CN202881402U - Floor type air cooling oxy-hydrogen electrolytic cell - Google Patents
Floor type air cooling oxy-hydrogen electrolytic cell Download PDFInfo
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- CN202881402U CN202881402U CN2012205350883U CN201220535088U CN202881402U CN 202881402 U CN202881402 U CN 202881402U CN 2012205350883 U CN2012205350883 U CN 2012205350883U CN 201220535088 U CN201220535088 U CN 201220535088U CN 202881402 U CN202881402 U CN 202881402U
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- ventilation
- tank
- cooled
- air
- electrolytic cell
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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
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model relates to an electrolytic cell, and in particular relates to a floor type air cooling oxy-hydrogen electrolytic cell. The floor type air cooling oxy-hydrogen electrolytic cell comprises an electrolytic cell body formed by a plurality of groups of electrolytic chambers combined in series, wherein the electrolytic cell body is uniformly provided with a plurality of floor type multi-layer ventilation and heat dissipation tanks in the horizontal direction; a group of electrolytic chambers are arranged between the adjacent ventilation and heat dissipation tanks; and the electrolytic chambers are provided with electrode plate groups that are cooled by the ventilation and heat dissipation tanks. The floor type air cooling oxy-hydrogen electrolytic cell disclosed by the utility model adopts a plurality of floor type multi-layer ventilation and heat dissipation tanks to cool the electrolytic chambers of the electrolytic cell body by means of air cooling, the external cooling air can simultaneously enter the multi-layer structure of the ventilation and heat dissipation tanks to have full and uniform contact with the electrode plates of the electrolytic chambers so as to take away the heat of the electrolytic chambers, and by the way of air cooling, the floor type air cooling oxy-hydrogen electrolytic cell has low energy consumption, is rarely influenced by external temperature and environment, and is very convenient and effective to use.
Description
Technical field
The utility model relates to a kind of electrolyzer, particularly the air-cooled oxyhydrogen electrolytic tank of a kind of building formula.
Background technology
Oxyhydrogen machine adopts the brine electrolysis technology, and hydrogen or oxygen gas is extracted in energising from water, and wherein hydrogen acts as a fuel, it is combustion-supporting that oxygen is used for, can replaced acetylene, the carbonaceous gass such as coal gas, liquefied gas, and have calorific value height, flame and concentrate, zero pollute, production efficiency is high, the advantages such as energy-saving convenient.The process that oxyhydrogen machine produces gas all is to carry out in electrolyzer, and the battery lead plate in the electrolyzer is switched on for a long time and can be generated a large amount of heats, if its cooling has not just been had a strong impact on output and the production efficiency of gas.At present, the radiating mode that the electrolyzer that uses on the large-scale oxyhydrogen machine is commonly used mainly is by water-cooled, although radiating effect is obvious, but owing to associated problem such as replenishing of the control that will consider water circulation use, water temperature and water coolant, the equipment of water-cooled not only needs to take a large amount of spaces, also brings higher energy consumption, and in the low meeting of some temperature icing area occurs, water-cooled has certain limitation, therefore uses inconvenience.
The utility model content
In order to overcome above-mentioned technical problem, the purpose of this utility model is to provide a kind of formula air-cooled oxyhydrogen electrolytic tank in building air-cooled and can efficiently radiates heat that adopts.
The technical scheme that the utility model adopts is:
The air-cooled oxyhydrogen electrolytic tank of a kind of building formula, comprise the electrolyzer body that is formed by many groups tank room series combination, described electrolyzer body laterally evenly arranges the ventilation and heat groove of some buildings formula multilayer at it, one group of tank room is set between the adjacent ventilation and heat groove, and described tank room is provided with the electrode plate groups by the heat radiation of ventilation and heat groove.
As further improvement in the technical proposal, described each ventilation and heat groove comprises a plurality of ventilation slots that are laminated from the bottom to top.
As further improvement in the technical proposal, described electrode plate groups comprises at least two electrode plate, and described battery lead plate surrounds at least one sub-tank room with tank room, and the battery lead plate at described tank room two ends consists of the cell wall of ventilation and heat groove.
As further improvement in the technical proposal, be provided with barrier film in the described sub-tank room, described barrier film is divided into anolyte compartment and cathode compartment with sub-tank room, and the top of described barrier film is provided with the hydrogen outlet that is communicated with cathode compartment and the oxygen outlet that is communicated with the anolyte compartment.
As further improvement in the technical proposal, described each hydrogen outlet is connected to the hydrogen general export of electrolyzer body by pipeline, and described each oxygen outlet is connected to the oxygen general export of electrolyzer body by pipeline.
As further improvement in the technical proposal, described barrier film is provided with the first water-in that is communicated with cathode compartment and the second water-in that is communicated with the anolyte compartment.
As further improvement in the technical proposal, described the first water-in and the second water-in be the position on the lower at the middle part of barrier film both sides respectively.
As further improvement in the technical proposal, described every group of electrode plate groups comprises 4 electrode plate, and described battery lead plate is divided into three sub-tank rooms with the tank room component.
The beneficial effects of the utility model are: the utility model adopts the ventilation and heat groove of some buildings formula multilayer to dispel the heat by the tank room of air-cooled form to the electrolyzer body, extraneous cooling air can enter the multilayered structure of ventilation and heat groove simultaneously, with the electrode plate groups of tank room fully, take away the heat of tank room after the uniform contact, owing to adopted air-cooled form, its energy consumption is lower, and be subjected to the impact of external temperature environment less, very easy to use, effective.
Description of drawings
Below in conjunction with drawings and embodiments the utility model is further specified.
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the synoptic diagram of the utility model barrier film.
Embodiment
Formula air-cooled oxyhydrogen electrolytic tank in a kind of building comprises the electrolyzer body 1 that is formed at horizontal series combination by many groups tank room, and electrolyzer body 1 is at its horizontal even, equally spaced ventilation and heat groove 2 that some buildings formula multilayer is set.One group of tank room is set between the adjacent ventilation and heat groove 2, and tank room is provided with the electrode plate groups by 2 heat radiations of ventilation and heat groove, and electrode plate groups is communicated with power supply and produces hydrogen and oxygen in order to brine electrolysis.
As further preferred embodiment, each ventilation and heat groove 2 comprises a plurality of ventilation slots 21 that are laminated from the bottom to top, the cross section of these ventilation slots 21 is the rectangle of congruence, the front and back end of running through electrolyzer body 1, extraneous cooling air enters a plurality of ventilation slots 21 from front end, take away the heat that electrode plate groups produces after, flow away from the rear end, because the air output of each ventilation slot 21 is identical with intake velocity, so its heat radiation evenly, fully.
As further preferred embodiment, electrode plate groups comprises 3, positive poles that connect power supply of at least two electrode plate, and another piece connects negative pole.Battery lead plate 3 surrounds at least one sub-tank room 4 with tank room.The battery lead plate 3 at tank room two ends consists of the cell wall of ventilation and heat grooves 2, thereby so tank room at the battery lead plate 3 and cooling air heat exchange heat radiation at two ends.
As further preferred embodiment, as shown in Figure 2, in every sub-tank room 4 barrier film 5 is installed, barrier film 5 is the ion permeable membrane that can only see through ion, sub-tank room 4 is divided into anolyte compartment and cathode compartment, water generates oxygen in anolyte compartment's electrolysis, generates hydrogen in the cathode compartment electrolysis, and the top of barrier film 5 is provided with the hydrogen outlet 51 that is communicated with cathode compartment and the oxygen outlet 52 that is communicated with the anolyte compartment.
As further preferred embodiment, each hydrogen outlet 51 is connected to the hydrogen general export of electrolyzer body 1 by pipeline, and each oxygen outlet 52 is connected to the oxygen general export of electrolyzer body 1 by pipeline.
As further preferred embodiment, barrier film 5 is provided with the first water-in 53 that is communicated with cathode compartment and the second water-in 54 that is communicated with the anolyte compartment.The moisturizing of sub-tank room 4 mainly is to enter from these two water-ins.
As further preferred embodiment, the first water-in 53 and the second water-in 54 be the position on the lower at the middle part of barrier film 5 both sides respectively, and symmetrical.So, prevented because the obstruction of two water-ins that cause is stopped up in sub-tank room 4 bottoms.
As further preferred embodiment, every group of electrode plate groups comprises 4 electrode plate 3, a side positively charged of every electrode plate 3, and opposite side is electronegative, and battery lead plate 3 is divided into three sub-tank rooms 4 with the tank room component.
The above be the utility model preferred embodiment, it does not consist of the restriction to the utility model protection domain.
Claims (8)
1. air-cooled oxyhydrogen electrolytic tank of building formula, it is characterized in that: comprise the electrolyzer body (1) that is formed by many groups tank room series combination, described electrolyzer body (1) laterally evenly arranges the ventilation and heat groove (2) of some buildings formula multilayer at it, between the adjacent ventilation and heat groove (2) one group of tank room is set, described tank room is provided with the electrode plate groups by ventilation and heat groove (2) heat radiation.
2. the air-cooled oxyhydrogen electrolytic tank of building formula according to claim 1, it is characterized in that: described each ventilation and heat groove (2) comprises a plurality of ventilation slots (21) that are laminated from the bottom to top.
3. the air-cooled oxyhydrogen electrolytic tank of building formula according to claim 1 and 2, it is characterized in that: described electrode plate groups comprises at least two electrode plate (3), described battery lead plate (3) surrounds at least one sub-tank room (4) with tank room, and the battery lead plate (3) at described tank room two ends consists of the cell wall of ventilation and heat groove (2).
4. the air-cooled oxyhydrogen electrolytic tank of building formula according to claim 3, it is characterized in that: be provided with barrier film (5) in the described sub-tank room (4), described barrier film (5) is divided into anolyte compartment and cathode compartment with sub-tank room (4), and the top of described barrier film (5) is provided with the hydrogen outlet (51) that is communicated with cathode compartment and the oxygen outlet (52) that is communicated with the anolyte compartment.
5. the air-cooled oxyhydrogen electrolytic tank of building formula according to claim 4, it is characterized in that: described each hydrogen outlet (51) is connected to the hydrogen general export of electrolyzer body (1) by pipeline, and described each oxygen outlet (52) is connected to the oxygen general export of electrolyzer body (1) by pipeline.
6. it is characterized in that according to claim 4 or the air-cooled oxyhydrogen electrolytic tank of 5 described building formulas: described barrier film (5) is provided with the first water-in (53) of being communicated with cathode compartment and second water-in (54) of connection anolyte compartment.
7. the air-cooled oxyhydrogen electrolytic tank of building formula according to claim 6 is characterized in that: described the first water-in (53) and the second water-in (54) be the position on the lower at the middle part of barrier film (5) both sides respectively.
8. the air-cooled oxyhydrogen electrolytic tank of building formula according to claim 3, it is characterized in that: described every group of electrode plate groups comprises 4 electrode plate (3), described battery lead plate (3) is divided into three sub-tank rooms (4) with the tank room component.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012205350883U CN202881402U (en) | 2012-10-18 | 2012-10-18 | Floor type air cooling oxy-hydrogen electrolytic cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012205350883U CN202881402U (en) | 2012-10-18 | 2012-10-18 | Floor type air cooling oxy-hydrogen electrolytic cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202881402U true CN202881402U (en) | 2013-04-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012205350883U Expired - Fee Related CN202881402U (en) | 2012-10-18 | 2012-10-18 | Floor type air cooling oxy-hydrogen electrolytic cell |
Country Status (1)
| Country | Link |
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| CN (1) | CN202881402U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110952109A (en) * | 2019-12-17 | 2020-04-03 | 西安优耐特容器制造有限公司 | Multi-stage electrolytic tank |
| CN113195789A (en) * | 2018-12-20 | 2021-07-30 | 海默斯有限公司 | Rack-mounted box for heating equipment |
-
2012
- 2012-10-18 CN CN2012205350883U patent/CN202881402U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113195789A (en) * | 2018-12-20 | 2021-07-30 | 海默斯有限公司 | Rack-mounted box for heating equipment |
| CN110952109A (en) * | 2019-12-17 | 2020-04-03 | 西安优耐特容器制造有限公司 | Multi-stage electrolytic tank |
| CN110952109B (en) * | 2019-12-17 | 2021-08-13 | 西安优耐特容器制造有限公司 | Multi-stage electrolytic tank |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130417 Termination date: 20151018 |
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| EXPY | Termination of patent right or utility model |