CN106159303B - A kind of high power DC vanadium cell electricity storage station - Google Patents
A kind of high power DC vanadium cell electricity storage station Download PDFInfo
- Publication number
- CN106159303B CN106159303B CN201610776912.7A CN201610776912A CN106159303B CN 106159303 B CN106159303 B CN 106159303B CN 201610776912 A CN201610776912 A CN 201610776912A CN 106159303 B CN106159303 B CN 106159303B
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- Prior art keywords
- anode
- cathode
- inlet tube
- tube
- variable frequency
- Prior art date
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
- H01M8/188—Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/10—Primary casings, jackets or wrappings of a single cell or a single battery
- H01M50/147—Lids or covers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/0276—Sealing means characterised by their form
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04276—Arrangements for managing the electrolyte stream, e.g. heat exchange
- H01M8/04283—Supply means of electrolyte to or in matrix-fuel cells
-
- 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
- Y02E60/10—Energy storage using batteries
-
- 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
- Y02E60/50—Fuel cells
Abstract
The present invention provides a kind of high power DC vanadium cell electricity storage station, including anode outlet tube, filter one, cathode inlet tube, multistage crossover sub one, multistage crossover sub two, filter two, anode inlet tube, seal cover board, anode connecting tube, cabinet, electrode plate, seal convexity block and cathode connecting conduit, filter one is equipped on anode outlet tube, filter two is installed on anode inlet tube, seal cover board lower end is equipped with cabinet, two electrode plates are symmetrically mounted on box house, seal convexity block is fixed on electrode plate lower end, electrode plate is mutually tightly connected by seal convexity with box house bottom end, cathode inlet tube is connected by multistage crossover sub one with cathode connecting conduit, anode connecting tube passes through multistage crossover sub two with anode inlet tube and is connected, the present invention is easy to use, convenient for operation, prevent line clogging, it improves Anolyte quality, convenient for safeguarding and replacement, reduces cost, stability is good, high reliablity.
Description
Technical field
The present invention is a kind of high power DC vanadium cell electricity storage station, belongs to battery apparatus field.
Background technique
High power DC vanadium cell electricity storage station is that will have the vanadium ion solution of different valence state respectively as anode and cathode
Active material, be separately stored in respective electrolyte storage tank, electrolyte by pump effect, by external receiver circulation point
The cathode chamber and anode chamber of battery are not flowed through, and oxidation and reduction reaction occurs in electrode plate surface, realize the charge and discharge to battery
Electricity.
Often there is sediment in anolyte on existing direct current vanadium cell electricity storage station, can block runner, reduces anolyte
Quality also results in pile and scraps, and the electrode plate in existing direct current vanadium cell electricity storage station can be by electrolytic corrosion, every one section
Time will carry out full maintenance or replacement by professional person, and this maintenance is expensive, laborious, increases maintenance cost.
Summary of the invention
In view of the deficienciess of the prior art, it is an object of the present invention to provide a kind of high power DC vanadium cell electricity storage station, with
The problems mentioned above in the background art are solved, the present invention is easy to use, convenient for operation, prevents line clogging, improves anolyte
Quality, convenient for safeguarding and replacement, reduces cost, stability is good, high reliablity.
To achieve the goals above, the present invention is to realize by the following technical solutions: a kind of high power DC vanadium electricity
Pond electricity storage station, including go out liquid structure, cell reaction case, feed liquor structure and DC power supply, the liquid structure out is by anode liquid storage
Tank, anode outlet tube, filter one, variable frequency pump one, cathode outlet tube, variable frequency pump two and cathode fluid reservoir composition, the sun
Pole fluid reservoir right end is equipped with anode outlet tube, and filter one, one right side of filter are equipped on the anode outlet tube
Equipped with variable frequency pump one, the variable frequency pump one is mounted on anode outlet tube, is equipped with cathode on the right side of the anode outlet tube and is gone out liquid
It manages, variable frequency pump two is installed on the cathode outlet tube, cathode fluid reservoir, the cathode storage are equipped on the right side of the variable frequency pump two
Flow container left end is connected with cathode outlet tube, and the feed liquor structure is by cathode inlet tube, variable frequency pump three, multistage crossover sub one, more
Grade crossover sub two, filter two, variable frequency pump four and anode inlet tube form, and are equipped with variable frequency pump on the cathode inlet tube
Three, multistage crossover sub one is equipped on the left of the variable frequency pump three, multistage one right end of crossover sub connects cathode inlet tube, institute
It states and multistage crossover sub two is installed on the left of multistage crossover sub one, multistage two left end of crossover sub is equipped with anode feed liquor
It manages, filter two is installed on the anode inlet tube, variable frequency pump four, the variable frequency pump four are equipped on the left of the filter two
It is mounted on anode inlet tube, the cell reaction case is reacted by seal cover board, anode connecting tube, cabinet, electrode plate, anolyte
Chamber, seal convexity block, ionic membrane, catholyte reaction chamber and cathode connecting conduit composition, the seal cover board lower end are equipped with cabinet,
There are two the electrode plate is set, two electrode plates are symmetrically mounted on box house, and the anolyte reaction chamber right end is equipped with
Ionic membrane, the ionic membrane right end are equipped with catholyte reaction chamber, be equipped between two electrode plates anolyte reaction chamber,
Ionic membrane and catholyte reaction chamber, there are two the seal convexity block is set, two seal convexity blocks are separately fixed at two
A electrode plate lower end, the electrode plate are mutually tightly connected by seal convexity with box house bottom end, and the anode connecting tube is right
Side is equipped with cathode connecting conduit, and the anode connecting tube and cathode connecting conduit are symmetrically mounted on seal cover board, and the cabinet is built-in
Match anolyte reaction chamber, seal convexity block, ionic membrane and catholyte reaction chamber, anode fluid reservoir upper end jointed anode
Inlet tube, cathode fluid reservoir upper end are equipped with cathode inlet tube, and the cathode inlet tube passes through multistage crossover sub one and yin
Pole connecting tube is connected, and the anode connecting tube passes through multistage crossover sub two with anode inlet tube and is connected, the direct current
Source is connected by electric wire with two electrode plates, and the anode outlet tube passes through cabinet and is connected with anolyte reaction chamber, described
Cathode outlet tube passes through cabinet and is connected with catholyte reaction chamber.
Further, potentiometer is installed on the anode outlet tube.
Further, anti-down irrigation pipe, institute are connected between the anode outlet tube right part upper end and anolyte reaction chamber
It states and is connected with anti-down irrigation pipe between cathode outlet tube left part upper end and catholyte reaction chamber.
Further, there are two handles for installation on the seal cover board upper surface.
Further, the seal convexity block is equipped with sealing ring.
Further, the ionic membrane upper end is equipped with snap-gauge and snap-gauge is mounted on seal cover board.
Beneficial effects of the present invention: a kind of high power DC vanadium cell electricity storage station, by addition filter, this sets the present invention
Meter, which is realized, is filtered removal of impurities and sediment to electrolyte, restores electrolyte quality, solves existing direct current vanadium cell electricity storage station
On anolyte often there is sediment, can block runner, reduce anolyte quality, also result in the problems such as pile is scrapped, this
Invention is quickly connected to connecting tube with inlet tube by adding multistage crossover sub, design realization, is also convenient for replacing.
Because of addition seal cover board, cabinet and electrode plate, which realizes quick-replaceable electrode plate, solves existing direct current
Electrode plate in vanadium cell electricity storage station can by electrolytic corrosion, will be carried out at regular intervals by professional person full maintenance or
The problems such as replacement, this maintenance is expensive, laborious, increases maintenance cost, because adding seal convexity block, which realizes sealing
Effect.
Because adding potentiometer, design realization is monitored the present invention, and because adding anti-down irrigation pipe, which prevents electricity
Solution liquid reverse irrigation returns back out liquid pipe, and because adding handle, which lifts seal cover board convenient for staff, and because adding sealing ring, this is set
Meter improves sealing effect, and because adding snap-gauge, which realizes positioning action, facilitates installation seal cover board, and the present invention is easy to use,
Convenient for operation, line clogging is prevented, improves anolyte quality, convenient for safeguarding and replacement reduces cost, stability is good, reliability
It is high.
Detailed description of the invention
Upon reading the detailed description of non-limiting embodiments with reference to the following drawings, other feature of the invention,
Objects and advantages will become more apparent upon:
Fig. 1 is a kind of structural schematic diagram of high power DC vanadium cell electricity storage station of the present invention；
Fig. 2 is a kind of schematic diagram of the cell reaction case of high power DC vanadium cell electricity storage station of the present invention；
In figure: 1- anode fluid reservoir, 2- anode outlet tube, 3- filter one, 4- variable frequency pump one, 5- cell reaction case, 6-
Cathode outlet tube, 7- variable frequency pump two, 8- cathode fluid reservoir, 9- cathode inlet tube, 10- variable frequency pump three, 11- multistage crossover sub
One, 12- DC power supply, 13- multistage crossover sub two, 14- filter two, 15- variable frequency pump four, 16- anode inlet tube, 17- are close
Cover plate, 18- anode connecting tube, 19- cabinet, 20- electrode plate, 21- anolyte reaction chamber, 22- seal convexity block, 23- ion
Film, 24- catholyte reaction chamber, 25- cathode connecting conduit.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to
Specific embodiment, the present invention is further explained.
Fig. 1 and Fig. 2 are please referred to, the present invention provides a kind of technical solution: a kind of high power DC vanadium cell electricity storage station, including
Liquid structure, cell reaction case 5, feed liquor structure and DC power supply 12 out, liquid structure is by anode fluid reservoir 1, anode outlet tube out
2, filter 1, variable frequency pump 1, cathode outlet tube 6, variable frequency pump 27 and cathode fluid reservoir 8 form, and anode fluid reservoir 1 is right
End is equipped with anode outlet tube 2, and filter 1 is equipped on anode outlet tube 2, and one 3 right side of filter is equipped with variable frequency pump 1,
Variable frequency pump 1 is mounted on anode outlet tube 2, and cathode outlet tube 6 is equipped on the right side of anode outlet tube 2, is pacified on cathode outlet tube 6
Equipped with variable frequency pump 27,27 right side of variable frequency pump is equipped with cathode fluid reservoir 8, and 8 left end of cathode fluid reservoir is connected with cathode outlet tube
6。
Feed liquor structure is by cathode inlet tube 9, variable frequency pump 3 10, multistage crossover sub 1, multistage crossover sub 2 13, mistake
Filter 2 14, variable frequency pump 4 15 and anode inlet tube 16 form, and are equipped with variable frequency pump 3 10, variable frequency pump on cathode inlet tube 9
3 10 left sides are equipped with multistage crossover sub 1, and multistage one 11 right end of crossover sub connects cathode inlet tube 9, multistage crossover sub
One 11 left sides are equipped with multistage crossover sub 2 13, and multistage 2 13 left end of crossover sub is equipped with anode inlet tube 16, anode feed liquor
Filter 2 14 is installed on pipe 16,2 14 left side of filter is equipped with variable frequency pump 4 15, variable frequency pump 4 15 be mounted on anode into
In liquid pipe 16.
Cell reaction case 5 by seal cover board 17, anode connecting tube 18, cabinet 19, electrode plate 20, anolyte reaction chamber 21,
Seal convexity block 22, ionic membrane 23, catholyte reaction chamber 24 and cathode connecting conduit 25 form, and 17 lower end of seal cover board is equipped with case
Body 19, there are two electrode plate 20 is set, two electrode plates 20 are symmetrically mounted on inside cabinet 19, and 21 right end of anolyte reaction chamber is equipped with
Ionic membrane 23,23 right end of ionic membrane are equipped with catholyte reaction chamber 24, are equipped with anolyte reaction chamber between two electrode plates 20
21, ionic membrane 23 and catholyte reaction chamber 24, there are two seal convexity block 22 is set, two seal convexity blocks 22 are separately fixed at
Two 20 lower ends of electrode plate, electrode plate 20 are mutually tightly connected by seal convexity with 19 inner bottom of cabinet, anode connecting tube 18
Right side is equipped with cathode connecting conduit 25, and anode connecting tube 18 and cathode connecting conduit 25 are symmetrically mounted on seal cover board 17, cabinet 19
Inside assemble anolyte reaction chamber 21, seal convexity block 22, ionic membrane 23 and catholyte reaction chamber 24.
1 upper end jointed anode inlet tube 16 of anode fluid reservoir, 8 upper end of cathode fluid reservoir be equipped with cathode inlet tube 9, cathode into
Liquid pipe 9 passes through multistage crossover sub 1 and is connected with cathode connecting conduit 25, and anode connecting tube 18 passes through with anode inlet tube 16
Multistage crossover sub 2 13 is connected, and DC power supply 12 is connected by electric wire with two electrode plates 20, and anode outlet tube 2 passes through
Cabinet 19 is connected with anolyte reaction chamber 21, and cathode outlet tube 6 passes through cabinet 19 and is connected with catholyte reaction chamber 24.
Potentiometer is installed on anode outlet tube 2, is connected between 2 right part upper end of anode outlet tube and anolyte reaction chamber 21
There is anti-down irrigation pipe, is connected with anti-down irrigation pipe, seal cover board between 6 left part upper end of cathode outlet tube and catholyte reaction chamber 24
There are two handle, seal convexity block 22 is equipped with sealing ring for installation on 17 upper surfaces, and 23 upper end of ionic membrane is equipped with snap-gauge and snap-gauge
It is mounted on seal cover board 17.
Specific embodiment: check for scarce in use, staff first checks the present invention
It falls into, can not be just carried out if there is defect using needing that maintenance personal is notified to repair at this time, if there is no problem
If can be carried out using in use, staff runs variable frequency pump 1 and variable frequency pump 27 simultaneously, variable frequency pump 1 works
Anolyte in anode fluid reservoir 1 can be extracted into anode outlet tube 2, then enter anolyte by anode outlet tube 2 and react
In chamber 21, for anolyte when anode outlet tube 2 flows, anolyte can pass through filter 1, and filter 1 is realized anolyte
In removal of impurities and sediment filter out, restore the quality of anolyte, prevent anode outlet tube 2 block, variable frequency pump 27 work can
The catholyte in cathode fluid reservoir 8 is extracted into cathode outlet tube 6, then enters catholyte by cathode outlet tube 6 and react
In chamber 24, then catholyte and anolyte are reacted in cabinet 19, realize electric discharge or charging.
Staff runs variable frequency pump 3 10 and variable frequency pump 4 15 simultaneously, and the work of variable frequency pump 3 10 can react catholyte
Catholyte in chamber 24 is extracted into cathode connecting conduit 25, is entered back into cathode inlet tube 9, subsequently into cathode fluid reservoir 8 into
Row storage, the work of variable frequency pump 4 15 can be extracted into the anolyte in anolyte reaction chamber 21 in anode connecting tube 18, enter back into
In anode inlet tube 16, subsequently into being stored in anode fluid reservoir 1, anolyte is when anode inlet tube 16 flows, anode
Liquid can pass through filter 2 14, filter 2 14 realize in anolyte removal of impurities and sediment filter out, restore anolyte
Quality, prevent anode inlet tube 16 block.
When maintenance personal needs repairing or replaces electrode plate 20, maintenance personal opens seal cover board 17, then repairs people
Electrode plate 20 is repaired or replaced in member, and then maintenance personal closes seal cover board 17, because adding seal cover board 17, cabinet
19 and electrode plate 20, which realizes quick-replaceable electrode plate 20, solves the electrode in existing direct current vanadium cell electricity storage station
Full maintenance or replacement will can be carried out by professional person at regular intervals, this maintenance is expensive, takes by electrolytic corrosion
Power, the problems such as increasing maintenance cost.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention, for this field skill
For art personnel, it is clear that invention is not limited to the details of the above exemplary embodiments, and without departing substantially from spirit of the invention or
In the case where essential characteristic, the present invention can be realized in other specific forms.Therefore, in all respects, should all incite somebody to action
Embodiment regards exemplary as, and is non-limiting, the scope of the present invention by appended claims rather than on state
Bright restriction, it is intended that including all changes that fall within the meaning and scope of the equivalent elements of the claims in the present invention
It is interior.Any reference signs in the claims should not be construed as limiting the involved claims.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (6)
1. a kind of high power DC vanadium cell electricity storage station, including go out liquid structure, cell reaction case, feed liquor structure and direct current
Source, it is characterised in that: the liquid structure out goes out liquid by anode fluid reservoir, anode outlet tube, filter one, variable frequency pump one, cathode
Pipe, variable frequency pump two and cathode fluid reservoir composition, the anode fluid reservoir right end are equipped with anode outlet tube, and the anode goes out liquid
It is equipped with filter one on pipe, is equipped with variable frequency pump one on the right side of the filter one, the variable frequency pump one is mounted on anode outlet tube
On, it is equipped with cathode outlet tube on the right side of the anode outlet tube, variable frequency pump two, the frequency conversion are installed on the cathode outlet tube
Two right side of pump is equipped with cathode fluid reservoir, and cathode fluid reservoir left end is connected with cathode outlet tube；
The feed liquor structure by cathode inlet tube, variable frequency pump three, multistage crossover sub one, multistage crossover sub two, filter two,
Variable frequency pump four and anode inlet tube form, and are equipped with variable frequency pump three on the cathode inlet tube, set on the left of the variable frequency pump three
There is multistage crossover sub one, multistage one right end of crossover sub connects cathode inlet tube, one left side of multistage crossover sub
Multistage crossover sub two is installed, multistage two left end of crossover sub is equipped with anode inlet tube, pacifies on the anode inlet tube
Equipped with filter two, variable frequency pump four is equipped on the left of the filter two, the variable frequency pump four is mounted on anode inlet tube；
The cell reaction case by seal cover board, anode connecting tube, cabinet, electrode plate, anolyte reaction chamber, seal convexity block,
Ionic membrane, catholyte reaction chamber and cathode connecting conduit composition, the seal cover board lower end are equipped with cabinet, and the electrode plate is equipped with
Two, two electrode plates are symmetrically mounted on box house, and the anolyte reaction chamber right end is equipped with ionic membrane, the ion
Film right end is equipped with catholyte reaction chamber, is equipped with anolyte reaction chamber, ionic membrane and cathode between two electrode plates
Liquid reaction chamber, there are two the seal convexity block is set, two seal convexity blocks are separately fixed at two electrode plate lower ends, institute
It states electrode plate to be mutually tightly connected by seal convexity with box house bottom end, cathode is equipped on the right side of the anode connecting tube and is connected
Pipe, the anode connecting tube and cathode connecting conduit are symmetrically mounted on seal cover board, and anolyte reaction is assembled in the cabinet
Chamber, seal convexity block, ionic membrane and catholyte reaction chamber；
Anode fluid reservoir upper end jointed anode inlet tube, cathode fluid reservoir upper end are equipped with cathode inlet tube, the yin
Pole inlet tube is connected by multistage crossover sub one with cathode connecting conduit, and the anode connecting tube passes through more with anode inlet tube
Grade crossover sub two is connected, and the DC power supply is connected by electric wire with two electrode plates, and the anode outlet tube passes through
Cabinet is connected with anolyte reaction chamber, and the cathode outlet tube passes through cabinet and is connected with catholyte reaction chamber.
2. a kind of high power DC vanadium cell electricity storage station according to claim 1, it is characterised in that: the anode outlet tube
On potentiometer is installed.
3. a kind of high power DC vanadium cell electricity storage station according to claim 1, it is characterised in that: the anode outlet tube
Anti-down irrigation pipe is connected between right part upper end and anolyte reaction chamber, the cathode outlet tube left part upper end is reacted with catholyte
Anti-down irrigation pipe is connected between chamber.
4. a kind of high power DC vanadium cell electricity storage station according to claim 1, it is characterised in that: on the seal cover board
There are two handles for installation on end face.
5. a kind of high power DC vanadium cell electricity storage station according to claim 1, it is characterised in that: the seal convexity block
It is equipped with sealing ring.
6. a kind of high power DC vanadium cell electricity storage station according to claim 1, it is characterised in that: the ionic membrane upper end
Equipped with snap-gauge and snap-gauge is mounted on seal cover board.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610776912.7A CN106159303B (en) | 2016-08-31 | 2016-08-31 | A kind of high power DC vanadium cell electricity storage station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610776912.7A CN106159303B (en) | 2016-08-31 | 2016-08-31 | A kind of high power DC vanadium cell electricity storage station |
Publications (2)
| Publication Number | Publication Date |
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| CN106159303A CN106159303A (en) | 2016-11-23 |
| CN106159303B true CN106159303B (en) | 2019-02-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610776912.7A Expired - Fee Related CN106159303B (en) | 2016-08-31 | 2016-08-31 | A kind of high power DC vanadium cell electricity storage station |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111490280A (en) * | 2020-04-23 | 2020-08-04 | 贵州聚能世纪科技有限责任公司 | Method for thoroughly solving leakage of vanadium cell stack |
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|---|---|---|---|---|
| JPH08138718A (en) * | 1994-11-08 | 1996-05-31 | Sumitomo Electric Ind Ltd | Operating method of redox-flow cell |
| US5648184A (en) * | 1995-04-13 | 1997-07-15 | Toyo Boseki Kabushiki Kaisha | Electrode material for flow-through type electrolytic cell, wherein the electrode comprises carbonaceous material having at least one groove |
| CN204257760U (en) * | 2014-10-21 | 2015-04-08 | 国网电力科学研究院武汉南瑞有限责任公司 | The online recovery device of a kind of mobile high-power type all-vanadium redox flow battery electrolyte |
| CN204315671U (en) * | 2014-11-24 | 2015-05-06 | 国家电网公司 | A kind of all-vanadium flow battery carrying working power |
| EP2899789A1 (en) * | 2012-09-18 | 2015-07-29 | Sumitomo Electric Industries, Ltd. | Redox flow battery |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10230124B2 (en) * | 2013-12-03 | 2019-03-12 | Massachusetts Institute Of Technology | Gravity induced flow cell |
-
2016
- 2016-08-31 CN CN201610776912.7A patent/CN106159303B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08138718A (en) * | 1994-11-08 | 1996-05-31 | Sumitomo Electric Ind Ltd | Operating method of redox-flow cell |
| US5648184A (en) * | 1995-04-13 | 1997-07-15 | Toyo Boseki Kabushiki Kaisha | Electrode material for flow-through type electrolytic cell, wherein the electrode comprises carbonaceous material having at least one groove |
| EP2899789A1 (en) * | 2012-09-18 | 2015-07-29 | Sumitomo Electric Industries, Ltd. | Redox flow battery |
| CN204257760U (en) * | 2014-10-21 | 2015-04-08 | 国网电力科学研究院武汉南瑞有限责任公司 | The online recovery device of a kind of mobile high-power type all-vanadium redox flow battery electrolyte |
| CN204315671U (en) * | 2014-11-24 | 2015-05-06 | 国家电网公司 | A kind of all-vanadium flow battery carrying working power |
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| CN106159303A (en) | 2016-11-23 |
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