CN205368508U - Divide cavate hydrogen oxygen partial pressure from electrolytic device - Google Patents
Divide cavate hydrogen oxygen partial pressure from electrolytic device Download PDFInfo
- Publication number
- CN205368508U CN205368508U CN201521102919.8U CN201521102919U CN205368508U CN 205368508 U CN205368508 U CN 205368508U CN 201521102919 U CN201521102919 U CN 201521102919U CN 205368508 U CN205368508 U CN 205368508U
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- CN
- China
- Prior art keywords
- electrolysis
- hydrogen
- ion exchange
- exchange membrane
- amberplex
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- 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.)
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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 divide cavate hydrogen oxygen partial pressure from electrolytic device, the device include electrolysis trough, amberplex, control circuit board and lithium cell, amberplex's rim seal is fixed on the inner wall of electrolysis trough, and the electrolysis trough passes through to form a seal chamber and the 2nd seal chamber after amberplex separates, and a seal chamber lies in amberplex's below, and the 2nd seal chamber lies in amberplex's top, a seal chamber internal fixation has the positive electricity polar plate that parallels and lie in its below with amberplex, and the 2nd seal chamber internal fixation has the negative electricity polar plate that parallels and lie in its top with amberplex, amberplex is slope form to be fixed on the inner wall of electrolysis trough, a formation gaseous triangular space between the horizontal plane that the brineelectrolysis is close to this acute angle and the inside wall of positive electricity polar plate and electrolysis trough. The utility model discloses an amberplex has realized oxygen and other clean separation gaseous and hydrogen, has realized producing of pure hydrogen then.
Description
Technical field
This utility model relates to hydrogen-oxygen separation technology field, particularly relates to a kind of cavity-separating hydrogen-oxygen separation electrolysis unit.
Background technology
The gas that density that hydrogen is known in the world is minimum, is the minimum material of relative molecular mass, and hydrogen is the element that in universe, content is maximum, and the quality of hydrogen only has the 1/14 of air, and namely when 0 DEG C, a standard atmosphere pressure, the density of hydrogen is 0.0899g/L.
Large number of biological research shows, hydrogen has the effect in selectivity with free radical and nitrous acid anion, and this is that anti-oxidative damage is treated the basis of disease by hydrogen.Research shows, the disease type that hydrogen can be treated is very many, for instance more than the 68 kind of disease such as encephalopathy, cerebral ischemia, alzheimer disease, parkinson disease, depression, spinal cord injury, skin allergy, type 2 diabetes mellitus, acute pancreatitis, organ transplant injury, small intestinal ischemia, system inflammation reaction, radiation injury, retina injury and deafness after malignant tumor, colitis, carbon monoxide poisoning.It is worth although human body is had potential treatment disease by hydrogen, but in order to reach antioxidative purpose, how to use hydrogen to be still the major issue that we face.The mode of currently used hydrogen has 3 kinds, and one is can adopt directly to breathe the mixing gas containing hydrogen, and two is the solution drinking or injecting hydrogen, and three is produce hydrogen through skin diffusion and induction E.From using and economic angle considers, it is more satisfactory method that ordinary people drinks the water of hydrogen.Being used by a large amount of crowds on Japan, TaiWan, China, Hong Kong and other places, hydrogen will become the healthy patron saint of the mankind.How hydrogen manufacturing becomes the problem that human needs solves.
1972, Japanese Scientists fujishima and honda found to use ultraviolet radiation TiO under applied voltage2Water decomposition is produced hydrogen by electrode, discloses the probability of available decomposing water with solar energy hydrogen first.This Optical Electro-Chemistry transformation process utilizes solar energy to produce hydrogen by photochemical catalyzing, solar energy low for energy density is converted to there is high-energy, density, high efficiency chemical energy, it it is a kind of desirably green hydrogen manufacturing approach, being expected to solve the problem of energy resource supply and environmental pollution, therefore this technology is most to have theoretical significance and actual application prospect simultaneously.But this technology faces a problem in application process: how the gas that photoelectrolysis produces in running carries out ON-LINE SEPARATION.Although this mode utilizes light energy source to solve the preparation of hydrogen, but cannot obtain pure hydrogen, in the process separated, hydrogen is easy to mix with other gas, and it is toxic that this gas has, and therefore have impact on the use of hydrogen.
Along with expanding economy, the follow-up device occurring in that a kind of water electrolysis obtains hydrogen-oxygen, be still employing KOH or NaOH solution by domestic and international existing electrolysis moisture after, decompose electrolysis water with plumbous zinc electrode and obtain hydrogen and oxygen, required electronics is about 3kw/h-5kw/h.This isolation not only gas production is not enough, and the hydrogen most importantly decomposited and oxygen cannot separate, and therefore still cannot realize the preparation of pure hydrogen.
Summary describes, and is badly in need of one on the market and can complete to separate hydrogen with oxygen and other gas, obtains the technology of pure hydrogen.
Utility model content
For the weak point existed in above-mentioned technology, this utility model provides a kind of cavity-separating hydrogen-oxygen separation electrolysis unit, electrolysis bath is separated into two completely isolated cavitys, owing to achieving the discharge of other gases such as extraction and the oxygen of pure hydrogen.
For achieving the above object, this utility model provides a kind of cavity-separating hydrogen-oxygen separation electrolysis unit,.
The beneficial effects of the utility model are: compared with prior art, and the cavity-separating hydrogen-oxygen separation electrolysis unit that this utility model provides, including electrolysis bath, ion exchange membrane, control circuit plate and lithium battery；The edge seal of described ion exchange membrane is fixed on the inwall of electrolysis bath and the distribution of inclined shape, electrolysis bath is formed for containing the first sealing cavity carrying out electrolysis water and for containing the second sealing cavity of drinkable water after being separated by ion exchange membrane, described first annular seal space body is positioned at the lower section of ion exchange membrane, and described second annular seal space body is positioned at the top of ion exchange membrane；Described control circuit plate and lithium battery are each attached in the bottom of electrolysis bath, and lithium battery electrically connects with control circuit plate；
It is fixed with, in described first annular seal space body, the positive electrode plate paralleled with ion exchange membrane and be disposed below, being fixed with, in described second annular seal space body, the negative electrode plate paralleled with ion exchange membrane and be positioned above, described positive electrode plate and negative electrode plate all electrically connect with control circuit plate；The inclined shape of described ion exchange membrane is fixed on the inwall of electrolysis bath, and the medial wall of electrolysis bath is in an acute angle with positive electrode plate acclivitous one end shape；Electrolysis water forms a gas trigonum near between the horizontal plane and positive electrode plate and the medial wall of electrolysis bath of this acute angle.
Wherein, this device also includes a check valve, and outer water tube seals cavity by check valve and first and connects, and is added water in the first annular seal space body by check valve.
Wherein, the outer surface of described electrolysis bath is plated with an insulating barrier.
Wherein, the internal diameter of described electrolysis bath is about 9cm.
1) by this electrolysis bath being separated into after arranging ion exchange membrane in electrolysis bath two completely isolated sealing cavitys, and in the first annular seal space body, place positive electrode plate, in the second annular seal space body, place negative electrode plate, on negative electrode plate, produce hydrogen during electrolysis, positive electrode plate produces oxygen；Due to ion exchange membrane separate from, can completely by completely isolated to the hydrogen after electrolysis and oxygen, therefore the hydrogen in the second annular seal space body is pure hydrogen, and therefore the water in the second annular seal space body is capable of direct drinking；Pure hydrogen can also be discharged and collect, in order to follow-up use or coordinate other to use.Above-mentioned improvement, it is achieved that oxygen and other gas are kept completely separate with hydrogen, then achieve producing of pure hydrogen.
2) being fixed on the inwall of electrolysis bath by inclined for ion exchange membrane shape, the medial wall of electrolysis bath is in an acute angle with positive electrode plate acclivitous one end shape；Electrolysis water forms a gas trigonum near between the horizontal plane and positive electrode plate and the medial wall of electrolysis bath of this acute angle；The nitrogen existed in oxygen and electrolysis water after electrolysis is discharged after being all gathered in this gas trigonum；This gas trigonum, other gases such as this region, without being separately provided, is formed according to hemodialysis principle, the nitrogen originally existed in oxygen that electrolysis obtains and electrolysis water can be automatically moved into this gas trigonum, is then then exhausted from；This design, can not only discharge other gases such as oxygen, it is to avoid these gases cannot be discharged and return in water, and water is polluted timely；And, other gases such as oxygen can be driven in time, stop these gases completely and mix with hydrogen, it is ensured that the absolute purity of hydrogen.
3) feature such as this utility model has reasonable in design, simple operation, cost is low, making pure hydrogen is effective.
Accompanying drawing explanation
Fig. 1 is cavity-separating hydrogen-oxygen separation electrolysis unit structural representation of the present utility model.
Main element symbol description is as follows:
10, electrolysis bath 11, ion exchange membrane
12, control circuit plate 13, lithium battery
14, first cavity the 15, second sealing cavity is sealed
16, positive electrode plate 17, negative electrode plate
18, gas trigonum.
Detailed description of the invention
In order to more clearly state this utility model, below in conjunction with accompanying drawing, this utility model is further described.
Referring to Fig. 1, cavity-separating hydrogen-oxygen separation electrolysis unit of the present utility model, including electrolysis bath 10, ion exchange membrane 11, control circuit plate 12 and lithium battery 13；The edge seal of ion exchange membrane 11 is fixed on the inwall of electrolysis bath 10 and inclined distribution, electrolysis bath 10 passes through to be formed after ion exchange membrane 11 separates for containing the first sealing cavity 14 carrying out electrolysis water and for containing the second sealing cavity 15 of drinkable water, first seals cavity 14 is positioned off the lower section of proton exchange 11, and second seals cavity 15 is positioned off the top of proton exchange 11；Control circuit plate 12 and lithium battery 13 are each attached in the bottom of electrolysis bath 10, and lithium battery 13 electrically connects with control circuit plate 12；
It is fixed with, in first sealing cavity 14, the positive electrode plate 16 paralleled with ion exchange membrane 11 and be disposed below, it is fixed with the negative electrode plate 17 paralleled with ion exchange membrane 11 and be positioned above, positive electrode plate 16 and negative electrode plate 17 in second sealing cavity 15 all to electrically connect with control circuit plate 12；Control circuit plate 12 is energized after work the first electrolysis water sealed in cavity 14 to be carried out electrolysis, produces oxygen O after electrolysis on positive plate 162, negative electrode plate 17 produces hydrogen H2；By after the isolation of ion exchange membrane 11 produce hydrogen not with oxygen mix, formed pure hydrogen；
The inclined shape of ion exchange membrane 11 is fixed on the inwall of electrolysis bath 10, and the medial wall of electrolysis bath 10 is in an acute angle with positive electrode plate 16 acclivitous one end shape；Electrolysis water forms a gas trigonum 18 near between the horizontal plane and the medial wall of positive electrode plate 16 and electrolysis bath 10 of this acute angle；The nitrogen existed in oxygen and electrolysis water after electrolysis is discharged after being all gathered in this gas trigonum 18；By the formation of gas trigonum 18, the gas that can seal first in cavity 14 in time is discharged.
Compared to the situation of prior art, the cavity-separating hydrogen-oxygen separation electrolysis unit that this utility model provides, have the advantages that
1) by this electrolysis bath 10 being separated into after arranging ion exchange membrane 11 in electrolysis bath 10 two completely isolated sealing cavitys, and seal placement positive electrode plate 16 in cavity 14 first, seal second and in cavity 15, place negative electrode plate 17, on negative electrode plate 17, produce hydrogen during electrolysis, positive electrode plate 16 produces oxygen；Due to ion exchange membrane 11 separate from, can completely by completely isolated to the hydrogen after electrolysis and oxygen, therefore the hydrogen in the second annular seal space body is pure hydrogen, and therefore the water in the second annular seal space body is capable of direct drinking；Pure hydrogen can also be discharged and collect, in order to follow-up use or coordinate other to use.Above-mentioned improvement, it is achieved that oxygen and other gas are kept completely separate with hydrogen, then achieve producing of pure hydrogen.
2) being fixed on the inwall of electrolysis bath 10 by inclined for ion exchange membrane 11 shape, the medial wall of electrolysis bath 10 is in an acute angle with positive electrode plate 16 acclivitous one end shape；Electrolysis water forms a gas trigonum 18 near between the horizontal plane and positive electrode plate and the medial wall of electrolysis bath of this acute angle；The nitrogen existed in oxygen and electrolysis water after electrolysis is discharged after being all gathered in this gas trigonum；This gas trigonum 18, other gases such as this region, without being separately provided, is formed according to hemodialysis principle, the nitrogen originally existed in oxygen that electrolysis obtains and electrolysis water can be automatically moved into this gas trigonum, is then then exhausted from；This design, can not only discharge other gases such as oxygen, it is to avoid these gases cannot be discharged and return in water, and water is polluted timely；And, other gases such as oxygen can be driven in time, stop these gases completely and mix with hydrogen, it is ensured that the absolute purity of hydrogen.
3) feature such as this utility model has reasonable in design, simple operation, cost is low, making pure hydrogen is effective.
In the present embodiment, this device also includes a check valve (not shown), and outer water tube seals cavity 14 by check valve and first and connects, and is added water in the first sealing cavity 14 by check valve.This case is added water by check valve in the first annular seal space body and carries out electrolysis；If during the enough electrolysis of the water in the first annular seal space body, check valve can be closed；If the water in the first annular seal space body is inadequate, opens check valve and add water.After carrying out electrolysis due to the water in the first annular seal space body, the inside remnants have a lot of harmful gas or impurity, because can not be passed into by this water in the additional water pipe added water, thus to use the check valve of one-way flow, it is to avoid water refluxes.Certainly, this case is not limited to seal cavity by check valve to first and add water, it is also possible to be use other modes such as permeable membrane to add water；If the change to the mode of adding water, as long as ensureing that in the first annular seal space body, water does not have the embodiment of backflow phenomenon, belong to this case simple deformation or conversion, fall in the protection domain of this case.
In the present embodiment, the outer surface of electrolysis bath 10 is plated with an insulating barrier (not shown).Owing to needing to carry out passing through electrolysis in electrolysis bath, it is therefore desirable to its outer surface is insulated.
In the present embodiment, the internal diameter of electrolysis bath 10 is about 9cm.The design of electrolysis bath 10 internal diameter in this case, it is achieved that the water electrolysis in small size isolates hydrogen and oxygen；And divide chamber by ion exchange membrane, it is achieved that producing of pure hydrogen.
In this utility model, the water in the first annular seal space body is served only for electrolysis；Water in second annular seal space body can directly be drunk, it is also possible to directly collects at pure hydrogen, can be used for making the cosmetics such as facial film, be used for treating multiple disease, healthy to be beneficial to man.
The cavity-separating hydrogen-oxygen separation electrolysis unit that this utility model provides cleans and makes hydrogen peroxide or disinfectant function automatically, this device is set with automatic cleaning function, because water is after electrolysis except producing hydrogen and oxygen, also can produce the ion of other mineral because of the difference of water quality, after Reusability device, these mineral ions can be attached on battery lead plate and form usually said incrustation scale.The accumulation of incrustation scale can affect the efficiency of battery lead plate and then affect use effect of device.Just automatically clean once so apparatus system is set as often using five times.The way cleaned is by positive and negative electrode umpolung, originally produces to produce in the second annular seal space body of hydrogen oxygen, originally produces to produce in the first annular seal space body of oxygen hydrogen.On the one hand, the hydrogen of generation can will be attached to the material reduction on the battery lead plate of the first sealing cavity, thus cleaning electrode plate.On the other hand, producing the hydrogen peroxide with disinfective action in the second annular seal space body, hydrogen peroxide may be used for vegetables and fruits cleaning and sterilizing, table-ware disinfection etc..
Disclosed above being only several specific embodiment of the present utility model, but this utility model is not limited to this, the changes that any person skilled in the art can think of all should fall into protection domain of the present utility model.
Claims (4)
1. a cavity-separating hydrogen-oxygen separation electrolysis unit, it is characterised in that include electrolysis bath, ion exchange membrane, control circuit plate and lithium battery；The edge seal of described ion exchange membrane is fixed on the inwall of electrolysis bath and the distribution of inclined shape, electrolysis bath is formed for containing the first sealing cavity carrying out electrolysis water and for containing the second sealing cavity of drinkable water after being separated by ion exchange membrane, described first annular seal space body is positioned at the lower section of ion exchange membrane, and described second annular seal space body is positioned at the top of ion exchange membrane；Described control circuit plate and lithium battery are each attached in the bottom of electrolysis bath, and lithium battery electrically connects with control circuit plate；
It is fixed with, in described first annular seal space body, the positive electrode plate paralleled with ion exchange membrane and be disposed below, being fixed with, in described second annular seal space body, the negative electrode plate paralleled with ion exchange membrane and be positioned above, described positive electrode plate and negative electrode plate all electrically connect with control circuit plate；The inclined shape of described ion exchange membrane is fixed on the inwall of electrolysis bath, and the medial wall of electrolysis bath is in an acute angle with positive electrode plate acclivitous one end shape；Electrolysis water forms a gas trigonum near between the horizontal plane and positive electrode plate and the medial wall of electrolysis bath of this acute angle.
2. cavity-separating hydrogen-oxygen separation electrolysis unit according to claim 1, it is characterised in that this device also includes a check valve, outer water tube seals cavity by check valve and first and connects, and is added water in the first annular seal space body by check valve.
3. cavity-separating hydrogen-oxygen separation electrolysis unit according to claim 1, it is characterised in that the outer surface of described electrolysis bath is plated with an insulating barrier.
4. cavity-separating hydrogen-oxygen separation electrolysis unit according to claim 1, it is characterised in that the internal diameter of described electrolysis bath is about 9cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521102919.8U CN205368508U (en) | 2015-12-28 | 2015-12-28 | Divide cavate hydrogen oxygen partial pressure from electrolytic device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521102919.8U CN205368508U (en) | 2015-12-28 | 2015-12-28 | Divide cavate hydrogen oxygen partial pressure from electrolytic device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205368508U true CN205368508U (en) | 2016-07-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521102919.8U Withdrawn - After Issue CN205368508U (en) | 2015-12-28 | 2015-12-28 | Divide cavate hydrogen oxygen partial pressure from electrolytic device |
Country Status (1)
| Country | Link |
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| CN (1) | CN205368508U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105441972A (en) * | 2015-12-28 | 2016-03-30 | 深圳市赫拉铂氢时代科技有限公司 | Separated cavity type hydrogen and oxygen separating electrolyser and method thereof |
-
2015
- 2015-12-28 CN CN201521102919.8U patent/CN205368508U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105441972A (en) * | 2015-12-28 | 2016-03-30 | 深圳市赫拉铂氢时代科技有限公司 | Separated cavity type hydrogen and oxygen separating electrolyser and method thereof |
| CN105441972B (en) * | 2015-12-28 | 2018-08-10 | 深圳市赫拉铂氢时代科技有限公司 | Cavity-separating hydrogen-oxygen detaches electrolysis unit and its method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160706 Effective date of abandoning: 20180810 |