. 3 is the structural representation of injector electrode.
In Fig. 1-3:
1-reactor body, 2-plate type electrode, 3-injector electrode, 3-1 conductive metal pipe, 3-2 conducting metal nozzle, 4-insulation covering, 5-water-in, 6-ozone hydroecium, 7-water outlet, 8-spacer, 9-reactor, 10-powerstat, 11-high-tension transformer, 12-current-limiting resistance, 13-electrical condenser, 14-isolator, 15-high voltage silicon rectifier stack, 16-air switch
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail:
As Figure 1-3, in water body of the present utility model, ozonizer seals and is detachably connected with in pairs plate type electrode 2 and injector electrode 3 on reactor body 1, according to user's needs, or can the interior pairing of reactor body more than 1 to or tens pairs or hundreds of to injector electrode 3 and plate type electrode 2, to meet the ozone amount of user's needs, from several tons of processing per hour to a few kiloton water.Each injector electrode 3 comprises the conducting metal nozzle 3-2 that conductive metal pipe 3-1 and this conductive metal pipe 3-1 one end are sealedly and fixedly connected, the plate end of described plate type electrode 2 and the nozzle end of injector electrode 3 are all positioned at reactor body 1, the plate end of each plate type electrode 2 is corresponding with the nozzle 3-2 of an injector electrode 3, be positioned at cover on the injector electrode 3 of reactor body 1 and have insulation covering 4, the external diameter of the conductive metal pipe 3-1 of described injector electrode 3 is 10-15mm, internal diameter is 1.5-2.5mm, the through hole that the taper hole that is 10 °-26 ° by a coaxial circular hole and cone angle in described nozzle 3-2 forms, the taper hole end of described nozzle 3-2 forms cone table outward, the area of the conductive metal sheet of each plate type electrode 2 be the nozzle 3-2 of the injector electrode 3 corresponding with it cone table face area 80-120 doubly, the thickness of the conductive metal sheet of described plate type electrode 2 is 5-8mm.The bottom of one end of described reactor body 1 is provided with water-in 5, and above plate type electrode 2 is identical with ZL200610054528 with the structure of injector electrode 3 grades, and circuit theory of the present utility model is also identical with ZL200610054528, does not repeat at this.
Improvements of the present invention are: the other end of described reactor body 1 is provided with the ozone hydroecium 6 communicating with reactor body 1 bottom, the volume of described ozone hydroecium 6 is less than the volume of reactor body 1, the bottom of described ozone hydroecium 6 is provided with water outlet 7, the nozzle of each described injector electrode 3 is provided with spacer 8, and the middle part on the top of described spacer 8 is provided with air outlet.
When use, clean water through ozonize enters in reactor body 1 from water-in, air or oxygen enters in nozzle 3-2 from the conductive metal pipe 3-1 of injector electrode 3, shape nozzle 3-2 ejection, then spray (spacer 8 can stop entering of liquid) from the air outlet of spacer 8, reach between two electrodes, when electric discharge, between injector electrode 3 and plate electrode 2, form plasma channel, produce high temperature (20000-30000K), high pressure (500-1000MPa), intensive ultraviolet, ozone, cavitation stream, shockwave and a large amount of free radicals; Under ultraviolet katalysis, the oxidation capacity of ozone and free radical improves greatly, thereby greatly improves the effect of processing waste water.The ozone and the free radical that produce are directly dissolved in water, then ozone water enters ozone hydroecium 6, in the time entering ozone hydroecium 6, because volume diminishes and is accelerated suddenly, the ozone water of accelerating is gone out from water outlet 7 again, enter centrifugal fluidic device and fully mix with sewage, mixed sewage enters reaction chamber reaction, thereby kills the germ in sewage and organism is degraded.
More than describe preferred embodiment of the present utility model in detail.Should be appreciated that those of ordinary skill in the art just can make many modifications and variations according to design of the present utility model without creative work.Therefore, all technician in the art comply with design of the present utility model on the basis of existing technology by the available technical scheme of logical analysis, reasoning, or a limited experiment, all should be in by the determined protection domain of claims.

Claims (3)

1. ozonizer in a water body, comprise reactor body (1), detachably be connected with in pairs plate type electrode (2) and injector electrode (3) in the upper sealing of reactor body (1), each injector electrode (3) comprises the conducting metal nozzle (3-2) that conductive metal pipe (3-1) and this conductive metal pipe (3-1) one end are sealedly and fixedly connected, the nozzle end of the plate end of described plate type electrode (2) and injector electrode (3) is all positioned at reactor body (1), the plate end of each plate type electrode (2) is corresponding with the nozzle (3-2) of an injector electrode (3), the upper cover of injector electrode (3) that is positioned at reactor body (1) has insulation covering (4), it is characterized in that: the bottom of one end of described reactor body (1) is provided with water-in (5), the other end of described reactor body (1) is provided with the ozone hydroecium (6) communicating with reactor body (1) bottom, the volume of described ozone hydroecium (6) is less than the volume of reactor body (1), the bottom of described ozone hydroecium (6) is provided with water outlet (7), the nozzle of each described injector electrode (3) is provided with spacer (8), the top of described spacer (8) is provided with air outlet.
2. ozonizer in water body as claimed in claim 1, it is characterized in that: the external diameter of the conductive metal pipe (3-1) of described injector electrode (3) is 10-15mm, internal diameter is 1.5-2.5mm, the through hole that the taper hole that is 10 °-26 ° by a coaxial circular hole and cone angle in described nozzle (3-2) forms, the taper hole end of described nozzle (3-2) forms cone table outward, the area of the conductive metal sheet of each plate type electrode (2) be the nozzle (3-2) of the injector electrode (3) corresponding with it cone table face area 80-120 doubly, the thickness of the conductive metal sheet of described plate type electrode (2) is 5-8mm.
3. ozonizer in water body according to claim 1, is characterized in that: the air outlet of described spacer (8) is arranged on the middle part on spacer (8) top.
CN201420220281.7U 2014-04-30 2014-04-30 Ozonator in water Withdrawn - After Issue CN203794624U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420220281.7U CN203794624U (en) 2014-04-30 2014-04-30 Ozonator in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420220281.7U CN203794624U (en) 2014-04-30 2014-04-30 Ozonator in water

Publications (1)

Publication Number Publication Date
CN203794624U true CN203794624U (en) 2014-08-27

Family

ID=51376857

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420220281.7U Withdrawn - After Issue CN203794624U (en) 2014-04-30 2014-04-30 Ozonator in water

Country Status (1)

Country Link
CN (1) CN203794624U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103991848A (en) * 2014-04-30 2014-08-20 重庆优楷科技有限公司 Ozone generator in water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103991848A (en) * 2014-04-30 2014-08-20 重庆优楷科技有限公司 Ozone generator in water
CN103991848B (en) * 2014-04-30 2015-10-21 重庆优楷科技有限公司 Ozonizer in a kind of water body

Similar Documents

Publication Publication Date Title
CN103482735B (en) Water spray discharge air plasma jet processing unit and high voltage source thereof
CN104211137B (en) Plasma water treatment device
CN105905976B (en) A kind of microbubble biphase gas and liquid flow Non-thermal Plasma Technology in Water Treatment and method
CN103466747A (en) Device for removing toxicity in traditional Chinese medicine wastewater by plasma discharge
CN104370350A (en) Electrochemistry apparatus for water treatment and method
CN205999054U (en) Plasma produces the device of sterilization activated water
CN201785237U (en) DBD (dielectric barrier discharge) plasma hydroxyl radical generating device for waste water treatment
CN103693714A (en) High-pressure atomizing dielectric barrier discharge plasma water treatment device
CN203419777U (en) Electrochemical device for water treatment
CN103537245B (en) A kind of Venturi ionization device for the preparation of hydroxyl radical free radical
CN202107566U (en) Equipment for water treatment of high-voltage discharge plasma
CN104229945B (en) Partial reflux pressurized aeration formula plasma sewage treating apparatus
CN102491446A (en) Processing technology and device of optical fiber plasma liquid
CN203794624U (en) Ozonator in water
CN101148285A (en) Method for processing waste water by high-voltage impulse gas-phase humidification discharge
CN103991848B (en) Ozonizer in a kind of water body
CN104860381A (en) Method and apparatus for treating atrazine waste water by using combination of multi-needle corona discharge and titanium dioxide catalyst
CN201572352U (en) Cold plasma generator
CN110642340B (en) Circulating flow type electric-assisted ozone water treatment equipment and method for treating water by using same
CN207551913U (en) A kind of aqueous hydrogen peroxide solution process units
CN107010603A (en) A kind of ozone generating-device and method for water process
CN108128879A (en) A kind of oxidizing gas synergistic device
CN1944240B (en) Plasma ozone generator
CN203999032U (en) A kind of compact cascade type low-temperature atmosphere-pressure discharge plasma is processed the system containing algae sewage
CN203878006U (en) Electroprocessing sewage purifying and recycling system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20140827

Effective date of abandoning: 20151021

C25 Abandonment of patent right or utility model to avoid double patenting