CN204874762U - Electrolyte liquid feeding circulative cooling system - Google Patents
Electrolyte liquid feeding circulative cooling system Download PDFInfo
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- CN204874762U CN204874762U CN201520615873.3U CN201520615873U CN204874762U CN 204874762 U CN204874762 U CN 204874762U CN 201520615873 U CN201520615873 U CN 201520615873U CN 204874762 U CN204874762 U CN 204874762U
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- liquid
- electrolytic solution
- pipeline
- electrolyzer
- air collector
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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 an electrolyte liquid feeding circulative cooling system, include: the electrolysis trough, it is electrolysis generating device, and the electrolysis trough is a confined cell body, and is full of electrolyte in it, stock solution gas collection jar, its vertical orientation setting in edge are in the top of electrolysis trough, and the bottom of stock solution gas collection jar communicates with each other through the upper portion gas -liquid of a gas -liquid pipeline with the electrolysis trough, the fluid infusion jar, its vertical orientation setting in edge is in the below of stock solution gas collection jar, and it has electrolyte or distilled water to hold in the fluid infusion jar, and, power unit, its through first fluid pipeline and second fluid pipeline respectively with fluid infusion jar and stock solution gas collection jar liquid intercommunication separately to in electrolyte in the fluid infusion jar or distilled water benefit income stock solution gas collection jar. The utility model discloses both need not to force the heat dissipation to the electrolysis trough, need not derive the postcooling with electrolyte again, and utilized the subsidiary tank structure of system self and pipeline can realize the circulation of electrolyte cooling, guaranteed stable electrolytic efficiency and part life.
Description
Technical field
The utility model relates to a kind of filtration refrigerating unit, and more particularly, the utility model relates to a kind of electrolytic solution liquid feeding circulating cooling system of hydro-electrolytic hydroxide generator.
Background technology
In the process of water electrolysis hydrogen making, due to factors such as the generation of electrolytic reaction, the pressure-tight structures of electrolyzer, electrolyzer electrolyte inside constant temperature can be caused to raise, when after the too high even liquid boiling of electrolyte temperature, serious negative impact can be produced to electrolytic efficiency and gas production rate.
General employing carries out air blast cooling heat radiation to electrolyzer and electrolytic solution derivation cooling two kinds of modes carry out cooling process to electrolytic solution.The mode of electrolyzer air blast cooling heat radiation, the Structural Design Requirement for electrolyzer is higher, complex structure, and cost is higher; Air blast cooling is dispelled the heat, and can bring the rising of power consumption.The mode of cooling derived by electrolytic solution, and comparatively complicated to circulation of elecrolyte pipeline system design, must be realized derivation and the backflow of electrolytic solution by corrosion resistant recycle pump, in technological process, security requirement is higher.
Utility model content
An object of the present utility model solves at least the problems referred to above and/or defect, and provide the advantage will illustrated at least below.
The utility model also has an object to be to provide a kind of electrolytic solution liquid feeding circulating cooling system, by arranging sealant supplement cylinder and actuating unit, liquid in sealant supplement cylinder is added in liquid storage air collector, simultaneously also can to liquid make-up in sealant supplement cylinder, and, spiral coil cooling tube is arranged in the sealant supplement cylinder being full of electrolytic solution or distilled water, by the electrolytic solution cooling flow in liquid storage air collector, achieves the circulating cooling of electrolytic solution.
The technical scheme that the utility model provides is:
A kind of electrolytic solution liquid feeding circulating cooling system, comprising:
Electrolyzer, it is electrolysis of water, and described electrolyzer is a cell body closed, and is full of electrolytic solution in it;
Liquid storage air collector, it is vertically arranged on the top of described electrolyzer, and the bottom of described liquid storage air collector is communicated with the top gas-liquid of described electrolyzer by an Air-liquid pipeline;
Sealant supplement cylinder, it is vertically arranged on the below of described liquid storage air collector, accommodates electrolytic solution or distilled water in described sealant supplement cylinder; And,
Actuating unit, its by first liquid pipeline and second liquid pipeline respectively with described sealant supplement cylinder and described liquid storage air collector fluid connection separately, so that the electrolytic solution in described sealant supplement cylinder or distilled water are filled in described liquid storage air collector.
Preferably, in described electrolytic solution liquid feeding circulating cooling system, described actuating unit is liquid feeding recycle pump, described liquid feeding recycle pump is arranged on by described sealant supplement cylinder, the fluid inlet of described liquid feeding recycle pump is communicated with the lower liquid of described sealant supplement cylinder by described first liquid pipeline, and its liquid outlet is communicated with the upper liquid of described liquid storage air collector by second liquid pipeline.
Preferably, in described electrolytic solution liquid feeding circulating cooling system, in described electrolyzer, be provided with the first liquid level sensor, in described liquid storage air collector, be provided with the second liquid level sensor, in described sealant supplement cylinder, be provided with the 3rd liquid level sensor.
Preferably, described electrolytic solution liquid feeding circulating cooling system, also comprises:
Spiral coil cooling tube, it is vertically arranged in described sealant supplement cylinder, and in the electrolytic solution be soaked in described sealant supplement cylinder or distilled water, one end of described spiral coil cooling tube is communicated with the bottom liquid of described liquid storage air collector by the 3rd fluid pipeline, and the other end is communicated with the lower liquid of described electrolyzer by the 4th fluid pipeline.
Preferably, in described electrolytic solution liquid feeding circulating cooling system, the shape of described spiral coil cooling tube is volution, W type or S type.
Preferably, described electrolytic solution liquid feeding circulating cooling system, also comprises:
Fluid-through port, it is arranged on the bottom of described liquid storage air collector, and described fluid-through port is communicated with one end of described 3rd fluid pipeline, to make described liquid storage air collector by described 3rd fluid pipeline and described spiral coil cooling tube fluid connection.
Preferably, described electrolytic solution liquid feeding circulating cooling system, also comprises:
Gas collection mouth, it is arranged on the bottom of described liquid storage air collector, and described gas collection mouth and one end of described Air-liquid pipeline are communicated with that described liquid storage air collector is communicated with described electrolyzer gas-liquid by described Air-liquid pipeline; And,
Fluid infusion mouth, it is arranged on the top of described liquid storage air collector, and described fluid infusion mouth is communicated with one end of described second liquid pipeline described liquid storage air collector is communicated with described actuating unit by described second liquid pipeline.
Preferably, in described electrolytic solution liquid feeding circulating cooling system, described sealant supplement cylinder and described electrolyzer are in same level height.
Preferably, in described electrolytic solution liquid feeding circulating cooling system, the bottom of described electrolyzer is also provided with electrolyzer fluid inlet, and described electrolyzer fluid inlet is communicated with one end of described 4th fluid pipeline, to make described spiral coil cooling tube and described electrolyzer fluid connection.
Preferably, in described electrolytic solution liquid feeding circulating cooling system, the top of described sealant supplement cylinder is also provided with liquid adding hole and liquid level access panel.
The utility model at least comprises following beneficial effect:
Spiral coil cooling tube shape in the utility model sealant supplement cylinder can be volution, W type or S type, fully increases contact area, improves radiating effect, and coil pipe material can perfect heat-dissipating and the stainless steel of acid-alkali-corrosive-resisting or aluminum alloy material.
Device of the present utility model is both without the need to carrying out forced heat radiation to electrolyzer, cooling after electrolytic solution need not being derived again, utilize the subsidiary tank structure of system self and pipeline can realize the circulation temperature lowering of electrolytic solution, ensure that stable electrolytic efficiency and parts work-ing life.This device is applicable to automotive field and other miniature water Electrowinning oxyhydrogen devices.
The utility model simplicity of design, cost is low, power consumption is low, simultaneously safe model, and efficiency is very high, is applicable to large-scale promotion and uses.
Part is embodied by explanation below by other advantage of the present utility model, target and feature, part also will by research and practice of the present utility model by those skilled in the art is understood.
Accompanying drawing explanation
Fig. 1 is the structural representation of electrolytic solution liquid feeding circulating cooling system described in the utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail, can implements according to this with reference to specification sheets word to make those skilled in the art.
Should be appreciated that used hereinly such as " to have ", other element one or more do not got rid of in " comprising " and " comprising " term or the existence of its combination or interpolation.
As shown in Figure 1, the utility model provides a kind of electrolytic solution liquid feeding circulating cooling system, comprising:
Electrolyzer 1, it is electrolysis of water, and described electrolyzer 1 is a cell body closed, and is full of electrolytic solution in it;
Liquid storage air collector 2, it is vertically arranged on the top of described electrolyzer 1, and the bottom of described liquid storage air collector 2 is communicated by the top gas-liquid of an Air-liquid pipeline 3 with described electrolyzer 1;
Sealant supplement cylinder 7, it is vertically arranged on the below of described liquid storage air collector 2, accommodates electrolytic solution or distilled water in described sealant supplement cylinder 7; And,
Actuating unit 8, its by first liquid pipeline 9 and second liquid pipeline 10 respectively with described sealant supplement cylinder 7 and described liquid storage air collector 2 fluid connection separately, so that the electrolytic solution in described sealant supplement cylinder 7 or distilled water are filled in described liquid storage air collector.
As preferably, described actuating unit 8 is liquid feeding recycle pump, it is other that described liquid feeding recycle pump is arranged on described sealant supplement cylinder 7, the fluid inlet of described liquid feeding recycle pump is communicated with by the lower liquid of described first liquid pipeline 9 with described sealant supplement cylinder 7, and its liquid outlet is communicated with the upper liquid of described liquid storage air collector 2 by second liquid pipeline 10.
As preferably, in described electrolyzer 1, be provided with the first liquid level sensor, in described liquid storage air collector 2, be provided with the second liquid level sensor, in described sealant supplement cylinder 7, be provided with the 3rd liquid level sensor.The bottom limit level height of described liquid storage air collector 2 is set to 1/4 ~ 1/3 of its height, and such height can ensure that electrolytic solution enters in liquid storage air collector 2 with the gas that electrolysis produces.The upper limit level height of liquid storage air collector 2 is set to 3/4 of its height, can ensure the Existential Space of the gas that a part of space produces for electrolysis like this.
As preferably, also comprise:
Spiral coil cooling tube 4, it is vertically arranged in described sealant supplement cylinder 7, and in the electrolytic solution be soaked in described sealant supplement cylinder 7 or distilled water, one end of described spiral coil cooling tube 7 is communicated with the bottom liquid of described liquid storage air collector 2 by the 3rd fluid pipeline 5, and the other end is communicated with the lower liquid of described electrolyzer 1 by the 4th fluid pipeline 6.
As preferably, the shape of described spiral coil cooling tube 4 is volution, W type or S type.
As preferably, also comprise:
Fluid-through port 220, it is arranged on the bottom of described liquid storage air collector 2, and described fluid-through port 220 is communicated with one end of described 3rd fluid pipeline 5, to make described liquid storage air collector 2 by described 3rd fluid pipeline 5 and described spiral coil cooling tube 4 fluid connection.
As preferably, also comprise:
Gas collection mouth 210, it is arranged on the bottom of described liquid storage air collector 2, and described gas collection mouth 210 and one end of described Air-liquid pipeline 3 are communicated with that described liquid storage air collector 2 is communicated with described electrolyzer 1 gas-liquid by described Air-liquid pipeline 3; And,
Fluid infusion mouth, it is arranged on the top of described liquid storage air collector 2, and described fluid infusion mouth 230 is communicated with one end of described second liquid pipeline 10 described liquid storage air collector 2 is communicated with described actuating unit 8 by described second liquid pipeline 10.
As preferably, described sealant supplement cylinder 7 is in same level height with described electrolyzer 1.
As preferably, the bottom of described electrolyzer 1 is also provided with electrolyzer fluid inlet 120, and described electrolyzer fluid inlet 120 is communicated with one end of described 4th fluid pipeline 6, to make described spiral coil cooling tube 4 and described electrolyzer 1 fluid connection.
As preferably, the top of described sealant supplement cylinder 7 is also provided with liquid adding hole 710 and liquid level access panel.As preferably, sealant supplement cylinder is also provided with upper and lower spacing scale, when being observed the liquid level in sealant supplement cylinder by liquid level access panel lower than lower limit scale, can supplement by manually carrying out liquid feeding by liquid adding hole 710.
The workflow of the utility model device is: the gas produced by electrolyzer 1 Inner electrolysis enters liquid storage air collector 2 through air outlet 110, exports gas export line to for use by the air outlet 240 of liquid storage air collector.Simultaneously, upwards exporting continuously of gas, electrolyzer 1 electrolyte inside is driven to flow in liquid storage air collector 2, electrolytic solution in liquid storage air collector 2 is under the effect of difference of altitude, gravity, gas output pressure etc., through bottom fluid-through port 220, enter the stainless steel spiral coil cooling tube 4 in sealant supplement cylinder 7, cooled by the electrolytic solution in sealant supplement cylinder 7 or distilled water to spiral coil cooling tube 4, electrolytic solution cooled in spiral coil cooling tube 4 is back in electrolyzer 1 by electrolyzer 1 bottom electrolyzer fluid inlet 120.So reach the effect of electrolytic solution persistent loop cooling.And, the first liquid level sensor is provided with in described electrolyzer 1, the second liquid level sensor is provided with in described liquid storage air collector 2, the 3rd liquid level sensor is provided with in described sealant supplement cylinder 7, first, second, and third liquid level sensor is all connected with electrical control system, and for detecting the liquid level change of respective liquid in container.Along with the electrolysis loss of electrolytic solution, when liquid storage air collector 2 Inner electrolysis liquid level is lower than bottom limit level, the second liquid level sensor sends signal to electrical control system, and electric control system controls liquid feeding recycle pump starts, and the liquid in sealant supplement cylinder 7 pumps into liquid storage air collector 2; Along with the rising of liquid level in liquid storage air collector 2, when reaching upper limit level, the second liquid level sensor sends signal to electrical control system, and electric control system controls liquid feeding recycle pump stops.In sealant supplement cylinder 7, electrolytic solution or the distilled water of new cooling is added as required, to realize the liquid feeding refrigeration cycle of whole system by the liquid adding hole 710 of sealant supplement cylinder 7.
In one of them embodiment of the present utility model, as shown in Figure 1, a kind of liquid feeding circulating cooling system of electrolytic solution, has had electrolytic solution fluid infusion and hydronic effect concurrently.System is made up of electrolyzer 1, electrolytic solution liquid storage air collector 2 (kettle/bottle), sealant supplement cylinder 7 (kettle/bottle), spiral coil cooling tube 4 and connecting pipeline etc.In this embodiment, electrolyzer 1 adopts controllable type water electrolyzer.
As shown in Figure 1, in electrolyzer 1, be full of electrolytic solution, electrolytic solution electrolysis can be produced gas.Liquid storage air collector 2 is positioned at above electrolyzer 1, and tank base establishes fluid-through port 220 and gas collection mouth 210, is connected respectively with the spiral coil cooling tube 4 in sealant supplement cylinder 7 and electrolyzer 1 air outlet 110; Fluid infusion mouth 230 is established on tank body top, is connected by pump 8 with sealant supplement cylinder 7, and this place's pump 8 adopts liquid feeding recycle pump.Establish the second liquid level sensor in container for storing liquid 2, tank body top sets out gas port 240, is connected with gas export line.
Establish stainless spiral coil cooling tube 4 in sealant supplement cylinder 7, spiral coil cooling tube 4 lower port is connected with electrolyzer 1 bottom fluid inlet 120, establishes pump 8 bottom sealant supplement cylinder 7, is connected with liquid storage air collector 2 top fluid infusion mouth 230.
Here the module number illustrated and treatment scale are used to simplify explanation of the present utility model.The application of liquid storage air collector of the present utility model, sealant supplement cylinder and pipeline etc., modifications and variations be will be readily apparent to persons skilled in the art.
As mentioned above, device of the present utility model is both without the need to carrying out forced heat radiation to electrolyzer, cooling after electrolytic solution need not being derived again, utilize the subsidiary tank structure of system self and pipeline can realize the circulation temperature lowering of electrolytic solution, ensure that stable electrolytic efficiency and parts work-ing life.This device is applicable to automotive field and other miniature water Electrowinning oxyhydrogen devices.
Although embodiment of the present utility model is open as above, but it is not restricted to listed in specification sheets and embodiment utilization, it can be applied to various applicable field of the present utility model completely, for those skilled in the art, can easily realize other amendment, therefore do not deviating under the universal that claim and equivalency range limit, the utility model is not limited to specific details and illustrates here and the legend described.
Claims (10)
1. an electrolytic solution liquid feeding circulating cooling system, is characterized in that, comprising:
Electrolyzer, it is electrolysis of water, and described electrolyzer is a cell body closed, and is full of electrolytic solution in it;
Liquid storage air collector, it is vertically arranged on the top of described electrolyzer, and the bottom of described liquid storage air collector is communicated with the top gas-liquid of described electrolyzer by an Air-liquid pipeline;
Sealant supplement cylinder, it is vertically arranged on the below of described liquid storage air collector, accommodates electrolytic solution or distilled water in described sealant supplement cylinder; And,
Actuating unit, its by first liquid pipeline and second liquid pipeline respectively with described sealant supplement cylinder and described liquid storage air collector fluid connection separately, so that the electrolytic solution in described sealant supplement cylinder or distilled water are filled in described liquid storage air collector.
2. electrolytic solution liquid feeding circulating cooling system as claimed in claim 1, it is characterized in that, described actuating unit is liquid feeding recycle pump, described liquid feeding recycle pump is arranged on by described sealant supplement cylinder, the fluid inlet of described liquid feeding recycle pump is communicated with the lower liquid of described sealant supplement cylinder by described first liquid pipeline, and its liquid outlet is communicated with the upper liquid of described liquid storage air collector by second liquid pipeline.
3. electrolytic solution liquid feeding circulating cooling system as claimed in claim 1, is characterized in that, be provided with the first liquid level sensor in described electrolyzer, be provided with the second liquid level sensor in described liquid storage air collector, be provided with the 3rd liquid level sensor in described sealant supplement cylinder.
4. the electrolytic solution liquid feeding circulating cooling system as described in as arbitrary in claims 1 to 3, is characterized in that, also comprise:
Spiral coil cooling tube, it is vertically arranged in described sealant supplement cylinder, and in the electrolytic solution be soaked in described sealant supplement cylinder or distilled water, one end of described spiral coil cooling tube is communicated with the bottom liquid of described liquid storage air collector by the 3rd fluid pipeline, and the other end is communicated with the lower liquid of described electrolyzer by the 4th fluid pipeline.
5. electrolytic solution liquid feeding circulating cooling system as claimed in claim 4, it is characterized in that, the shape of described spiral coil cooling tube is volution, W type or S type.
6. electrolytic solution liquid feeding circulating cooling system as claimed in claim 4, is characterized in that, also comprise:
Fluid-through port, it is arranged on the bottom of described liquid storage air collector, and described fluid-through port is communicated with one end of described 3rd fluid pipeline, to make described liquid storage air collector by described 3rd fluid pipeline and described spiral coil cooling tube fluid connection.
7. electrolytic solution liquid feeding circulating cooling system as claimed in claim 1, is characterized in that, also comprise:
Gas collection mouth, it is arranged on the bottom of described liquid storage air collector, and described gas collection mouth and one end of described Air-liquid pipeline are communicated with that described liquid storage air collector is communicated with described electrolyzer gas-liquid by described Air-liquid pipeline; And,
Fluid infusion mouth, it is arranged on the top of described liquid storage air collector, and described fluid infusion mouth is communicated with one end of described second liquid pipeline described liquid storage air collector is communicated with described actuating unit by described second liquid pipeline.
8. electrolytic solution liquid feeding circulating cooling system as claimed in claim 1, it is characterized in that, described sealant supplement cylinder and described electrolyzer are in same level height.
9. electrolytic solution liquid feeding circulating cooling system as claimed in claim 1, it is characterized in that, the bottom of described electrolyzer is also provided with electrolyzer fluid inlet, and described electrolyzer fluid inlet is communicated with one end of described 4th fluid pipeline, to make described spiral coil cooling tube and described electrolyzer fluid connection.
10. electrolytic solution liquid feeding circulating cooling system as claimed in claim 1, it is characterized in that, the top of described sealant supplement cylinder is also provided with liquid adding hole and liquid level access panel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201520615873.3U CN204874762U (en) | 2015-08-14 | 2015-08-14 | Electrolyte liquid feeding circulative cooling system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520615873.3U CN204874762U (en) | 2015-08-14 | 2015-08-14 | Electrolyte liquid feeding circulative cooling system |
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| CN204874762U true CN204874762U (en) | 2015-12-16 |
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| CN201520615873.3U Expired - Fee Related CN204874762U (en) | 2015-08-14 | 2015-08-14 | Electrolyte liquid feeding circulative cooling system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109030586A (en) * | 2018-08-15 | 2018-12-18 | 盐城工业职业技术学院 | A kind of agricultural machinery carbon monoxide transducer |
| CN111616379A (en) * | 2019-02-27 | 2020-09-04 | 合肥华凌股份有限公司 | Pesticide residue removing device, electrolytic stock solution and household appliance |
| CN116212603A (en) * | 2021-12-03 | 2023-06-06 | 青岛海尔电冰箱有限公司 | Electrolytic deoxidization system for refrigerator and refrigerator with same |
| CN116623201A (en) * | 2023-06-06 | 2023-08-22 | 天津大学 | High-stability antiscaling electrolysis device based on seawater electrolysis |
-
2015
- 2015-08-14 CN CN201520615873.3U patent/CN204874762U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109030586A (en) * | 2018-08-15 | 2018-12-18 | 盐城工业职业技术学院 | A kind of agricultural machinery carbon monoxide transducer |
| CN111616379A (en) * | 2019-02-27 | 2020-09-04 | 合肥华凌股份有限公司 | Pesticide residue removing device, electrolytic stock solution and household appliance |
| CN116212603A (en) * | 2021-12-03 | 2023-06-06 | 青岛海尔电冰箱有限公司 | Electrolytic deoxidization system for refrigerator and refrigerator with same |
| CN116623201A (en) * | 2023-06-06 | 2023-08-22 | 天津大学 | High-stability antiscaling electrolysis device based on seawater electrolysis |
| CN116623201B (en) * | 2023-06-06 | 2024-01-05 | 天津大学 | High-stability antiscaling electrolysis device based on seawater electrolysis |
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Effective date of registration: 20180528 Address after: 215634 room 905-2, petrochemical trading building, Zhangjiagang Free Trade Zone, Suzhou, Jiangsu Patentee after: Suzhou Yong Hongyun Chemical Technology Co.,Ltd. Address before: 100176 C501A 3, building 1, Beijing, Daxing District economic and Technological Development Zone. Patentee before: CRRC ENERGY TECHNOLOGY (BEIJING) CO.,LTD. |
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Effective date of registration: 20181108 Address after: 214400 No. 8 Jinglian Road, Xia Gang Street, Jiangyin City, Wuxi City, Jiangsu Province Patentee after: JIANGSU BORUNTONG TECHNOLOGY Co.,Ltd. Address before: 215634 room 905-2, petrochemical trading building, Zhangjiagang Free Trade Zone, Suzhou, Jiangsu Patentee before: Suzhou Yong Hongyun Chemical Technology Co.,Ltd. |
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