CN201850311U - Self aspiration type electric chemical pure oxygen generation assembly - Google Patents
Self aspiration type electric chemical pure oxygen generation assembly Download PDFInfo
- Publication number
- CN201850311U CN201850311U CN2010205560543U CN201020556054U CN201850311U CN 201850311 U CN201850311 U CN 201850311U CN 2010205560543 U CN2010205560543 U CN 2010205560543U CN 201020556054 U CN201020556054 U CN 201020556054U CN 201850311 U CN201850311 U CN 201850311U
- Authority
- CN
- China
- Prior art keywords
- end plate
- oxygen
- diffusion layer
- gas diffusion
- anode
- 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.)
- Expired - Lifetime
Links
Images
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model provides a self aspiration type electric chemical pure oxygen generation assembly, which has the advantages that the structure is simple, the oxygen preparation process is simple, no pollution exists in the oxygen preparation process, and the prepared oxygen has high purity. The utility model is characterized in that the self aspiration type electric chemical pure oxygen generation assembly comprises a membrane electrode assembly, wherein the membrane electrode assembly comprises an anode gas diffusion layer, an anode catalyzing layer, a proton exchange membrane, a cathode catalyzing layer and a cathode gas diffusion layer, the proton exchange membrane comprises a center part and a peripheral outwards exposed part, a porous gas end plate, a cathode sealing frame sheet, the peripheral outwards exposed part of the proton exchange membrane, an anode sealing frame sheet and an oxygen end plate are sequentially and fixedly connected, the right center of the porous gas end plate is uniformly distributed with small holes, the small holes are right aligned with the cathode gas diffusion layer, the cathode gas diffusion layer is communicated with a negative electrode of an external direct current power supply, an oxygen through hole is arranged in the middle of the oxygen end plate and is communicated with an oxygen output pipe, and the anode gas diffusion layer is communicated with a positive electrode of the external direct current power supply.
Description
Technical field
The utility model relates to the technical field that electrochemistry is made pure oxygen, is specially a kind of self-respiration type electrochemistry pure oxygen generating assembly.
Background technology
The producing apparatus of existing electrochemistry pure oxygen, all need be at electrolyzer or/and make in the environment of electrolytic solution, its complex structure, to make oxygen process loaded down with trivial details, and make in the oxygen process easily pollute, the purity of oxygen is not up to standard.
Summary of the invention
At the problems referred to above, the utility model provides a kind of self-respiration type electrochemistry pure oxygen generating assembly, and it is simple in structure, the manufacturing oxygen process is simple, and is pollution-free in the process of manufacturing oxygen, and the oxygen high purity that produces.
A kind of self-respiration type electrochemistry pure oxygen generating assembly, its technical scheme is such:
It is characterized in that: it comprises membrane electrode assembly, described membrane electrode assembly comprises anode gas diffusion layer, anode catalyst layer, proton exchange membrane, cathode catalysis layer, cathode gas diffusion layer, described proton exchange membrane comprises centre portions and exposed parts all around, the porous gas end plate, negative electrode sealing frame sheet, exposed parts around the described proton exchange membrane, anode seal frame sheet, the oxygen end plate is fastenedly connected successively, the center of described porous gas end plate is evenly equipped with aperture, described aperture faces described cathode gas diffusion layer, described cathode gas diffusion layer is communicated with the external dc power negative pole, described oxygen end plate middle part has the oxygen through hole, described oxygen through hole is communicated with oxygen output tube, and described anode gas diffusion layer is communicated with the external dc power positive pole.
It is further characterized in that: described porous gas end plate is an electro-conductive material when constituting, directly the fits internal surface of described porous gas end plate of described cathode gas diffusion layer, outside the described porous gas end plate by lead connection external dc power negative pole;
When described porous gas end plate is non-conducting material, in the middle cathode cavity that described cathode gas diffusion layer, negative electrode sealing frame sheet, porous gas end plate three surround the negative electrode current collection layer is housed, described cathode gas diffusion layer connects the negative electrode current collection layer, described negative electrode current collection layer forms spirrillum or netted for the conducting metal filament winding, described porous gas end plate is passed in its outer end, connects the external dc power negative pole;
Described oxygen end plate is an electro-conductive material when constituting, the fit internal surface of described oxygen end plate of described anode gas diffusion layer, and the described oxygen end plate outside connects the external dc power positive pole by lead;
When described oxygen end plate is non-conducting material, in the grading electrode cavity that described anode gas diffusion layer, anode seal frame sheet, oxygen end plate three surround the anode current collection layer is housed, described anode gas diffusion layer connects described anode current collection layer, described anode current collection layer forms spirrillum or netted for the conducting metal filament winding, wire hole, the connection external dc power positive pole of described oxygen end plate passed in its outer end, and the gap between described anode current collection layer and wire hole is filled with seal gum;
Screw is anchored on described oxygen end plate after passing exposed parts, the anode seal frame sheet all around of porous gas end plate, negative electrode sealing frame sheet, proton exchange membrane successively;
Described proton exchange membrane is specially the hydrogen ion exchange membrane.
After adopting structure of the present utility model, the voltage difference of external direct supply is during greater than 0.65 V and less than 1.45V, air is via the aperture of porous air end plate, the mode that cathode gas diffusion layer transmits by diffusion is drawn onto cathode catalysis layer, electronics is via the cathode side current collection layer, cathode gas diffusion layer, enter cathode catalysis layer, afterwards at anode gas diffusion layer, anode catalyst layer, proton exchange membrane, cathode catalysis layer, the acting in conjunction of cathode gas diffusion layer generates oxygen down, oxygen is exported from oxygen output tube, and it is simple in structure, the process of making oxygen is simple; Be packaged in inside owing to make the whole membrane electrode assembly of oxygen, the pure oxygen of generation can only be exported from oxygen output tube, the oxygen high purity that produces; Adopt membrane electrode assembly to make oxygen, pollution-free in the process of its manufacturing oxygen.
Description of drawings
Fig. 1 is the three-dimensional mounting structure synoptic diagram of specific embodiment of the utility model one;
Fig. 2 is the three-dimensional mounting structure synoptic diagram of specific embodiment of the utility model two;
Fig. 3 is the structural representation enlarged view of membrane electrode assembly in the utility model.
Embodiment
Specific embodiment one: see Fig. 1, Fig. 3, it comprises membrane electrode assembly 1, membrane electrode assembly 1 comprises anode gas diffusion layer 9, anode catalyst layer 10, proton exchange membrane 11, cathode catalysis layer 12, cathode gas diffusion layer 13, proton exchange membrane 11 comprises centre portions and exposed parts 14 all around, screw 7 passes porous gas end plate 5 successively, negative electrode sealing frame sheet 4, exposed parts 14 around the proton exchange membrane, behind the anode seal frame sheet 15, be anchored on oxygen end plate 6, porous gas end plate 5 is a non-conducting material, cathode gas diffusion layer 13, negative electrode sealing frame sheet 4, cathode cavity in the middle of being surrounded by between porous gas end plate 5 threes, in the middle cathode cavity negative electrode current collection layer 3 is housed, cathode gas diffusion layer 13 connects negative electrode current collection layer 3, negative electrode current collection layer 3 forms spirrillum or netted for the conducting metal filament winding, its wire can be platinum filament, spun gold, filamentary silver, the platinum plating silk, gold-plated silk, silver-plated silk, porous gas end plate 5 is passed in negative electrode current collection layer 3 outer ends, the negative pole that connects external dc power 16, the center of porous gas end plate 5 is evenly equipped with aperture 17, aperture 17 faces cathode gas diffusion layer 13, oxygen end plate 6 is a non-conducting material, anode gas diffusion layer 9, anode seal frame sheet 15, oxygen end plate 6 threes are surrounded by the grading electrode cavity, anode current collection layer 2 is housed in the grading electrode cavity, anode gas diffusion layer 9 connects anode current collection layer 2, anode current collection layer 2 forms spirrillum or netted for the conducting metal filament winding, its wire can be platinum filament, spun gold, filamentary silver, the platinum plating silk, gold-plated silk, silver-plated silk, the wire hole 18 of oxygen end plate 6 is passed in anode current collection layer 2 outer ends, connect the positive pole of external dc power 16, the gap that anode current collection layer 2 and wire hole are 18 is filled with seal gum and (belongs to existing mature technology, do not draw among the figure); Oxygen end plate 6 middle parts have oxygen through hole 19, and oxygen through hole 19 is communicated with oxygen output tube 8, and proton exchange membrane 11 is specially the hydrogen ion exchange membrane.
Specific embodiment two: see Fig. 2, Fig. 3, it comprises membrane electrode assembly 1, membrane electrode assembly 1 comprises anode gas diffusion layer 9, anode catalyst layer 10, proton exchange membrane 11, cathode catalysis layer 12, cathode gas diffusion layer 13, proton exchange membrane 11 comprises centre portions and exposed parts 14 all around, screw 7 passes porous gas end plate 5 successively, negative electrode sealing frame sheet 4, exposed parts 14 around the proton exchange membrane, behind the anode seal frame sheet 15, be anchored on oxygen end plate 6, the center of porous gas end plate 5 is evenly equipped with aperture 17, aperture 17 faces cathode gas diffusion layer 13, porous gas end plate 5 constitutes for electro-conductive material, electro-conductive material can be a graphite cake, the platinum plate, the gold plate, silver plate, the platinum plating plate, coated plate, silver-plated plate, the internal surface of cathode gas diffusion layer 13 direct applying porous gas end plates 5, porous gas end plate 5 outsides connect the negative pole of external dc power 16 by lead 20, oxygen end plate 6 constitutes for electro-conductive material, electro-conductive material can be a graphite cake, the platinum plate, the gold plate, silver plate, the platinum plating plate, coated plate, silver-plated plate, the internal surface of anode gas diffusion layer 9 applying oxygen end plates 6, oxygen end plate 6 outsides connect the positive pole of external dc power 16 by lead 21, oxygen end plate 6 middle parts have oxygen through hole 19, oxygen through hole 19 is communicated with oxygen output tube 8, and proton exchange membrane 11 is specially the hydrogen ion exchange membrane.
Its principle is as follows: external direct current power supply 16 voltage differences are during greater than 0.65V and less than 1.45V, there is oxygen to produce, at this moment, air is drawn onto in the cathode catalysis layer 12 via the aperture 17 of porous air end plate 5, the mode that cathode gas diffusion layer 13 transmits by diffusion, electronics enters cathode catalysis layer 12 after being conducted to cathode gas diffusion layer 13, following electrochemical reaction takes place in airborne oxygen and electronics and the hydrogen ion that comes via proton exchange membrane 11 transmission in cathode catalysis layer 12, and generation water, that is cathodic reaction: O
2+ 4H
++ 4e
-à 2H
2O.
The water that generates relies on concentration diffusion mode to be passed in the anode catalyst layer 10 by proton exchange membrane 11 and is broken down into oxygen, electronics and hydrogen ion, and following electrochemical reaction: 2H promptly takes place
2O à O
2+ 4H
++ 4e
-, pure oxygen is concentrated thus and forms; Under the effect of hydrogen ion at electrical forces of 10 li generations of anode catalyst layer, be delivered to cathode catalysis layer 12 by proton exchange membrane 11; Electronics in 10 li generations of anode catalyst layer is drawn via anode gas diffusion layer 9, and finally turns back in the cathode catalysis layer 12; The concentrated pure oxygen that forms is released from oxygen bleed line 8 at last via the oxygen through hole 19 of anode gas diffusion layer 9, oxygen end plate 6.
Negative electrode sealing frame sheet 4 place proton exchange membrane around between exposed parts 14 and the porous air end plate 5, anode seal frame sheet 15 place proton exchange membrane around between exposed parts 14 and the oxygen end plate 6, under the preliminary tension effect of screw 7, form seamless trim, its effect is that the pure oxygen that guarantees all generations can only enter oxygen through hole 19, and can not let out from other place; Prevented also that simultaneously the gas in the environment from bleeding in the anode region of self-respiration type electrochemistry pure oxygen generating assembly.
Claims (7)
1. self-respiration type electrochemistry pure oxygen generating assembly, it is characterized in that: it comprises membrane electrode assembly, described membrane electrode assembly comprises anode gas diffusion layer, anode catalyst layer, proton exchange membrane, cathode catalysis layer, cathode gas diffusion layer, described proton exchange membrane comprises centre portions and exposed parts all around, the porous gas end plate, negative electrode sealing frame sheet, exposed parts around the described proton exchange membrane, anode seal frame sheet, the oxygen end plate is fastenedly connected successively, the center of described porous gas end plate is evenly equipped with aperture, described aperture faces described cathode gas diffusion layer, described cathode gas diffusion layer is communicated with the external dc power negative pole, described oxygen end plate middle part has the oxygen through hole, described oxygen through hole is communicated with oxygen output tube, and described anode gas diffusion layer is communicated with the external dc power positive pole.
2. a kind of self-respiration type electrochemistry pure oxygen generating assembly according to claim 1, it is characterized in that: when described porous gas end plate is the electro-conductive material formation, directly the fit internal surface of described porous gas end plate of described cathode gas diffusion layer, the described porous gas end plate outside connects the external dc power negative pole by lead.
3. a kind of self-respiration type electrochemistry pure oxygen generating assembly according to claim 1, it is characterized in that: when described porous gas end plate is non-conducting material, in the middle cathode cavity that described cathode gas diffusion layer, negative electrode sealing frame sheet, porous gas end plate three surround the negative electrode current collection layer is housed, described cathode gas diffusion layer connects the negative electrode current collection layer, described negative electrode current collection layer forms spirrillum or netted for the conducting metal filament winding, described porous gas end plate is passed in its outer end, connects the external dc power negative pole.
4. a kind of self-respiration type electrochemistry pure oxygen generating assembly according to claim 1, it is characterized in that: when described oxygen end plate is the electro-conductive material formation, the fit internal surface of described oxygen end plate of described anode gas diffusion layer, the described oxygen end plate outside connects the external dc power positive pole by lead.
5. a kind of self-respiration type electrochemistry pure oxygen generating assembly according to claim 1, it is characterized in that: when described oxygen end plate is non-conducting material, described anode gas diffusion layer, anode seal frame sheet, in the grading electrode cavity that oxygen end plate three surrounds the anode current collection layer is housed, described anode gas diffusion layer connects described anode current collection layer, described anode current collection layer forms spirrillum or netted for the conducting metal filament winding, the wire hole of described oxygen end plate is passed in its outer end, connect the external dc power positive pole, the gap between described anode current collection layer and wire hole is filled with seal gum.
6. a kind of self-respiration type electrochemistry pure oxygen generating assembly according to claim 1, it is characterized in that: screw is anchored on described oxygen end plate after passing exposed parts, the anode seal frame sheet all around of porous gas end plate, negative electrode sealing frame sheet, proton exchange membrane successively.
7. a kind of self-respiration type electrochemistry pure oxygen generating assembly according to claim 1, it is characterized in that: described proton exchange membrane is specially the hydrogen ion exchange membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205560543U CN201850311U (en) | 2010-10-11 | 2010-10-11 | Self aspiration type electric chemical pure oxygen generation assembly |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205560543U CN201850311U (en) | 2010-10-11 | 2010-10-11 | Self aspiration type electric chemical pure oxygen generation assembly |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201850311U true CN201850311U (en) | 2011-06-01 |
Family
ID=44092711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205560543U Expired - Lifetime CN201850311U (en) | 2010-10-11 | 2010-10-11 | Self aspiration type electric chemical pure oxygen generation assembly |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201850311U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101967650A (en) * | 2010-10-11 | 2011-02-09 | 无锡国赢科技有限公司 | Self-breathing electrochemical pure oxygen generation assembly |
| CN102330107A (en) * | 2011-09-06 | 2012-01-25 | 无锡国赢科技有限公司 | Self-breathing electrochemical pure oxygen generating module packaged by using binder |
| WO2012065524A1 (en) * | 2010-11-15 | 2012-05-24 | 无锡国赢科技有限公司 | Air-breathing electrochemical oxygen generator |
| CN113026042A (en) * | 2021-03-01 | 2021-06-25 | 南京理工大学 | Micro electrochemical reactor based on micro-fluidic technology |
-
2010
- 2010-10-11 CN CN2010205560543U patent/CN201850311U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101967650A (en) * | 2010-10-11 | 2011-02-09 | 无锡国赢科技有限公司 | Self-breathing electrochemical pure oxygen generation assembly |
| WO2012065524A1 (en) * | 2010-11-15 | 2012-05-24 | 无锡国赢科技有限公司 | Air-breathing electrochemical oxygen generator |
| CN102330107A (en) * | 2011-09-06 | 2012-01-25 | 无锡国赢科技有限公司 | Self-breathing electrochemical pure oxygen generating module packaged by using binder |
| CN102330107B (en) * | 2011-09-06 | 2014-03-19 | 无锡国赢科技有限公司 | Self-breathing electrochemical pure oxygen generating module packaged by using binder |
| CN113026042A (en) * | 2021-03-01 | 2021-06-25 | 南京理工大学 | Micro electrochemical reactor based on micro-fluidic technology |
| CN113026042B (en) * | 2021-03-01 | 2021-12-03 | 南京理工大学 | Micro electrochemical reactor based on micro-fluidic technology |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101967650B (en) | Self-breathing electrochemical pure oxygen generation assembly | |
| CN201850311U (en) | Self aspiration type electric chemical pure oxygen generation assembly | |
| JP2011514634A5 (en) | ||
| CN201864781U (en) | Self breathing type electrochemical oxygen generator | |
| CN101967651B (en) | Self-breathing electrochemical oxygen generator | |
| JP6948393B2 (en) | Microelectrode fiber optics, optical cables, and hydrogen production equipment for hydrogen production by opto-electrical water splitting | |
| CN111534830B (en) | Device and method for producing high-purity hydrogen by electrolyzing water | |
| CN108258267A (en) | A kind of acid cathode-alkali anode low temperature alcohol fuel battery | |
| CN217628644U (en) | Three-electrode system-based electrolytic tank for two-step method water electrolysis hydrogen production | |
| CN203159721U (en) | Self-breathing type electrochemical oxygen generation system | |
| CN201956423U (en) | Spraying heating vacuum sucker for membrane electrodes of proton exchange membrane fuel cells | |
| CN110034319A (en) | A kind of zinc-water fuel cell and its application in power generation production hydrogen | |
| CN114457351A (en) | Method and device for producing hydrogen by electrolyzing water step by step based on single-electrolytic-tank double-electrode two-step method | |
| CN109975706A (en) | A kind of test method in oxygen reduction cathode service life | |
| CN103840184A (en) | Single-cell activation method for direct borohydride fuel cell | |
| CN209210940U (en) | A kind of electrolytic chamber | |
| CN103173781B (en) | A kind of self-respiration type electro-chemistry oxygen-producing system | |
| CN104953132A (en) | Liquid flow-type alcohol-hydrogen peroxide fuel cell and manufacturing method thereof | |
| CN219861610U (en) | Anode end plate based on PEM water electrolysis tank | |
| CN104084225B (en) | Phosphorus doping Graphene hydrogen-peroxide reduction catalyst and preparation method without metal | |
| CN220952094U (en) | Polar plate runner device and corresponding polar plate of alkaline water electrolysis bath | |
| CN114755282B (en) | Novel membrane electrode test device of pure water electrolysis catalyst | |
| CN215418236U (en) | Air battery anode | |
| CN216237301U (en) | Efficient proton exchange membrane electrolytic cell | |
| CN214458365U (en) | Electrolytic tank device for preparing sodium borohydride by direct current electrolytic method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110601 Effective date of abandoning: 20120222 |