CN206368199U - Pure water hydrogen and oxygen electrolyzing manufacturing machine - Google Patents

Pure water hydrogen and oxygen electrolyzing manufacturing machine Download PDF

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Publication number
CN206368199U
CN206368199U CN201720012104.3U CN201720012104U CN206368199U CN 206368199 U CN206368199 U CN 206368199U CN 201720012104 U CN201720012104 U CN 201720012104U CN 206368199 U CN206368199 U CN 206368199U
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hydrogen
layer
oxygen
pure water
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黄林祥
蔡启圣
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North Vision Tech Inc
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)

Abstract

A kind of pure water hydrogen and oxygen electrolyzing manufacturing machine is that an electrolysis unit is positioned over into a sealing to contain body, by the PEM in electrolysis unit, catalyst layer, diffusion metal level, electrode, deionized water is electrolysed, it is set to produce hydrogen and oxygen, and it is gas-insulated by two kinds, it is not more than 60 microns of alloy diffusion metal level by aperture, and porosity is higher than 25%, reaches preferably hydrogen manufacturing and oxygen generation efficiency.

Description

Pure water hydrogen and oxygen electrolyzing manufacturing machine
Technical field
A kind of pure water hydrogen and oxygen electrolyzing manufacturing machine, for for producing hydrogen and oxygen.
Background technology
Most hydrogen is all present in the forms such as water and organic compound on the earth, and hydrogen is a kind of colourless, odorless, nothing The nonmetallic gas of taste, and it is easy to collection again because not having toxicity and radioactivity, or even high-energy can be produced, and it is anti-with oxygen element Should so that have wide range of applications, including chemistry, physics, even engineering science, physiology etc., especially medically, ground according to part Study carefully prompting, hydrogen can produce reaction bonded with hydroxy radical, the residual of internal hydroxy radical thereby be reduced, again it is desirable that hydrogen The strong anti-oxidation power that molecule possesses, can develop more benefit materials.
And the mode for obtaining hydrogen includes heat chemistry, water-gas, water electrolysis, steam restructuring etc. and may achieve, it will especially steam Hydrogen yield when gas recombination method is used for natural gas is a kind of method on the largest scale.When vapor and methane high temperature about 1000- When 1400K reacts, carbon monoxide and hydrogen can be produced, in this reaction, relatively low pressure is bestowed to course of reaction on the contrary Efficiency can more be more than high pressure, but must be carried out under high pressure for fear of hydrogen purification system, to shorten the time so that course of reaction Equally using high pressure by the way of, however, but also therefore limit output efficiency, on the other hand, due to needed during output pressurization add Temperature, even if the mode for being adjusted by pressure shortens processing time, but the amplitude shortened is still limited, and hydrogen molecule is at high temperature Hydrogen atom is easily dissociated into, the big hydrogen atom of activity will likely produce reaction with other elements, therefore hydrogen purity will be caused to beat greatly Discount, furthermore, it is careless slightly in the case of mass storage also because hydrogen activity is big, i.e., it can cause peace event of endangering.
Another common method is water electrolysis method, adds water to electrolyte formation solion, and logical with a pair of electrodes Enter direct current to be electrolysed, hydrogen and oxygen are produced via redox reaction, but which is because must be added to electrolyte ability Make water decomposition, be especially usually to add strong acid or highly basic as electrolyte, so the hydrogen purity produced still has doubt.
As PEM comes out, water electrolysis may not necessarily rely on the addition of electrolyte again, but directly by pure water electricity Solution, as shown in figure 5, there is an apparatus for electrolyzing 9, pure water enters reaction chamber 92 by anode-side, reaction chamber 92 in addition to an electrode, The anode diffusion layer and anode catalyst layer of stainless (steel) wire are additionally provided with, it is conductive and anode catalyst layer by stainless (steel) wire Effect, pure water dissociates as oxonium ion and hydrogen ion herein, oxonium ion then guide be connected to anode stainless (steel) wire release electronics and As oxygen discharge;Hydrogen ion and water can penetrate the PEM in reaction chamber 92, further touch cathode catalysis Oxidant layer, and rear the cathode diffusion layer that is constituted of carbon paper or carbon cloth, hydrogen ion leads via carbon paper or carbon cloth Electrical and permeability, reception is reduced into hydrogen discharge via the electronics that negative electrode is provided.
Wherein, because the inoxidizability of carbon fiber is extremely low, therefore it is only capable of not using in anode-side as cathode diffusion layer; Though the tensile strength of another aspect carbon fiber is big, bend resistance effect is poor, it is impossible to bear lateral larger pressure;Especially carbon is fine Wei Bu is that, to weave shaping, thickness can not arbitrarily increase, and also further limits the thickness of cathode diffusion layer, with regard to this influence hydrogen ion Useful effect region between cathode diffusion layer.
Therefore, how to increase the useful effect region between hydrogen ion and cathode diffusion layer, lift the production capacity of hydrogen, and Allow anode diffusion layer and cathode diffusion layer to use identical material-structure, the diffusion layer of both sides arbitrarily can be exchanged mutually, does not have There is the risk of assembly defect, also reduce cost of getting the raw materials ready, and bear lateral pressure conversion, be exactly this case focus to be improved.
Utility model content
Main purpose of the present utility model, is to provide a kind of with identical diffusion metal-layer structure, while as cloudy Pole and the pure water hydrogen and oxygen electrolyzing manufacturing machine of anode diffusion layer, because both sides use identical material, structure, can arbitrarily be exchanged, by To reduce get the raw materials ready management cost and the risk of assembly defect.
Another object of the present utility model, be to provide it is a kind of with diffusion metal level as negative electrode and anode diffusion layer Pure water hydrogen and oxygen electrolyzing manufacturing machine, because the ductility for spreading metal level is good, can bear after a large amount of generations of gas, chamber interior Pressure increase, to lift reliability and extend warranty cycle.
A further object of the present utility model, is to provide a kind of with pure water electrolysis hydrogen of the diffusion metal level as diffusion layer Oxygen manufacturing machine, by increase thickness of diffusion layer, is substantially improved hydrogen production efficiency.
A kind of pure water hydrogen and oxygen electrolyzing manufacturing machine disclosed in this case, including:One electrolysis unit and a sealing contain body, by Sealing contains the water injection hole injection pure water on body, is diffused to via anode metal layer after one layer of oxidation catalyst layer, pure water receives The electric energy of electrode supply is dissociated, and isolates oxygen with hydrogen ion by PEM, and hydrogen ion meets reducing catalyst layer It is reduced into after hydrogen and passes through by cathode metal layer, negative electrode, is finally discharged by hydrogen blistering, in addition, oxygen is then via anode metal layer, sun Pole, is finally discharged by oxygen outlet.
It is with the diffusion made by such as titanium or its alloy by the pure water hydrogen and oxygen electrolyzing manufacturing machine that this case is provided Metal level, the thickness of hundreds of microns (μm) can be not only obtained easily so that useful effect region increases, and use lifting aerogenesis Efficiency;And with good bend resistance ability, in the case where gas producing efficiency is lifted, the environment that can be increased with proof pressure is carried High product service life;And using identical structure simultaneously as anode metal layer and cathode metal layer, the therebetween matter of clipping Proton exchange and catalyst layer, are not required to prepare two kinds of different diffusion layer materials, therefore can reduce and get the raw materials ready and manage in assembling Cost.
Brief description of the drawings
Fig. 1 is the perspective view of the preferred embodiment of the utility model first, for illustrating pure water hydrogen and oxygen electrolyzing manufacturing machine Structure
Fig. 2 is Fig. 1 sectional view, for aiding in illustrating structure relative position.
Fig. 3 is the partial perspective view of the preferred embodiment of the utility model first, for illustrating another fixed proton exchange The mode of film.
Fig. 4 is the perspective view of the preferred embodiment of the utility model second, for illustrating two groups of pure water hydrogen and oxygen electrolyzing systems Make the structure after machine is combined.
Fig. 5 is the schematic perspective view of known technology.
Symbol description
1st, 1 ' ... electrolysis unit 11,11 ' ... PEMs
13rd, 13 ' ... catalyst layer 131 ... oxidation catalyst layers
133 ... reducing catalysts layer 15,15 ' ... spreads metal level
153 ... anode metal layer 155 ... cathode metal layers
17 ... electrodes 171,171 ' ... anodes
173rd, the sealing of 173 ' ... negative electrodes 2,2 ' ... contains body
21 ... water injection hole 23 ... hydrogen blisterings
25 ... oxygen outlet 27 ... packaging insulating housings
271 ... anode casing 273 ... cathode shells
277 ... flexible waterproof layer 9 ... apparatus for electrolyzing
92 ... reaction chambers
Embodiment
About of the present utility model foregoing and other technology contents, feature and effect, in following cooperation Figure of description In the detailed description of preferred embodiment, it can clearly appear from;In addition, in embodiments, identical element is by with similar mark Number represent.
The pure water hydrogen and oxygen electrolyzing manufacturing machine of the preferred embodiment of this case first, please with reference to shown in Fig. 1 to Fig. 3, pure water is electric There is solution hydrogen-oxygen manufacturing machine an electrolysis unit 1 and a sealing for containing electrolysis unit 1 to contain body 2, wherein, sealing is contained Body 2 is made up of in this example packaging insulating housing 27 and two panels seal, wherein, packaging insulating housing 27 includes anode Housing 271 and cathode shell 273, another seal further include a flexible waterproof layer 277 for being interpreted as water proof rubber, and in this example An open-work is formed, certainly, the flexible waterproof layer forms a plurality of open-works without for fear of this case implementation.
For purposes of illustration only, the PEM 11 in above-mentioned electrolysis unit 1 is set into symmetrical center line and anti-with two panels flexibility The sandwiched PEM 11 of water layer 277, uses the structure that PEM is protected in both sides, extends the life-span of PEM, and The open-work of two flexible waterproof layers 277 is covered with PEM 11, now, two sides are sequentially symmetrical arranged to the left and right by symmetrical center line Be the catalyst layer 13 for being coated on PEM 11, diffusion metal level 15 and be close to diffusion metal level 15 electrode 17.For It is easy to explanation, the region surrounded jointly by PEM 11, flexible waterproof layer 277 and anode casing 271 is defined herein is One oxidation space, for accommodating oxidation catalyst layer 131, anode metal layer 153, anode 171;Relatively, definition is by PEM 11st, the region that flexible waterproof layer 277 and cathode shell 273 are surrounded jointly is then referred to as a reduction space, for accommodating reducing catalyst layer 133rd, cathode metal layer 155, negative electrode 173, both of the aforesaid reaction compartment are two separate spaces, and deionized water is only capable of being handed over by proton Film 11 is changed to pass through, and the hydrogen produced by respective region then completely cuts off completely with oxygen, it is impossible to it is penetrating.
Certainly, except two layers of flexible waterproof layer 277 is sandwiched therebetween by PEM 11, support, waterproof and gas-tight are used as External let out waits effect, and single flexible waterproof layer 277 can be more directly arranged at using PEM 11, and simplification structure is easy to Change.
In this example, diffusion metal level 15 is interpreted as the fine and close orifice plate of titanium, and titanium densification orifice plate has plural number small Through hole (not shown), and the aperture of through hole is 20 to 60 microns, and overall porosity is then 30% to 50%.Due in this example The fine and close orifice plate of titanium there are 700 to 800 micron thickness, and porosity is very big so that hydrogen ion or oxonium ion are carrying out oxygen When change or reduction, excellent compaction interval can be provided, allow gas producing efficiency to double.Even learnt via experiment, When aperture is 30 microns and porosity is 40%, optimal hydrogen generation efficiency can be reached.Another aspect, by the strong against corrosion of titanium The features such as property, high-strength structure, the damage that oxidation reaction is caused can be greatly reduced.
During running, deionized water is injected by the water injection hole 21 for being arranged at anode casing 271, until liquid level is close to anode The hydrogen blistering 23 on oxygen outlet 25 and cathode shell 273 on housing 271, and open electrode switch be powered proceed by solution From.In this example, to lift the production capacity of hydrogen, the dense porous knot of about 700 to 800 microns of diffusion metal level 15 of thickness is utilized Structure, increases the surface area of oxidation/reduction reaction, compared to the tens of microns thickness of conventional carbon cloth, can greatly improve production Tolerance.When deionized water touches anode region and is accelerated by anode catalyst, it is electrolysed immediately and disengages hydrogen ion and hydrogen Oxygen radical ion.
Wherein, in hydroxide ion, it is partially exposed to and disengages electronics including anode 171 and the grade of anode metal layer 153, and And form oxygen molecule;Hydrogen ion then passes through PEM by the acid ion transmission on hydrone and PEM 11 11st, reducing catalyst layer 133 and reach the fine and close orifice plate of titanium as cathode metal layer 155, negative electrode 173 is then by this titanium Fine and close orifice plate, discharges electronics on a large scale, and hydrogen is combined to form with hydrogen ion.Because being using deionized pure in electrolytic process Water, the interference without strong acid or highly basic thereby can expeditiously obtain the hydrogen of higher purity, the hydrogen is immediately by hydrogen blistering 23 Discharge is then discharged for a small amount of storages, oxygen by oxygen outlet 25.
The preferred embodiment of this case second, as shown in figure 4, including two groups of electrolysis units in the pure water hydrogen and oxygen electrolyzing manufacturing machine 1 ', and contain the sealing of electrolysis unit 1 ' and contain body 2 ' to save space and cost, will by the way of partial electrode is shared All electrolysis units are combined, in this example, are hydrogen due to what is mainly collected, therefore the cathode electrode for producing hydrogen is total to With.Wherein, the structure of each electrolysis unit is all similar with first embodiment, therefore will not be repeated here.In two groups of electrolysis units 1 ' PEM 11 ' and both sides anode 171 ' and negative electrode 173 ', it is all sandwiched by the institute of diffusion metal level 15 ' of both sides respectively It is fixed, the area of PEM 11 ' is just corresponded to due to spreading the size of metal level 15 ' so that the diffusion gold of both sides Category layer 15 ' is close to the catalyst layer 13 ' of the both sides of PEM 11 ' respectively, and this also causes between the diffusion metal level 15 ' of both sides Apart from extremely short, the electric field of uniform and high intensity is thereby formed in the both sides of PEM 11 ', makes overall dissociation efficiency is relative to carry Rise.
It the foregoing is only preferred embodiment of the present utility model, it is impossible to the model of the utility model implementation is limited with this Enclose, every simple equivalent changes and modifications made according to the utility model claims and description all should still belong to In the range of the utility model patent covers.

Claims (4)

1. a kind of pure water hydrogen and oxygen electrolyzing manufacturing machine, it is characterised in that including:
An at least electrolysis unit, including
At least one for ion penetration PEM, and in foregoing PEM two opposite sides be respectively coated one layer oxidation touch Matchmaker's layer and one layer of reducing catalyst layer;
A pair of diffusion metal levels with plural through hole include one layer and are disposed proximate in the anode metal layer of above-mentioned oxidation catalyst layer, It is disposed proximate to another in the cathode metal layer of above-mentioned reducing catalyst layer;
At least one pair of electrode includes an anode, and for being connected to above-mentioned anode metal layer, and one is connected to above-mentioned cathode metal layer Negative electrode;And
One sealing for containing above-mentioned electrolysis unit contains body, and the sealing contains body with a water injection hole, a hydrogen blistering, and One oxygen outlet, and aforementioned seal is injected into by foregoing water injection hole contains intrinsic deionized water liquid level less than foregoing hydrogen Hole and foregoing oxygen outlet.
2. pure water hydrogen and oxygen electrolyzing manufacturing machine as claimed in claim 1, it is characterised in that it is anti-that wherein above-mentioned sealing, which contains body, Water material.
3. pure water hydrogen and oxygen electrolyzing manufacturing machine as claimed in claim 2, it is characterised in that wherein above-mentioned sealing contains body and more wrapped Include two packaging insulating housings, and at least one foregoing two packaging insulatings housing joint of sealing seal.
4. pure water hydrogen and oxygen electrolyzing manufacturing machine as claimed in claim 3, it is characterised in that wherein above-mentioned seal is further included at least One flexible waterproof layer.
CN201720012104.3U 2017-01-05 2017-01-05 Pure water hydrogen and oxygen electrolyzing manufacturing machine Active CN206368199U (en)

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Application Number Priority Date Filing Date Title
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110512227A (en) * 2018-05-21 2019-11-29 洪昆喨 Electro-catalysis discharge reactor, hydrogen generating system and hydrogen production process
CN113874556A (en) * 2018-12-19 2021-12-31 唐纳德·欧文斯 Hydrogen production system and apparatus for improved fuel efficiency

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110512227A (en) * 2018-05-21 2019-11-29 洪昆喨 Electro-catalysis discharge reactor, hydrogen generating system and hydrogen production process
CN113874556A (en) * 2018-12-19 2021-12-31 唐纳德·欧文斯 Hydrogen production system and apparatus for improved fuel efficiency

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GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20171226

Address after: No. 1, No. 15, industrial east two, industrial park, Hsinchu, Taiwan, China

Co-patentee after: Cai Qisheng

Patentee after: NORTH VISION TECH Inc.

Address before: 2 floor, 52 Dongming street, Eastern Hsinchu

Co-patentee before: Cai Qisheng

Patentee before: Huang Linxiang

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20200331

Address after: No. 1, No. 15, industrial east two, industrial park, Hsinchu, Taiwan, China

Co-patentee after: Youxin Technology Co.,Ltd.

Patentee after: NORTH VISION TECH Inc.

Address before: No. 1, No. 15, industrial east two, industrial park, Hsinchu, Taiwan, China

Co-patentee before: Cai Qisheng

Patentee before: NORTH VISION TECH Inc.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20230829

Address after: No. 1, No. 15, industrial east two, industrial park, Hsinchu, Taiwan, China

Patentee after: NORTH VISION TECH Inc.

Address before: No. 1, No. 15, industrial east two, industrial park, Hsinchu, Taiwan, China

Patentee before: NORTH VISION TECH Inc.

Patentee before: Youxin Technology Co.,Ltd.