CN207986682U - A kind of active oxygen generator device - Google Patents

A kind of active oxygen generator device Download PDF

Info

Publication number
CN207986682U
CN207986682U CN201721725869.8U CN201721725869U CN207986682U CN 207986682 U CN207986682 U CN 207986682U CN 201721725869 U CN201721725869 U CN 201721725869U CN 207986682 U CN207986682 U CN 207986682U
Authority
CN
China
Prior art keywords
ozone
water
shell
catalyst
filter
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
CN201721725869.8U
Other languages
Chinese (zh)
Inventor
陈木发
薛立人
叶荣川
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.)
Hydrocarbon Technology Engineering Management (wuhan) Co Ltd
Original Assignee
Hydrocarbon Technology Engineering Management (wuhan) Co 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 Hydrocarbon Technology Engineering Management (wuhan) Co Ltd filed Critical Hydrocarbon Technology Engineering Management (wuhan) Co Ltd
Priority to CN201721725869.8U priority Critical patent/CN207986682U/en
Application granted granted Critical
Publication of CN207986682U publication Critical patent/CN207986682U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The utility model is related to a kind of active oxygen generator devices, including ozonized gas generator, catalyst tower, filter, the ozonized gas generator is by shell, into water distribution pipe, ozone electrode plate groups at, ozone electrode plate is mounted on by K-A-K-A interaction arrangement mode in shell, and direct current supply is carried out to ozone electrode plate, it is equipped on shell into water distribution pipe, shell is equipped with sewage draining exit and exhaust outlet, the lower part of catalyst tower connects with the exhaust outlet of ozonized gas generator, catalyst tower top is connected with filter, the top of filter is equipped with exhaust outlet and drainpipe.The utility model is powered using low voltage and high current to impregnating medium between anodic-cathodic plate in water, by the function of current, directly generates ozone and hydrogen and oxygen in water.By to positive and negative electrode coating film treatment increasing, its potential difference, anode generates ozone, amount of oxygen increases, and cathode generates hydrogen and increases, then handles three kinds of gases by catalyst and be converted to hydrogen peroxide and hydroxyl (H2O2With OH).

Description

A kind of active oxygen generator device
Technical field
The utility model is related to a kind of active oxygen generator devices, disclose the original that active oxygen is prepared using water as raw material Reason and device.Active oxygen includes ozone, oxygen, hydrogen peroxide and hydroxyl radical free radical (O3,O, H2O2,·OH)。
Background technology
Ozone is a kind of multi-functional nature or artificial gas, it can deodorization, reduce ultraviolet light to animals and plants on the earth Injury, help the regeneration of bone, help the treatment of cancer, eliminating bacteria, PM2.5, pesticide, fertilizer, mould and the micro- life of spore Object.Ozone only destroys cancer cell and damaged cell in human body, can not injure the cell of health.In 99% or more ozone treatment In, do not leave oxidized byproduct or side effect, ozone eventually become animals and plants all need oxygen.Therefore, under concentration control The ozone of generation is sharp weapon that are most environmentally friendly, can most improving Living Hygiene environment.
Since the mankind in 1840 have found ozone, electrolysis air generates the technology of ozone (or glow discharge), is sent out Exhibition for most generally with most durable commodity.But, using water as the electrolysis water technology in ozone source, have miniaturization, carryingization, Simplify, the advantage without exhaust gas.One of inventor of the utility model is engaged in the ozoniferous research and development of electrolysis water production more than 20 Year.Patent application is proposed during research and development successively, such as:United States Patent (USP) 9174895,12/602111, US20070272550, US2008/0181832A1 and US2010/0135869A1;Chinese patent CN101608317A, CN202912689U, CN105002517A and CN201510376097.0 etc..These inventions are all without solving the following basic of " electrolysis water generation ozone " Problem:
1. the purity and cost of anode material;
2. the protection and maintenance of cathode;
3. the potential burning of hydrogen and explosion crisis.
Invention content
The purpose of this utility model provides a kind of active oxygen generator device, which uses low-voltage (8-12V), high Electric current (maximum 100A) is powered the medium between anodic-cathodic plate of immersion in water, by the effect of electric current, makes electrode plate by direct current Potential electrolysis water directly generates ozone and hydrogen and oxygen in water.After by the coating film treatment to positive and negative electrode, make it Potential difference increases, and ozone, the amount of oxygen of anode generation are also synchronous to be increased, and the hydrogen that cathode generates is consequently increased, then by touching These three gases are converted to hydrogen peroxide and hydroxyl (H by the processing of matchmaker2O2With OH).Also solve the problems, such as following three simultaneously:
1. the purity and cost of anode material;
2. the protection and maintenance of cathode;
3. the potential burning of hydrogen and explosion crisis.
The technical solution of the utility model is:
Active oxygen generator device, including ozonized gas generator, catalyst tower, filter, the ozone gas occur Device by shell, into water distribution pipe, ozone electrode plate groups at ozone electrode plate is by K-A-K-A interaction arrangement Mode is mounted in shell, and carries out direct current supply to ozone electrode plate, is equipped with into water distribution pipe on shell, shell is equipped with Sewage draining exit and exhaust outlet, it is characterised in that:The lower part of catalyst tower connects with the exhaust outlet of ozonized gas generator, catalyst tower it is upper Portion is connected with filter, and the top of filter is equipped with exhaust outlet and drainpipe.
The ozone electrode plate has conductive Tu layer not using the stannic oxide of antimony dopant and two element of nickel as anode with surface Rust steel is cathode.
The hydrogen that the oxygen that the anode of ozone electrode plate generates is generated with cathode, the catalyst that can be filled in catalyst tower are online Merge into hydrogen peroxide;Combined hydrogen peroxide can be converted into hydroxyl radical free radical online by the catalyst filled in catalyst tower.
The cathode conduction Tu layer includes:Chromium, activated carbon, graphite, carbon nanotubes, graphene or carbon materials-metal oxidation Object composite wood.Wherein carbon materials-metal oxide composite wood is preferred.
The derived compound of the doped chemical nickel is:Nickel chloride, nickel sulfate, nickel nitrate, nickel phosphate, cross chloric acid nickel, Nickelous carbonate, bicarbonate nickel, nickel oxalate or nickel hydroxide.Wherein, nickelous carbonate is preferred.
The source metal for the catalyst filled in the catalyst tower is:Scandium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, yttrium, Zirconium, niobium, molybdenum, technetium, ruthenium, silver, cadmium, tungsten or cerium.Wherein, manganese, zirconium, tungsten are preferred.
The carrier that catalyst is filled in the catalyst tower is steel wire lump, structured packing or filter plate of porous ceramic block.Wherein, steel Pompon is preferred.
The device method of operation of the utility model is:
Clear water first passes through water inlet line and enters in the ozonized gas generator of lower part, when clear water reaches setting height, ozone Electrode plate (negative and positive the two poles of the earth), which is powered, to be started to react with water, and anode generates ozone and oxygen (O3、O2) gas, cathode generation hydrogen Gas (H2).The ozone of generation, oxygen, hydrogen under the action of flow by online catalyst when, hydrogen is converted to hydrogen peroxide (H2O2), it is eventually converted into free radical (OH), forms ozone, oxygen, hydrogen peroxide and hydroxyl radical free radical (O in water3,O,H2O2,· OH the active oxygen) coexisted.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Specific implementation mode
The utility model is further described in conjunction with attached drawing.
As shown in Figure 1, the utility model includes ozonized gas generator, catalyst tower 5, filter 6, the ozone gas Generator by shell 1, into water distribution pipe 2, ozone electrode plate groups at, ozone electrode plate by cathode 3- anode 4- cathodes 3- sun 4 interaction arrangement mode of pole is mounted in shell 1, and carries out direct current supply to ozone electrode plate, is equipped on shell 1 into water and is distributed Pipe 2, shell 1 are equipped with sewage draining exit and exhaust outlet, it is characterised in that:The lower part of catalyst tower 5 and the exhaust of ozonized gas generator Mouth connects, and the top of catalyst tower 5 is connected with filter 6, and the top of filter 6 is equipped with exhaust outlet and drainpipe.
The ozone electrode plate has conductive Tu layer not using the stannic oxide of antimony dopant and two element of nickel as anode with surface Rust steel is cathode.
The hydrogen that the oxygen that the anode of ozone electrode plate generates is generated with cathode, the catalyst that can be filled in catalyst tower are online Merge into hydrogen peroxide;Combined hydrogen peroxide can be converted into hydroxyl radical free radical online by the catalyst filled in catalyst tower.
Operation principle and feature:
The basic chemistry of water electrolysis is that equation (1) is shown:
H2O(l)→2H2(g)+O2(g) Eo=1.23V (1)
Applying under 1.23V normal voltages, water generates hydrogen on cathode by electrolysis, meanwhile, water is also electric on anode Solution generates oxygen.Equally it is anodic product, the yield of ozone is then very little.On the base material (titanium) of anode, it is necessary to plate One layer can promote the catalyst that voltage (be known as oxygen and overpotential occurs) occurs for oxygen, and the yield of ozone can just have practical water It is flat.
For example, stannic oxide is plated in the anode formed in titanium sheet, it can make oxygen that overpotential occur and be promoted to 1.52V.Cause This, before anode generates oxygen, ozone can be generated largely.However, stannic oxide is semi-conducting material, it must be adulterated specifically Element keeps stannic oxide conductive, and promotes stannic oxide and produce ozoniferous efficiency.The sun of stannic oxide and doped chemical composition Pole is that " efficiency is most in all " electrolysis water generation ozone " anode catalysts (characteristic that must have catalysis reaction and electrochemistry) system Height, cost is minimum, most environmentally friendly one group.
With stannic oxide (SnO2) based on ozone anode, need antimony dopant and nickel, improve stannic oxide respectively and lead Electric degree and ozone generation rate.The available precursor (or starting material) of tin-three element of antimony-nickel and preferably, as table one show:
One electrolysis water of table generates ozone (O3) in SnO2The component of anode
The stannic oxide of antimony dopant is known as ATO, stannic oxide can also doped indium (In) or fluorine (F) be used as conductive element, point Also known as it is ITO or FTO.When ATO is as anode electrolysis water, hydroxyl radical free radical (OH) will produce;SnO2The identification of anode quality, It cannot be only according to the O in water3The height of concentration, should also measure the oxidation-reduction potential of water, and unit is mV.The oxidation-reduction potential of water Value is the index of aqueous solution " redox " ability, than O in water3Concentration more can be shown that the ability of " sterilizing decontamination ".
One of inventor of this case is once with stannous oxalate (SnC2O4) butter of tin is substituted, solve stannic oxide anode system When making, butter of tin leads to the problem of hydrochloric acid " injury equipment and operator " (Chinese patent application publication No. CN105002517A).Synthesis of oxalic acid stannous must be using oxalic acid as one of raw material (another raw material is stannous chloride), and pharmaceutical grade oxalic acid The market price be 33 times of technical grade oxalic acid.Therefore technical grade oxalic acid must be purified with " recrystallization ", technique includes 80 DEG C water-soluble Solve oxalic acid, and 80 DEG C of hot solutions of filtering.But, if technical grade oxalic acid contains the hot water soluble impurity of energy, filtering and crystallization Effect is bad.Equally it is technical grade, citric acid is not only cheaper than oxalic acid, and the purity of technical grade citric acid and pharmaceutical grade lemon Sour same level.Therefore, the utility model is using stannous citrate as SnO2Derived compound, the utility model also use lemon Lemon acid be complexing agent, collocation ethylene glycol fuel generate colloidal sol-gel, lock (tin-antimony-nickel) three metal ions, reduce they Volatility under high temperature, it is ensured that the metal ratio that the catalyst film of synthesis has formula designed.It is aforementioned to utilize citric acid and second The low-temperature combustion synthesis of glycol is that MP Pechini are initiated for 1967 in the Christian era, and obtain U.S. Patent No. 3330697. The metal oxide catalyst that the method is formed has many advantages, such as " low power consuming, nano crystals, composition is uniform, structure is closely knit ".
The Section 2 of " electrolysis water leads to the problem of ozone " technology is to be solved, is the incrustation of cathode, need frequent scale removal guarantor It supports (maintenance period is depending on the water quality of water inlet).The design of current " electrolysis water generation ozone " reactive tank, including stainless steel (SS) source as the waste water of the base material of cathode and tap water or low stain as ozone.As electrolysis carries out a period of time, Calcium and magnesium ion in water can with carbonate and water pollutant by the product of cathodic reduction, will all be deposited on the surfaces SS and by its It is completely covered, becomes the incrustation for making SS insulate.Once SS cathodes are non-conductive, electrolytic cell just stops generating ozone, and anode Chang Lian Band is impaired.At this point, electrolytic cell just must stop work, regenerated.To exempt the maintenance of cathode and the long-play of electrolytic cell, this Utility model proposes following two kinds of solutions:
1) the chromium film of the surfaces SS coat foods grade
The technique that " high temperature oxidation and corrosion " is resisted with the coating chromium film of motor vehicle exhaust emission metal tube, by conductive food-grade The plating of (trivalent chromium) golden yellow chromium film on stainless steel, will be as exempting from the cathode of maintenance.Chromium film is smooth compared with stainless steel densification, makes in water Suspended matter be not easy to adhere to, meanwhile, the resistance to corrosion of chromium is strong, and have catalytic action.
2) carbon-coating of the surfaces SS applying conductive
With the material that carbon black is mixed with sticker, it is coated with manufactured cathode on metal base, in DC electric field, energy By the O in water2It is reduced to H2O2, and then and O3Reaction generates hydroxyl radical free radical (OH), is peroxone reactions, such as China Disclosed in patent CN105439258A.But, the needed O of the patent2With O3All from external input, and carbon black can be catalyzed carbonic acid Calcium/magnesium carbonate crystallizes on cathode, and painting carbon cathode is made more rapidly to be completely covered than what is do not applied instead.The utility model is with ceramics Adhesive, under 700-800 DEG C and anaerobic state, such as by carbon materials:Activated carbon, graphite, carbon nanotubes, graphene or " carbon materials- Metal oxide " composite wood fixes the cathode for becoming exempt from maintenance on stainless steel.It is that elasticity is very high to apply carbon cathode technique Technology, must asking for market can be more coordinated than chrome-plated process, such as:Change the color of cathode, promote the function of cathode (as generation is double Oxygen water decomposes obstinate pollutant) and promotion electrolytic efficiency.It is preferred to apply carbon material, it is that " carbon materials-metal oxide " are compound Material.
The electrolytic water device that the utility model is carried can generate two kinds of oxidants when energization operates:O3With O2, and one kind is also Former agent:H2.The utility model is not by gaseous product (the i.e. H of three kinds of high activities2-O2-O3) separation, and allow they in a cell The reaction of many " generating free radical " occurs for mixing.Wherein, O3It will be decomposed by the OH-ion in water, generate equation (2) extremely (8) chain reaction:
O3+OH-→O2+HO2 - (2)
O3+HO2 -→HO2·+O3·- (3)
HO2·→H++O2·- (4)
O2·-+O3→O2+O3·- (5)
O3·-+H+→HO3· (6)
HO3·→HO·+O2 (7)
HO·+O3→HO2·+O2 (8)
In addition, the product O of anode3With the product H of cathode2, the chain reaction of equation (9) can also occur:
H2+2O3→H2O2+2O2 (9)
The product of equation (2) to (9), belongs to oxygen containing oxidant, abbreviation active oxygen.Active oxygen has strong " sterilization " ability and high redox potential ORP value.Equation (2) to (9) is also shown:What anode generated is dissolved in water O3, can be consumed by oxidizable species in water.Therefore, the quality of " electrolysis water generation ozone " technology electrode production, except measurement water In O3Concentration should also measure the ORP value of Ozone Water.
The Section 3 of " electrolysis water leads to the problem of ozone " technology is to be solved to be:The potential burning of hydrogen and explosion crisis.This The H of the electrolysis unit of utility model2Yield, in H2-O2-O380% or more, O is accounted in gaseous product2With O3About respectively account for 13% with 5%, remaining gas is water vapour and air.By H caused by electrolytic cell2It is completely converted into active oxygen, H can be eliminated2Safety It threatens.
In order to promote H2Conversion ratio, the utility model develops online catalyst tower.Utilize the filtering with three-dimensional structure Carrier, such as:Steel wire lump (SB), structured packing or filter plate of porous ceramic block.It is preferred that steel wire lump will via Pechini methods " carbon materials " and " metal oxide " powder, is gradually added on steel wire lump, finally makes catalyst or the coating steel wire of functional group's covering Ball (CSB).Method and step:First with iron chloride (FeCl3) or hcl corrosion cleaning steel wire lump (SB), it is therefore intended that on removal steel wire Oil stain and be roughened the surface of steel wire, increase adhesive force of the covering on steel wire.It cleans and dries the steel wire lump after corrosion (SB), it is dipped into a few hours in a kind of solution of protective layer, so that medicament is fully reacted with steel wire lump, then with 700-800 DEG C sintering, steel wire ball surface formed protective film.
It can be used for the material of protective layer, including:Silica, aluminium oxide, aluminum phosphate, molecular sieve, zeolite (contain composite wood Material).Preferred protective film is zeolite.Protective film has the function of three:It prevents steel wire lump from corroding, carries catalyst or adsorption particle, And zeolite itself is also a kind of catalyst.
The steel wire lump (SB) for having plated protective film, then with ceramic binder, under 700-800 DEG C and anaerobic state, by carbon Material is such as:Activated carbon, graphite, carbon nanotubes or graphene are fixed on the protective layer of steel wire lump (SB), become cladding carbon film It is coated with steel wire lump (CSB).It is small that coating steel wire lump (CSB) is dipped into the number in metal oxide or the solution of specific functional group When, liquid medicine fully soaks the surface of carbon materials and different size of hole, and is reacted with the surface functionalities of carbon materials, generates bond. With iron, cobalt, nickel is preferred metallic element with copper, and iron oxide (Fe is made2O3), cobalt oxide (CoO/Co3O4), nickel oxide (NiO) with four kinds of catalyst of copper oxide (CuO).Iron, cobalt, nickel and steel wire lump catalyst made of four kinds of metals of copper are taken, it can be by electrolytic cell The H of interior generation2It is converted to H2O2, it is eventually transformed into OH.

Claims (2)

1. active oxygen generator device, including ozonized gas generator, catalyst tower, filter, the ozonized gas generator By shell, into water distribution pipe, ozone electrode plate groups at ozone electrode plate is by K-A-K-A interaction arrangement side Formula is mounted in shell, and carries out direct current supply to ozone electrode plate, is equipped on shell into water distribution pipe, shell is equipped with row Dirty mouth and exhaust outlet, it is characterised in that:The lower part of catalyst tower connects with the exhaust outlet of ozonized gas generator, the top of catalyst tower It is connected with filter, the top of filter is equipped with exhaust outlet and drainpipe.
2. active oxygen generator device according to claim 1, it is characterised in that:The load of catalyst is filled in the catalyst tower Body is steel wire lump, structured packing or filter plate of porous ceramic block.
CN201721725869.8U 2017-12-08 2017-12-08 A kind of active oxygen generator device Active CN207986682U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721725869.8U CN207986682U (en) 2017-12-08 2017-12-08 A kind of active oxygen generator device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721725869.8U CN207986682U (en) 2017-12-08 2017-12-08 A kind of active oxygen generator device

Publications (1)

Publication Number Publication Date
CN207986682U true CN207986682U (en) 2018-10-19

Family

ID=63816509

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721725869.8U Active CN207986682U (en) 2017-12-08 2017-12-08 A kind of active oxygen generator device

Country Status (1)

Country Link
CN (1) CN207986682U (en)

Similar Documents

Publication Publication Date Title
Yao et al. Highly selective electrochemical nitrate reduction using copper phosphide self-supported copper foam electrode: Performance, mechanism, and application
Xu et al. Electrocatalytic reduction of nitrate–a step towards a sustainable nitrogen cycle
Zhang et al. Electrochemical degradation of refractory pollutants using TiO2 single crystals exposed by high-energy {001} facets
CN107915210A (en) A kind of active oxygen generator device
JP5604204B2 (en) Ammonia synthesis method
Chen et al. Construction of rGO@ Ti/SnO2–Sb composite electrode for electrochemical degradation of fluoroquinolone antibiotic
CN106277180A (en) A kind of intensified by ultrasonic wave photoelectrocatalysis processes containing heavy metal and the device of persistent organic pollutant wastewater
JP2000254650A (en) Water treatment and water treatment device
JP2000226682A (en) Method and device for electrochemical processing
CN101531411A (en) Method for electrochemically disinfecting gas diffusion electrode system
CN105293688B (en) The system that nitrate nitrogen in water removal is removed in a kind of coupled biological anode electro-catalysis
WO2019149142A1 (en) Novel anode material and preparation method therefor, and device for generating ozone by electrolysis
WO2019149141A1 (en) Method for preparing sn-containing suspension and application thereof
CN104609532B (en) Method for removing PPCPs in treatment process of drinking water
CN112264004B (en) Catalytic material based on tungstate and application thereof in hydrogen peroxide production through water oxidation
Zha et al. Treatment of hazardous organic amine wastewater and simultaneous electricity generation using photocatalytic fuel cell based on TiO2/WO3 photoanode and Cu nanowires cathode
CN109576732A (en) Manufacture active oxygen O3Generator
Liu et al. Synergistic effect of single-atom Cu and hierarchical polyhedron-like Ta3N5/CdIn2S4 S-scheme heterojunction for boosting photocatalytic NH3 synthesis
Köktaş et al. Tetracycline removal from aqueous solution by electrooxidation using ruthenium-coated graphite anode
CN103641207B (en) A kind of Zinc-containing electroplating waste water combined electrolysis groove treatment process
JP2011131118A (en) Method and apparatus for preparing spray water for plant
Wang et al. A novel strategy to achieve simultaneous efficient formate production and p-nitrophenol removal in a co-electrolysis system of CO2 and p-nitrophenol
Ganthavee et al. Removal of pharmaceutically active compounds from wastewater using adsorption coupled with electrochemical oxidation technology: A critical review
Xu et al. Transition Metal‐Based Catalysts for Urea Oxidation Reaction (UOR): Catalyst Design Strategies, Applications, and Future Perspectives
CN207986682U (en) A kind of active oxygen generator device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant