CN201738010U - Cyclic electrolysis device - Google Patents
Cyclic electrolysis device Download PDFInfo
- Publication number
- CN201738010U CN201738010U CN2010202161467U CN201020216146U CN201738010U CN 201738010 U CN201738010 U CN 201738010U CN 2010202161467 U CN2010202161467 U CN 2010202161467U CN 201020216146 U CN201020216146 U CN 201020216146U CN 201738010 U CN201738010 U CN 201738010U
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- electrolyzer
- electrolysis device
- circulation
- cyclic electrolysis
- circulation line
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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 relates to a cyclic electrolysis device, which comprises an electrolysis unit, a circulation unit and a cooling unit. The electrolysis unit comprises an electrolytic cell, a plurality of electrode plates and a power supply, wherein an electrolyte is contained in the electrolytic cell. The circulation unit comprises a circulation pipeline, a temporary storage barrel, a liquid storage barrel and a return pipeline, wherein the temporary storage barrel is connected with the circulation pipeline, the liquid storage barrel is used for containing the electrolyte and is commutated with the temporary storage barrel, and the return pipeline is connected with the liquid storage barrel and the electrolytic cell. The cooling unit comprises a radiating fan arranged relative to the circulation pipeline. The liquid level of the electrolyte is close to the circulation pipeline, so that the electrolyte and the generated oxyhydrogen gas can be together cooled through the circulation pipeline, the temporary storage barrel, the liquid storage barrel and the return pipeline and then reflow into the electrolytic cell, thereby not only the power consumption is low, but also the temperature generated by electrolysis operation can be simultaneously lowered.
Description
Technical field
The utility model relates to a kind of electrolyzer, particularly relates to a kind of cyclic electrolysis device.
Background technology
After the Industrial Revolution, the natural resource of the earth such as oil, colliery, Sweet natural gas etc. are continued and exploitation in large quantities, until in recent years, countries in the world just come to realise limited earth resources can't not had and end most exploitation, and then look for clean substitute energy energetically, wherein, oxyhydrogen is a kind of gas that can burn and replace Sweet natural gas.
Oxyhydrogen is a kind of mixed gas with hydrogen and oxygen, and general oxyhydrogen is produced by electrolytic effect mostly.Consult Fig. 1, prior oxyhydrogen fuel-generating apparatus 100, having an electrolyzer 102 that is loaded with brine electrolysis 101, multi-disc compartment of terrain links to each other and is arranged in this electrolyzer 102 and is immersed in battery lead plate 103 in the brine electrolysis 101, and the power supply source 104 of the described battery lead plate 103 of an electrical connection, when described battery lead plate 103 is subjected to the driving of this power supply source 104 and conducts electricity, the electrolysis of promptly can switching on of this brine electrolysis 101, and then produce oxyhydrogen, with the use that acts as a fuel.
But, brine electrolysis 101 energising electrolysis except producing oxyhydrogen, meeting also can be accompanied by the generation heat, make that the temperature in the electrolyzer 102 continues to raise, and cause the oxyhydrogen Yin Wendu that produces through electrolysis too high and be full of the unfavorable follow-up burning of aqueous vapor; Simultaneously, also make brine electrolysis 101 cause electrolytic efficiency to reduce because temperature raises, certainly, the high temperature that continues also can cause member to cross cause thermal damage, stability and work-ing life that influence is whole.
Lodging in the above-mentioned shortcoming of initiation in this electrolyzer 102 for fear of heat, generally speaking, is as shown in Figure 2, a radiator fan 105 is set to reduce the temperature of this electrolyzer 102 around this electrolyzer 102.Yet, utilize this radiator fan 105 can only reduce the surface temperature of this electrolyzer 102, and can't effectively reduce the temperature of these electrolyzer 102 inside and brine electrolysis 101, therefore, the effect of radiating and cooling is relatively poor.
In order to improve the relatively poor shortcoming of above-mentioned radiating and cooling effect, relevant dealer develops technology as shown in Figure 3, the place of improving is: utilize a gang of Pu 106 to extract brine electrolysis 101 cooling that circulates to electrolyzer 102, though so can improve whole radiating efficiency, but, utilization group Pu 106 is extracted brine electrolysis 101 and is needed to consume a large amount of electric power, has increased the cost of electrolysis generation oxyhydrogen undoubtedly.
The utility model content
The purpose of this utility model is to provide a kind of can reduce temperature and the lower-cost cyclic electrolysis device that the electrolysis operation produces.
The utility model cyclic electrolysis device comprises the cycling element that an electrolysis cells, connect this electrolysis cells, and the cooling unit with the corresponding setting of this cycling element.
This electrolysis cells comprises that electrolyzer, a multi-disc that is loaded with electrolytic solution is arranged at intervals at the battery lead plate in this electrolyzer, and power supply source that is electrically connected described battery lead plate, each plate electrode plate all is formed with a circulation pore, and a through hole that is higher than this circulation pore.
This cycling element comprises that one is communicated with this electrolyzer and connects this temporary bucket with the circulation line of conveying electrolyte and oxyhydrogen, temporary bucket that is connected this circulation line, one and be installed in electrolytic solution and keep in a barrel liquid storing barrel that is interconnected with this with the gas piping of output oxyhydrogen, one, and return line that connects this liquid storing barrel and this electrolyzer, this circulation line has an influx that is communicated with this electrolyzer and flushes with the through hole height of described battery lead plate, and this return line has a refluxing opening that is communicated with this electrolyzer.This cooling unit comprises a radiator fan with the corresponding setting of this circulation line.
The purpose of this utility model and solve its technical problem and also can be applied to the following technical measures to achieve further.
Preferably, aforesaid cyclic electrolysis device, wherein this cooling unit also comprises a radiating fin that is arranged on this circulation line, this radiator fan is to be positioned at this radiating fin top.
Preferably, aforesaid cyclic electrolysis device, the circulation pore of wherein per two adjacent battery lead plates and through hole are to be staggered to be provided with, and the circulation pore of battery lead plate separately then is to be positioned on the identical axis with through hole.
Preferably, aforesaid cyclic electrolysis device, wherein this cycling element also comprises a control valve that is arranged on this return line, reaches a liquid level of electrolyte height in this electrolyzer of detecting to control the liquidometer that this control valve opens and closes.
Preferably, aforesaid cyclic electrolysis device wherein should have a hollow form staving, a rupture disk that is arranged at this staving top and a noise reduction part that is arranged in this staving by temporary bucket.
Preferably, aforesaid cyclic electrolysis device, wherein this noise reduction part is to be netted and to be all metal material made, this rupture disk then is a slice lead metal sheet.
Preferably, aforesaid cyclic electrolysis device, wherein this circulation line is the form of coil pipe.
Preferably, aforesaid cyclic electrolysis device, wherein this cyclic electrolysis device also comprises a pedestal, and this electrolysis cells, cycling element and this cooling unit all are to be arranged on this pedestal.
The beneficial effects of the utility model are: allow the liquid level of this electrolytic solution near with the influx of this circulation line, utilize the oxyhydrogen that produces that electrolytic solution is pushed in this circulation line, cooperate this radiator fan to the cooling of lowering the temperature of the electrolytic solution in the circulation line again, and electrolytic solution can flow into this temporary bucket and lower the temperature once more with liquid storing barrel, be back to again at last in this electrolyzer, to reduce temperature and the current consumption that the electrolysis operation produces.
Description of drawings
Fig. 1 is a synoptic diagram, and an existing electrolyzer is described;
Fig. 2 is another synoptic diagram, illustrates that one is provided with the electrolyzer of radiator fan;
Fig. 3 is another synoptic diagram, illustrates that one is provided with the electrolyzer at group Pu;
Fig. 4 is a synoptic diagram, and first preferred embodiment of cyclic electrolysis device of the present utility model is described;
Fig. 5 is a local amplification view, and the aspect of battery lead plate in the preferred embodiment is described;
Fig. 6 is a partial perspective view, aid illustration Fig. 5;
Fig. 7 is a partial top view, and the aspect of circulation line in the preferred embodiment is described;
Fig. 8 is a part sectioned view, and the aspect of temporary bucket in the preferred embodiment is described;
Fig. 9 is a synoptic diagram, and second preferred embodiment of cyclic electrolysis device of the present utility model is described;
Figure 10 is a vertical view, and the 3rd preferred embodiment of cyclic electrolysis device of the present utility model is described; And
Figure 11 is a side-view, aid illustration Figure 10.
Embodiment
Below in conjunction with drawings and Examples the utility model is elaborated: before the utility model is described in detail, be noted that in the following description content that similar elements is to represent with identical Reference numeral.
Consult Fig. 4, first preferred embodiment of the utility model cyclic electrolysis device 2 comprises the cycling element 4 that an electrolysis cells 3, connects this electrolysis cells 3, and one with the cooling unit 5 of these cycling element 4 corresponding settings.
This electrolysis cells 3 comprises that electrolyzer 31, a multi-disc that is loaded with electrolytic solution 32 is arranged at intervals at the battery lead plate 33 in this electrolyzer 31, and the power supply source 34 of the described battery lead plate 33 of an electrical connection, utilizes 32 energisings of 33 pairs of electrolytic solution of described battery lead plate to produce oxyhydrogens.
Consult Fig. 5,6, each electrode plate 33 all is formed with a circulation pore 35, an and through hole 36 that is higher than this circulation pore 35, and the circulation pore 35 of per two adjacent battery lead plates 33 is to be staggered to be provided with through hole 36, and the circulation pore 35 of battery lead plate 33 separately then is to be positioned on the identical axis L with through hole 36.Allow the liquid level 37 of this electrolytic solution 32 highly be near described through hole 36, so that described circulation pore 35 is to be soaked in this electrolytic solution 32.
Consult Fig. 4, this cycling element 4 comprises that a return line 45, that is communicated with that this electrolyzer 31 is connected this circulation line 41 with conveying electrolyte 32 with the circulation line 41, of oxyhydrogen temporary bucket 42, connects that this temporary bucket 42 is installed in electrolytic solution 32 with gas pipings 43, of output oxyhydrogen and is connected this liquid storing barrel 44 and this electrolyzer 31 with these temporary bucket 42 liquid storing barrels that are interconnected 44, is arranged at the control valve 46 on this return line 45, and one detects the liquid level 37 of electrolytic solution 32 in this electrolyzer 31 highly to control the liquidometer 47 of these control valve 46 keyings.This circulation line 41 has an influx 411 that is communicated with this electrolyzer 31 and highly flushes with the through hole 36 of described battery lead plate 33, and this return line 45 has the refluxing opening 451 of this electrolyzer 31 of connection.In this preferred embodiment, this circulation line 41 is forms of coil pipe as shown in Figure 7.
This cooling unit 5 comprise one with the radiator fan 51 of these circulation line 41 corresponding settings, in this preferred embodiment, this radiator fan 51 is to be positioned at this circulation line 41 tops.
Consult Fig. 8, should have the rupture disk 422 that a hollow form staving 421, is arranged at these staving 421 tops by temporary bucket 42, an and noise reduction part 423 that is arranged in this staving 421, in this preferred embodiment, this noise reduction part 423 is to be netted and to be all metal material made, and this rupture disk 422 then is a lead metal sheet.
Consult Fig. 4, when described battery lead plate 33 is subjected to the driving of this power supply source 34 and conducts electricity, promptly can the switch on electrolysis and then produce oxyhydrogen of this electrolytic solution 32, at this moment, because the liquid level 37 of this electrolytic solution 32 is to be positioned at described through hole 36 places, and the circulation pore 35 of per two adjacent battery lead plates 33 is to be staggered to be provided with through hole 36, therefore, when electrolytic solution 32 is flowed through described circulation pore 35 and through hole 36 and 33 of described battery lead plates bigger contact area is arranged, effectively improve the efficient that produces oxyhydrogen whereby.
Moreover, electrolysis also can make electrolytic solution 32 produce high temperature, and then form at the liquid level 37 of electrolytic solution 32 and to gush (bubbling) phenomenon of boiling, cooperate the oxyhydrogen that electrolysis produced, liquid level 37 can be formed and gush the electrolytic solution 32 that boils and push this influx 411 gradually and flow in this circulation line 41, at this moment, this radiator fan 51 can drive the temperature that air flowing not only can reduce the electrolytic solution 32 that is arranged in this circulation line 41 and oxyhydrogen, can also make the contained aqueous vapor condensation of oxyhydrogen to reduce the moisture in the oxyhydrogen.
Consult Fig. 4,8, then, oxyhydrogen and electrolytic solution 32 can flow in this temporary bucket 42.Can be because the proportion of oxyhydrogen is little from these gas piping 43 outputs, to supply follow-up use or storage; Electrolytic solution 32 then flows in staving 421 of this temporary bucket 42 because of ordering about of gravity, makes electrolytic solution 32 can be fully mix with the lower air of temperature or electrolytic solution 32 in the staving 421 and reduce temperature; When electrolytic solution 32 after this staving 421 flows into these liquid storing barrels 44, can mix mutually with the electrolytic solution 32 in the liquid storing barrel 44, and reduce temperature again.
What this will specify be, if it is too much to be somebody's turn to do temporary barrel 42 stored oxyhydrogen, and build-up of pressure is when increasing, can preferentially break through this rupture disk 422, and then let out except that the oxyhydrogen in this staving 421, avoid this staving 421 to blast because of pressure is excessive, this noise reduction part 423 then can reduce the noise when letting out except that oxyhydrogen.
Consult Fig. 4, when the liquid level 37 of the electrolytic solution 32 in these liquidometer 47 these electrolyzers 31 of detecting is lower than the influx 411 of this circulation line 41, then open this control valve 46, make in electrolytic solution 32 refluxing opening 451 these electrolyzers 31 of inflow in the liquid storing barrel 44 via return line 45; If then close this control valve 46 when the liquid level 37 of the electrolytic solution 32 in this electrolyzer 31 remains in the influx 411 of this circulation line 41.Effectively recycle electrolytic solution 32 whereby, can also control the electrolytic reaction temperature of electrolyzer 31, not only current consumption is low, also can reduce the temperature of electrolysis operation generation simultaneously and then keep electrolytic efficiency, avoids member to cross cause thermal damage, and can increase the service life.
Consult Fig. 9, second preferred embodiment of cyclic electrolysis device 2 of the present utility model roughly is identical with this first preferred embodiment, place inequality is: this cooling unit 5 comprises that also one is arranged at the radiating fin 52 on this circulation line 41, and this radiator fan 51 is to be positioned at this radiating fin 52 tops.The electrolytic solution 32 that utilizes this radiator fan 51 and this radiating fin 52 to cooperatively interact effectively to improve this circulation line 41 of flowing through and the cooling performance of oxyhydrogen.
Consult Figure 10,11, the 3rd preferred embodiment of cyclic electrolysis device 2 of the present utility model roughly is identical with this first preferred embodiment, comprise an electrolysis cells 3, one connects the cycling element 4 of this electrolysis cells 3, and one with the cooling unit 5 of these cycling element 4 corresponding settings, place inequality is: this cyclic electrolysis device 2 also comprises a pedestal 6, and this electrolysis cells 3, cycling element 4 and cooling unit 5 all are to be arranged on this pedestal 6, and this radiating fin 52 is directly around being arranged on this circulation line 41, utilize above-mentioned integration design, can effectively reduce whole volume.
In sum, cyclic electrolysis device 2 of the present utility model, utilization is highly to flush with the through hole 36 of described battery lead plate 33 with the influx 411 of this circulation line 41, and allow the liquid level 37 of electrolytic solution 32 highly be near this influx 411, by the oxyhydrogen that produces electrolytic solution 32 is pushed in this circulation line 41, cooperate the cooling of lowering the temperature of electrolytic solution 32 in 51 pairs of these circulation lines 41 of this radiator fan again, and electrolytic solution 32 can flow into and should lower the temperature once more with liquid storing barrel 44 by temporary bucket 42, be back to again at last in this electrolyzer 31, not only power consumption is low, also can reduce simultaneously the temperature of electrolysis operation generation and then effectively keep electrolytic efficiency, avoiding member to cross cause thermal damage increases work-ing life.
Claims (8)
1. cyclic electrolysis device comprises:
An electrolysis cells comprises that electrolyzer, a multi-disc that is loaded with electrolytic solution is arranged at intervals at the battery lead plate in the described electrolyzer, and a power supply source that is electrically connected described battery lead plate; And
A cycling element, comprise that one is communicated with described electrolyzer with conveying electrolyte and the circulation line of oxyhydrogen, a temporary bucket that is connected described circulation line, a described temporary barrel of gas piping with the output oxyhydrogen of connection, a liquid storing barrel that is installed in electrolytic solution and is interconnected with described temporary bucket, and the return line of a described liquid storing barrel of connection and described electrolyzer;
It is characterized in that: described cyclic electrolysis device also comprises a cooling unit, described cooling unit comprises the radiator fan of a corresponding setting of the circulation line with described cycling element, and each plate electrode plate of described electrolysis cells all is formed with a circulation pore, and through hole that is higher than described circulation pore, described circulation line has an influx that is communicated with described electrolyzer and flushes with the through hole height of described battery lead plate, and described return line has a refluxing opening that is communicated with described electrolyzer.
2. cyclic electrolysis device according to claim 1 is characterized in that: described cooling unit also comprises a radiating fin that is arranged on the described circulation line, and described radiator fan is to be positioned at described radiating fin top.
3. cyclic electrolysis device according to claim 1 is characterized in that: the circulation pore of per two adjacent battery lead plates and through hole are to be staggered to be provided with, and the circulation pore of battery lead plate separately then is to be positioned on the identical axis with through hole.
4. according to claim 1 or 2 or 3 described cyclic electrolysis devices, it is characterized in that: described cycling element also comprises a control valve that is arranged on the described return line, reaches a liquid level of electrolyte height in the described electrolyzer of detecting to control the liquidometer that described control valve opens and closes.
5. cyclic electrolysis device according to claim 4 is characterized in that: described temporary bucket has a hollow form staving, a rupture disk that is arranged at described staving top and a noise reduction part that is arranged in the described staving.
6. cyclic electrolysis device according to claim 5 is characterized in that: described noise reduction part is to be netted and to be all metal material made, and described rupture disk then is a slice lead metal sheet.
7. cyclic electrolysis device according to claim 1 is characterized in that: described circulation line is the form of coil pipe.
8. cyclic electrolysis device according to claim 1 is characterized in that: described cyclic electrolysis device also comprises a pedestal, and described electrolysis cells, cycling element and described cooling unit all are to be arranged on the described pedestal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202161467U CN201738010U (en) | 2010-06-01 | 2010-06-01 | Cyclic electrolysis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202161467U CN201738010U (en) | 2010-06-01 | 2010-06-01 | Cyclic electrolysis device |
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| Publication Number | Publication Date |
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| CN201738010U true CN201738010U (en) | 2011-02-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010202161467U Expired - Fee Related CN201738010U (en) | 2010-06-01 | 2010-06-01 | Cyclic electrolysis device |
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| CN (1) | CN201738010U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103361667A (en) * | 2012-04-06 | 2013-10-23 | 罗弘岳 | Heat radiation structure of hydrogen and oxygen generating device |
| CN103380087A (en) * | 2011-03-14 | 2013-10-30 | 金庆洙 | Open-cell type apparatus for preparing sodium hypochlorite |
| CN103390771A (en) * | 2013-07-30 | 2013-11-13 | 东莞市杉杉电池材料有限公司 | Battery electrolyte blending system |
| CN104357878A (en) * | 2014-11-21 | 2015-02-18 | 邹小立 | Device for assisting cooling of extracorporeal circulation of electrolytic bath |
| CN105624723A (en) * | 2014-10-16 | 2016-06-01 | 林信湧 | Gas generator |
| CN108385123A (en) * | 2018-01-30 | 2018-08-10 | 广西奔科衷新能源有限公司 | It is a kind of quickly for the device of engine hydrogen and oxygen mixture |
| CN108425127A (en) * | 2018-01-30 | 2018-08-21 | 广西奔科衷新能源有限公司 | A kind of device quickly preparing hydrogen and oxygen mixture |
| CN109385642A (en) * | 2017-08-04 | 2019-02-26 | 林信涌 | Gas generator |
-
2010
- 2010-06-01 CN CN2010202161467U patent/CN201738010U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103380087A (en) * | 2011-03-14 | 2013-10-30 | 金庆洙 | Open-cell type apparatus for preparing sodium hypochlorite |
| CN103380087B (en) * | 2011-03-14 | 2015-03-25 | 金庆洙 | Open-cell type apparatus for preparing sodium hypochlorite |
| CN103361667A (en) * | 2012-04-06 | 2013-10-23 | 罗弘岳 | Heat radiation structure of hydrogen and oxygen generating device |
| CN103390771A (en) * | 2013-07-30 | 2013-11-13 | 东莞市杉杉电池材料有限公司 | Battery electrolyte blending system |
| CN105624723A (en) * | 2014-10-16 | 2016-06-01 | 林信湧 | Gas generator |
| CN104357878A (en) * | 2014-11-21 | 2015-02-18 | 邹小立 | Device for assisting cooling of extracorporeal circulation of electrolytic bath |
| CN104357878B (en) * | 2014-11-21 | 2016-09-28 | 邹小立 | A kind of auxiliary electrolytic cell extracorporeal circulation heat sink |
| CN109385642A (en) * | 2017-08-04 | 2019-02-26 | 林信涌 | Gas generator |
| CN109385642B (en) * | 2017-08-04 | 2021-04-13 | 林信涌 | Gas generator |
| CN108385123A (en) * | 2018-01-30 | 2018-08-10 | 广西奔科衷新能源有限公司 | It is a kind of quickly for the device of engine hydrogen and oxygen mixture |
| CN108425127A (en) * | 2018-01-30 | 2018-08-21 | 广西奔科衷新能源有限公司 | A kind of device quickly preparing hydrogen and oxygen mixture |
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| Date | Code | Title | Description |
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| 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: 20110209 Termination date: 20150601 |
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| EXPY | Termination of patent right or utility model |