CN201746592U - Water electrolysis device - Google Patents
Water electrolysis device Download PDFInfo
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- CN201746592U CN201746592U CN2010202356357U CN201020235635U CN201746592U CN 201746592 U CN201746592 U CN 201746592U CN 2010202356357 U CN2010202356357 U CN 2010202356357U CN 201020235635 U CN201020235635 U CN 201020235635U CN 201746592 U CN201746592 U CN 201746592U
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- water
- ozone
- hydrogen
- titanium
- orifice plate
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/13—Ozone
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
- C25B9/73—Assemblies comprising two or more cells of the filter-press type
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Abstract
The utility model discloses a water electrolysis device, which comprises an electrolysis unit, a water tank, a gas liquid mixer, a gas liquid separator, and a power supply. The electrolysis unit comprises a casing. The top of the casing is provided with a water inlet. A positive pole titanium power supply orifice plate, a beta-PbO2 positive pole catalysis plate, a solid polyelectrolyte membrane, a Pt/C negative pole catalysis plate, and a negative pole titanium power supply orifice plate are arranged below the water inlet. The bottom of the water tank is provided with an engaged interface. The top is movably provided with a top cover. An ozone discharge pipe and a water compensation inlet are arranged on the top cover. An ozone discharge outlet is arranged on the water tank. The gas liquid mixer comprises a mixer container. An ozone inlet, a water inlet, and an ozone water outlet are arranged on the mixer container. The gas liquid separator comprises a separator container. A hydrogen water inlet, a hydrogen discharge pipe, and a water discharge outlet are arranged on the separator container. The positive pole of the power supply is connected with the positive pole of the electrolysis unit. The negative pole of the power supply is connected with the negative pole of the electrolysis unit. The water electrolysis device can electrolyze the water into ozone, ozone water, hydrogen gas, and hydrogen containing water, has simple structure, less energy consumption and low cost, and can be widely used.
Description
Technical field
The utility model relates to a kind of apparatus for electrolyzing.
Background technology
Ozone is a kind of strong oxidizer, has very strong instantaneous sterilization, sterilization, sterilization, deodorizing, decolouring, function such as fresh-keeping, can also decompose the organism that is difficult to decompose.At transmissible disease, virus popular public health and medical field without restraint, the disaggregating treatment field of the clean field of industrial circles such as the environmental area of control atmosphere pollution, water pollution, food and pharmacy, electronic industry, the highly difficult chemical substances such as sterilization, trade effluent and nuke rubbish of tap water tap water, its application is extremely important.
The application of ozone has two aspects: the one, and the application of ozone body, it is mainly used in the sterilization of air and purification, the decomposition of medium-gas, decomposition discharging of industrial tail gas etc.Ultrapure clean ozone body is used widely at aspects such as medicine industry, foodstuffs industry and medical treatment; The 2nd, the application of ozone water, present technology is ozone to be sneaked in the water obtain mostly, blending means is a lot, the consistency of ozone water difference that different modes obtains, but to reach application purpose, the slave unit cost of investment still is that energy consumption is all than higher.
At present, have the ozone system access method of the value utilized that following several mode is arranged:
1. be the ultraviolet low-pressure mercury fluorescent tube method of raw material with the natural air: the ozone concn that this method is produced out is very low, is used for sterilizing air more, and it is not high to produce the utility value of ozone water.
2. be the high frequency discharge method of raw material with the purity oxygen: the ozone concn that this method is produced out is higher than ultraviolet low-pressure mercury fluorescent tube method, no matter is the utilization of ozone or the utilization of ozone water, all is the method for relatively popularizing at present.Yet because this method produces oxynitride simultaneously, and oxynitride is a carcinogenic substance, therefore causes this method to be subjected to great restriction in the application in pure field and tap water field.
3. be the electrolytic process of raw material with the pure water: this method is raw material with water, with β-PbO
2For anode catalyst be under the electrolytic catalysis effect of cathod catalyst hydrogen to be separated with oxygen with platinum (Pt/c), anode generates O
2And O
3, negative electrode generates H.The ozone concn that this method is produced out is very high very pure, however since energy consumption big, cost an arm and a leg, and product is difficult to control, and causes being difficult to being popularized adopting.
It is documented that the research of water electrolysis formula ozonizer is since 1886,, come out in SPE formula electrolysis ozone generator in 1985 through the long term studies progress.The ozonizer basic structure of this form is with β-PbO
2Be anode catalyst layer, with platinum (Pt/c) is the cathode catalysis layer of catalyzer, clip solid polyelectrolyte membrane (SPE) in the middle of it, press from both sides porous matter titanium plate or the spumescence titanium material that has the electrical conductor effect and play the air-and water-permeable effect in the outside of anode and negative electrode, on its outside folder separately, accept the anode and cathode titanium plate that positive-negative power is given electricity again.During work, be provided with pure water to anode, pass to the direct current of 2～3.5V, water is under the katalysis of anodic-cathodic, hydrogen atom moves generation hydrogen by solid polyelectrolyte membrane (SPE) to negative electrode, the Sauerstoffatom that remains generates ozone at anode discharge, and platinum Catalytic Layer (the Pt 1mg/cm of negative electrode
2) play the effect that redox reaction generates hydrogen.The technology of this form is still the main flow of current Japanese market electrolysis ozone generator.
The basic structure of this ozonizer is: solid polyelectrolyte membrane (SPE) is placed on central authorities, anode (+electrode) and negative electrode (electrode) are placed on its both sides, anode ultrapure water raw material electrolyzer and negative electrode water storage tank are placed on the both sides of anode electrode and cathode electrode more respectively, the oxygen ozone body that contains that anode generates enters anode gas-liquid separation chamber (generally being called the anode water tank) together with the ozone water that contains ozone by anode electrolytic tank, the different specific weight that utilizes ozone and water is after this process is separated, and the ozone body that contains oxygen is discharged by the top of gas-liquid separation chamber; Water enters anode electrolytic tank by check valve again; The hydrogen G﹠W that negative electrode generates enters negative electrode gas-liquid separation chamber (generally being called the negative electrode water tank) by the negative electrode water storage tank, the different specific weight that utilizes the hydrogen G﹠W is after this is through separation, and hydrogen is by the top discharge of gas-liquid separation chamber and through being discharged in the atmosphere after the air dilution process; Water is discharged by negative electrode gas-liquid separation chamber.The electrolysis structure that this vertical arrangement is put equals electrode and electrolysis also is vertical storing with raw water, electrode and water are contacts side surfaces, the gravity of water is downward, and contacts side surfaces causes the friction contact of electrode and water in the electrolytic process, the ozone body that generates flows in the friction waters up, forms fluidity sinuous flow and loss.And this structure electrolysis groove volume is difficult for excessive, has caused the raw material water yield very little.In addition, friction and the loss that causes of sinuous flow have caused the intensification of liquid, so for the rising of controlled temperature, the means such as in addition exterior cooling water cycle cooling of having to again.The defective that this structure exists is:
(1) because ozone is strong oxidizer, so all overcurrent parts all must adopt the very strong material of erosion resistance, how with titanium alloy, stainless steel 316 with resin materials such as first-class metallic substance or polytetrafluoroethylene PTFE, PFA, component are many, connecting link is many, be difficult between the material connect, cause cost quite expensive, complicated structure can cause the complicated of water supply, liquid level, temperature dispatch control system, also cause the user to increase in aspect difficulty such as management, operation, maintenances, these all cause the limitation in the application;
(2) limit by its technology, in case interruption of power supply, the β-PbO of anode catalyst layer
2Very easily reduce deterioration, will arrive certain current efficiency and used time of concentration when restarting needs the time long, for this reason in case promptly can not cut off the power supply after passing to electric current, needs to be equipped with store battery or emergency power supply in the device, therefore is difficult to use and popularizes;
(3) ozone concn of ozonizer self is unadjustable, needs to reduce concentration by the air-pump inflating dilution when not needing too high ozone concn, has increased the exhaustion point and the consumable accessory hidden danger point of air pump outside the high ozonizer of power consumption again;
(4) its anode needs 10
6The ultrapure water that Ω cm is above, this condition restriction the application of ozonizer, and the environment that can't obtain ultrapure water just can't be used down;
(5) ozonizer is running stores, just need when using certain life-span to change, yet complicated syndeton makes the user can not carry out simple and safe dismounting and change, and must finish replacing under certain operation condition and technology.This also causes difficulty to application.
Hydrogen just is realized as far back as eighties of last century to the validity of human body oxidation-resisting and caducity and various diseases, in recent years, the medical expert of Japan has successfully resolved it theoretically the mechanism of HUMAN HEALTH effect has been caused a sensation, and inquires into hydrogen from all angles and is quickening to launch in the research of the medical effect of daily health caring, disease prevention and clinical treatment.The approach that human body is accepted hydrogen is mainly breathing hydrogen and quotes hydrogeneous water, and the report of injection hydrogen water is also arranged.Though hydrogen is the materials of a large amount of existence of nature, people but can't obtain it in daily life, have a lot of hydrogen and hydrogen water commodity to pour into market suddenly one after another at present, but its confidence level and price are kept someone at a respectful distance the people.
The utility model content
The purpose of this utility model provides a kind of apparatus for electrolyzing, can be ozone, ozone water, hydrogen and hydrogeneous water with water decomposition, and simple in structure, energy consumption is less, and cost is lower, but widespread use.
For achieving the above object, the technical solution of the utility model is:
A kind of apparatus for electrolyzing, it comprises electrolysis cells, water tank, gas liquid mixer, gas-liquid separator, power supply;
Described electrolysis cells comprises housing, and the top of described housing offers water-in, and the below of described water-in is provided with the anode titanium of the arranged transversely that links to each other successively from top to bottom and gives electric orifice plate, β-PbO
2Anode-catalyzed plate, solid polyelectrolyte membrane, Pt/C cathode catalysis plate, cathode titanium are given electric orifice plate, negative electrode water leg, the anode-catalyzed plate of described β-PbO2, Pt/C cathode catalysis plate are compressed to one by β-PbO2 anode-catalyzed electrode and POROUS TITANIUM PLATE, Pt/C cathode catalysis electrode and POROUS TITANIUM PLATE respectively, and described anode titanium is given electric orifice plate, β-PbO
2Anode-catalyzed plate, solid polyelectrolyte membrane, Pt/C cathode catalysis plate, cathode titanium are given electric orifice plate, the negative electrode water leg is fastening by holding bolt is whole electrolytic module, and described negative electrode water leg is provided with the hydrogen water discharge pipe;
The bottom of described water tank is provided with the interlock interface that matches and be connected with the water-in of described housing, and the top of described water tank is provided with ozone vent pipe, water supplement port, and the casing of described water tank is provided with the ozone water relief outlet;
Described gas liquid mixer comprises the mixing tank container that is used to mix ozone and water, described mixing tank container is provided with ozone inlet, water-in, ozone water outlet, described ozone inlet is connected with the ozone vent pipe of described water tank, and described water-in is connected in outside application water source;
Described gas-liquid separator comprises the separator vessel that is used for the separation of hydrogen G﹠W, and described separator vessel is provided with hydrogen water inlet, water port, hydrogen discharge pipe, and described hydrogen water inlet is connected with the hydrogen water discharge pipe of described electrolysis cells;
The positive pole of described power supply is connected for electric orifice plate with the anode titanium, and the negative pole of described power supply is connected for electric orifice plate with cathode titanium.
As a kind of preferred construction, the top of water tank described in the utility model also is movably equipped with top cover, and described ozone vent pipe, water supplement port are arranged on the top cover; Also be provided with ozone on the described ozone vent pipe and utilize mouth, ozone splitter, ozone leak protection valve, it is oxygen that described ozone splitter is used for ozone reduction; Also be provided with liquidometer, temperature sensor on the top cover of described water tank; The ozone inlet and the water-in of described gas liquid mixer are respectively equipped with nozzle; Also be provided with hydrogen utilization mouth and hydrogen gas leakage protective valve on the described hydrogen discharge pipe.
As a kind of preferred improvement structure, power supply described in the utility model comprises adjustment module, overload protection module, overheating protection module and the abnormal protection module that is used for controlling concn.
Alternatively, by being threaded, the water-in of described electrolysis cells is provided with internal thread between electrolysis cells described in the utility model and the water tank, and correspondence is provided with outside screw on the interlock interface of described water tank bottom; Also can be to be connected between described electrolysis cells and the water tank by the bayonet socket make-up.
Preferably, it is the direct puncture orifice plate that is evenly distributed that anode titanium described in the utility model gives electric orifice plate for electric orifice plate, cathode titanium, the area in described hole and give electric orifice plate/cathode titanium for the anode titanium and give more than 40% of the electric orifice plate total area, it is more than the 0.5mm that described anode titanium gives the thickness of electric orifice plate for electric orifice plate/cathode titanium.
Therefore compared with prior art, the utility model has following beneficial effect:
(1) each plate arranged transversely in the utility model electrolysis cells, water during work in the water tank falls to acting directly on the anode electrode naturally, the ozone body that generates through electrolysis directly rises, the loss that does not cause in the electrolysis cells because of frictional force and back flow of gas, reduced the consumption of electric energy, improved the speed that ozone concn rises, in addition, the size of water tank can be changeable as required, water yield abundance, can effectively take away the heat that produces in the electrode catalyst process, play favorable cooling effect, simple in structure, energy consumption is less, cost is lower, but widespread use;
(2) the mutual interlock of electrolysis cells and water tank in the utility model, electrolysis cells can remove and install as changing the bulb, and does not need the instrument of specialty, and is very easy to use;
(3) the utility model can generate 4 kinds of materials that utility value is high and be difficult to obtain simultaneously, that is: ozone gas, ozone water, hydrogen and hydrogeneous air water, the high cleanliness concentration of ozone gas that makes can be up to 250mg/L, consistency of ozone water can be up to 64ppm, and every 1A electric current can obtain high-concentrated ozone body about 4ml/min and the saturated hydrogen of 8ml/min.
Description of drawings
Accompanying drawing described herein is used to provide further understanding of the present utility model, constitutes the application's a part, does not constitute to improper qualification of the present utility model, in the accompanying drawings:
Fig. 1 is the structural representation of the utility model embodiment;
Fig. 2 is the structural representation of electrolysis cells among the utility model embodiment;
Fig. 3 is the structural representation of water tank among the utility model embodiment;
Fig. 4 is the structural representation of gas liquid mixer among the utility model embodiment;
Fig. 5 is the structural representation of gas-liquid separator among the utility model embodiment;
Fig. 6 is a structural representation of giving electroplax among the utility model embodiment.
Embodiment
Describe the utility model in detail below in conjunction with accompanying drawing and specific embodiment, be used for explaining the utility model in this illustrative examples of the present utility model and explanation, but not as to qualification of the present utility model.
As Fig. 1 to the embodiment that Figure 6 shows that a kind of apparatus for electrolyzing described in the utility model, it comprises electrolysis cells 1, water tank 2, gas liquid mixer 3, gas-liquid separator 4, power supply 5, electrolysis cells 1 comprises housing 10, the top of housing 10 offers water-in, and the below of water-in is provided with the anode titanium of the arranged transversely that links to each other successively from top to bottom and gives electric orifice plate 11, β-PbO
2Anode-catalyzed plate 12, solid polyelectrolyte membrane 13, Pt/C cathode catalysis plate 14, cathode titanium are given electric orifice plate 15, negative electrode water leg 17, β-PbO
2Anode-catalyzed plate 12, Pt/C cathode catalysis plate 14 are compressed to one by β-PbO2 anode-catalyzed electrode and POROUS TITANIUM PLATE, Pt/C cathode catalysis electrode and POROUS TITANIUM PLATE respectively, and the anode titanium is given electric orifice plate 11, β-PbO
2It is whole electrolytic module that anode-catalyzed plate 12, solid polyelectrolyte membrane 13, Pt/C cathode catalysis plate 14, cathode titanium give electric orifice plate 15, negative electrode water leg 17 fastening by holding bolt 18, and negative electrode water leg 17 is provided with hydrogen water discharge pipe 19; The bottom of water tank 2 is provided with the interlock interface 21 that matches and be connected with the water-in of housing 10, and the top of water tank 2 is provided with ozone vent pipe 23, water supplement port 24, and the casing of water tank 2 is provided with ozone water relief outlet 25; Gas liquid mixer 3 comprises the mixing tank container 31 that is used to mix ozone and water, mixing tank container 31 is provided with ozone inlet 32, water-in 33, ozone water outlet 34, ozone inlet 32 is connected with the ozone vent pipe 23 of water tank 2, and water-in 33 is connected in the application water source of outside; Gas-liquid separator 4 comprises the separator vessel 41 that is used for the separation of hydrogen G﹠W, and separator vessel 41 is provided with hydrogen water inlet 42, water port 44, hydrogen discharge pipe 43, and hydrogen water inlet 42 is connected with the hydrogen water discharge pipe 19 of electrolysis cells 1; The positive pole 51 of power supply 5 is connected for electric orifice plate 11 with the anode titanium, and the negative pole 52 of power supply 5 is connected for the negative electrode of electric orifice plate 15 with cathode titanium.
During work, water in the water tank 2 falls in the electrolysis cells 1 naturally by interlock interface 21, water is electrolyzed to produce ozone and hydrogen, wherein ozone rises in the water tank 2, water in the water tank 2 becomes the saturated ozone water of high density gradually, ozone overflows the water surface and enters in the gas liquid mixer 3 by ozone vent pipe 23 and ozone inlet 32, mixes the ozone water of lower concentration from ozone water outlet 34 can obtain continuously with answering water; It is hydrogen water that the hydrogen that electrolysis produces is assembled in negative electrode water leg 17, and flow into gas-liquid separator 4 by vent pipe 19 and hydrogen water inlet 42 successively, the hydrogen G﹠W constantly separates therein, hydrogen is discharged from hydrogen discharge pipe 43, and the water that contains the not separated hydrogen that falls is discharged from water port 44 and can directly be utilized; β-PbO
2Anode-catalyzed plate 12, Pt/C cathode catalysis plate 14 are compressed to one by β-PbO2 anode-catalyzed electrode and POROUS TITANIUM PLATE, Pt/C cathode catalysis electrode and POROUS TITANIUM PLATE respectively, the gap that can not have loose contact, reduce the impedance of conduction, improved current work efficient; β-PbO
2Anode-catalyzed plate 12 is made by chemical method, degradation phenomena can not occur, recovers works better within a short period of time but restart after the outage, does not need to be equipped with store battery or emergency power supply.
In the present embodiment, the top of water tank 2 also is movably equipped with top cover 22, and ozone vent pipe 23, water supplement port 24 are arranged on the top cover 22, and the movable top cover 22 that is provided with detachably gets off during use, is convenient to install and repairs; Also be provided with ozone on the ozone vent pipe 23 and utilize mouth 26, ozone splitter 27, ozone leak protection valve 28, it is oxygen that ozone splitter 27 is used for ozone reduction, ozone leak protection valve 28 can stop its leakage when ozone is not utilized, ozone enters ozone splitter 27, just is thrown in the air after thoroughly being reduced into oxygen; Also be provided with liquidometer 29, temperature sensor 20 on the top cover 22 of water tank 2, liquidometer 29 can be regulated the liquid level in the control water tank 2; The ozone inlet 32 of gas liquid mixer 3 and the meet of water-in 33 are provided with nozzle 34; Also be provided with hydrogen utilization mouth 45 and hydrogen gas leakage protective valve 46 on the hydrogen discharge pipe 43, when hydrogen was not utilized, hydrogen gas leakage protective valve 46 can stop the hydrogen leak outflow; Power supply 5 comprises the adjustment module that is used for controlling concn; the overload protection module; overheating protection module and abnormal protection module; the serviceability of power supply 5 and anodic-cathodic characteristic are coincide mutually; can be by improving or reduce the size adjustment that its output services power is realized ozone output; and then reach the purpose of regulating the using ozone water concentration; the effect of the overheating protection module of power supply 5 is to cut off the electricity supply automatically when electrolysis cells work is overheated; the effect of overload protection module is that electric current and voltage can be regulated automatically when the service rating superelevation; the effect of abnormal protection module is aging or extraneously can cut off the electricity supply when unusual when electrolysis cells; and can freely restart behind the power dump, do not need to be equipped with store battery or emergency use protection power supply.
In the present embodiment, adopt between electrolysis cells 1 and the water tank 2 and be threaded, the water-in of electrolysis cells 1 is provided with internal thread 16, correspondence is provided with outside screw on the interlock interface 21 of water tank 2 bottoms, electrolysis cells 1 can remove and install as changing the bulb like this, do not need the instrument of specialty, very easy to use; During real work, also can be to be connected between electrolysis cells 1 and the water tank 2 by the bayonet socket make-up.
In order to improve resistance to overturning, in the present embodiment, the anode titanium gives the direct puncture orifice plate of electric orifice plate 15 for being evenly distributed for electric orifice plate 11, cathode titanium, the area in hole and give electric orifice plate 11/ cathode titanium for the anode titanium and give more than 40% of electric orifice plate 15 total areas, it is more than the 0.5mm that the anode titanium gives the thickness of electric orifice plate 15 for electric orifice plate 11/ cathode titanium, can improve the stability of whole device like this, also the rising of easier controlled temperature.
The utility model can be according to demand consumption and concentration, be made into the device of various different sizes, as long as can realize to obtain the single-phase DC electricity and drink the pure water of grade, just can plug and play, not only can be widely used in industry, also provide possibility for extensively popularizing of family, cause institute, office, school, dentistry, medical treatment and public place.As utilize the utility model technological development to be used for the small-sized machine of family, and then its current consumption only is about 25W, the consumption in operation raw material water yield is about 25cc/h.Mix with tap water and the concentration ozone about up to 250mg/L, can obtain flow continuously and be about 1.5L/min, concentration is the ozone water about 4ppm, except that can be used for the cleaning of fruit and vegetable, fishery products, chopping board, cutter, tableware, towel etc., also can soak the effect of dirt settling to eliminate the surface such as fruit and vegetable and aquatic products raw meat, can also be used to wash one's hands, gargle, foot bath, hair washing etc. to reach fresh-keeping and to prolong staging life.In the high-concentration ozone water spray chamber that directly takes a morsel, refuse container, sewage draining exit etc., can also play purify air, effect such as deodoring and disinfecting.Directly utilize the ozone body of trace, more can be when bacteriophage be popular family, office, school and public place etc. keep off infection and spread, hydrogen of producing simultaneously and hydrogeneous water also can utilize, and prevent human senescence and daily health caring.
More than technical scheme that the utility model embodiment is provided be described in detail, used specific case herein principle and the embodiment of the utility model embodiment are set forth, the explanation of above embodiment only is applicable to the principle that helps to understand the utility model embodiment; Simultaneously, for one of ordinary skill in the art, according to the utility model embodiment, the part that on embodiment and range of application, all can change, in sum, this description should not be construed as restriction of the present utility model.
Claims (10)
1. apparatus for electrolyzing is characterized in that:
It comprises electrolysis cells, water tank, gas liquid mixer, gas-liquid separator, power supply;
Described electrolysis cells comprises housing, and the top of described housing offers water-in, and the below of described water-in is provided with the anode titanium of the arranged transversely that links to each other successively from top to bottom and gives electric orifice plate, β-PbO
2Anode-catalyzed plate, solid polyelectrolyte membrane, Pt/C cathode catalysis plate, cathode titanium are given electric orifice plate, negative electrode water leg, the anode-catalyzed plate of described β-PbO2, Pt/C cathode catalysis plate are compressed to one by β-PbO2 anode-catalyzed electrode and POROUS TITANIUM PLATE, Pt/C cathode catalysis electrode and POROUS TITANIUM PLATE respectively, and described anode titanium is given electric orifice plate, β-PbO
2Anode-catalyzed plate, solid polyelectrolyte membrane, Pt/C cathode catalysis plate, cathode titanium are given electric orifice plate, the negative electrode water leg is fastening by holding bolt is whole electrolytic module, and described negative electrode water leg is provided with the hydrogen water discharge pipe;
The bottom of described water tank is provided with the interlock interface that matches and be connected with the water-in of described housing, and the top of described water tank is provided with ozone vent pipe, water supplement port, and the casing of described water tank is provided with the ozone water relief outlet,
Described gas liquid mixer comprises the mixing tank container that is used to mix ozone and water, described mixing tank container is provided with ozone inlet, water-in, ozone water outlet, described ozone inlet is connected with the ozone vent pipe of described water tank, and described water-in is connected in outside application water source
Described gas-liquid separator comprises the separator vessel that is used for the separation of hydrogen G﹠W, and described separator vessel is provided with hydrogen water inlet, water port, hydrogen discharge pipe, and described hydrogen water inlet is connected with the hydrogen water discharge pipe of described electrolysis cells,
The positive pole of described power supply is connected for electric orifice plate with the anode titanium, and the negative pole of described power supply is connected for electric orifice plate with cathode titanium.
2. apparatus for electrolyzing according to claim 1 is characterized in that: the top of described water tank also is movably equipped with top cover, and described ozone vent pipe, water supplement port are arranged on the top cover.
3. apparatus for electrolyzing according to claim 1 is characterized in that: also be provided with ozone on the described ozone vent pipe and utilize mouth, ozone splitter, ozone leak protection valve, it is oxygen that described ozone splitter is used for ozone reduction.
4. apparatus for electrolyzing according to claim 2 is characterized in that: also be provided with liquidometer, temperature sensor on the top cover of described water tank.
5. apparatus for electrolyzing according to claim 1 is characterized in that: the ozone inlet and the water-in of described gas liquid mixer are respectively equipped with nozzle.
6. apparatus for electrolyzing according to claim 1 is characterized in that: also be provided with hydrogen utilization mouth and hydrogen gas leakage protective valve on the described hydrogen discharge pipe.
7. apparatus for electrolyzing according to claim 1 is characterized in that: described power supply is provided with adjustment module, overload protection module, overheating protection module and the abnormal protection module that is used for controlling concn.
8. apparatus for electrolyzing according to claim 1 is characterized in that: by being threaded, the water-in of described electrolysis cells is provided with internal thread between described electrolysis cells and the water tank, and correspondence is provided with outside screw on the interlock interface of described water tank bottom.
9. apparatus for electrolyzing according to claim 1 is characterized in that: be connected by the bayonet socket make-up between described electrolysis cells and the water tank.
10. apparatus for electrolyzing according to claim 1, it is characterized in that: it is the direct puncture orifice plate that is evenly distributed that described anode titanium gives electric orifice plate for electric orifice plate, cathode titanium, the area in described hole and give electric orifice plate/cathode titanium for the anode titanium and give more than 40% of the electric orifice plate total area, it is more than the 0.5mm that described anode titanium gives the thickness of electric orifice plate for electric orifice plate/cathode titanium.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202356357U CN201746592U (en) | 2010-06-22 | 2010-06-22 | Water electrolysis device |
| JP2013600027U JP3185328U (en) | 2010-06-22 | 2011-06-27 | Water electrolyzer |
| PCT/CN2011/001061 WO2011160446A1 (en) | 2010-06-22 | 2011-06-27 | Water electrolytic device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202356357U CN201746592U (en) | 2010-06-22 | 2010-06-22 | Water electrolysis device |
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| CN201746592U true CN201746592U (en) | 2011-02-16 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010202356357U Expired - Lifetime CN201746592U (en) | 2010-06-22 | 2010-06-22 | Water electrolysis device |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP3185328U (en) |
| CN (1) | CN201746592U (en) |
| WO (1) | WO2011160446A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102295326A (en) * | 2010-06-22 | 2011-12-28 | 刘迅 | Water electrolysis device |
| CN102899685A (en) * | 2012-09-12 | 2013-01-30 | 金华市广源环保科技有限公司 | Cathode and anode catalyst for low-voltage electrolytic ozone generator module and preparation method thereof |
| CN111206265A (en) * | 2018-11-21 | 2020-05-29 | 元智大学 | Air-water circulating system and multifunctional water electrolysis device thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63100190A (en) * | 1986-10-16 | 1988-05-02 | Sasakura Eng Co Ltd | Electrolytic device for generating gas |
| JP3048612B2 (en) * | 1990-09-06 | 2000-06-05 | ペルメレック電極株式会社 | Electrolytic ozone generator |
| JP3297250B2 (en) * | 1995-06-15 | 2002-07-02 | 三菱重工業株式会社 | Electrolytic ozone generator |
| TW401373B (en) * | 1997-03-07 | 2000-08-11 | Univ Wuhan | Electrolytic ozone generating apparatus |
| JP2001104995A (en) * | 1999-10-07 | 2001-04-17 | Teeiku Wan Sogo Jimusho:Kk | Electrolytic ozone forming method, electrolytic ozone forming apparatus and ozone water making apparatus |
| CN2431290Y (en) * | 2000-07-04 | 2001-05-23 | 胡柏 | Generator for producing ozone by electrolyzing process |
| CN2431291Y (en) * | 2000-07-11 | 2001-05-23 | 上海奥赛科技有限公司 | Generator for producing large flow of ozone water |
| HUP0501204A2 (en) * | 2005-12-23 | 2007-07-30 | Thales Rt | Ozone generating electrolytic cell |
-
2010
- 2010-06-22 CN CN2010202356357U patent/CN201746592U/en not_active Expired - Lifetime
-
2011
- 2011-06-27 WO PCT/CN2011/001061 patent/WO2011160446A1/en active Application Filing
- 2011-06-27 JP JP2013600027U patent/JP3185328U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102295326A (en) * | 2010-06-22 | 2011-12-28 | 刘迅 | Water electrolysis device |
| CN102899685A (en) * | 2012-09-12 | 2013-01-30 | 金华市广源环保科技有限公司 | Cathode and anode catalyst for low-voltage electrolytic ozone generator module and preparation method thereof |
| CN111206265A (en) * | 2018-11-21 | 2020-05-29 | 元智大学 | Air-water circulating system and multifunctional water electrolysis device thereof |
| CN111206265B (en) * | 2018-11-21 | 2021-06-04 | 元智大学 | Air-water circulating system and multifunctional water electrolysis device thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3185328U (en) | 2013-08-15 |
| WO2011160446A1 (en) | 2011-12-29 |
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