CN106876763A - A kind of all-vanadium flow battery - Google Patents

A kind of all-vanadium flow battery Download PDF

Info

Publication number
CN106876763A
CN106876763A CN201510923780.1A CN201510923780A CN106876763A CN 106876763 A CN106876763 A CN 106876763A CN 201510923780 A CN201510923780 A CN 201510923780A CN 106876763 A CN106876763 A CN 106876763A
Authority
CN
China
Prior art keywords
electrolyte
vanadium
flow battery
ion concentration
concentration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201510923780.1A
Other languages
Chinese (zh)
Inventor
李春花
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Qingdao Xiangzhi Electronic Technology Co Ltd
Original Assignee
Qingdao Xiangzhi Electronic Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Qingdao Xiangzhi Electronic Technology Co Ltd filed Critical Qingdao Xiangzhi Electronic Technology Co Ltd
Priority to CN201510923780.1A priority Critical patent/CN106876763A/en
Publication of CN106876763A publication Critical patent/CN106876763A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/18Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
    • H01M8/184Regeneration by electrochemical means
    • H01M8/188Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

The present invention relates to a kind of all-vanadium flow battery, belong to flow battery field.A kind of all-vanadium flow battery, including anode electrolyte and electrolyte liquid, it is characterised in that:Anode electrolyte is identical with the total vanadium amount in electrolyte liquid, and vanadium ion concentration is 1.1~1.5 times of vanadium ion concentration in electrolyte liquid in anode electrolyte.Capacity attenuation of the all-vanadium flow battery that the present invention is provided in cyclic process is greatly improved.

Description

A kind of all-vanadium flow battery
Technical field
The present invention relates to a kind of all-vanadium flow battery, belong to flow battery field.
Background technology
All-vanadium flow battery, with it is safe, have extended cycle life, fast response time the features such as, be especially suitable for the demand of extensive energy storage. In all-vanadium redox flow battery system, electrolyte is respectively stored in both positive and negative polarity storage tank, is circulated between pile and electrolyte storage tank by circulating pump, and There is redox reaction in electrode surface, realize the storage and release of electric energy.
The concentration and volume of the both positive and negative polarity electrolyte storage tank electrolyte inside original state of usual all-vanadium redox flow battery system is Identical, with the carrying out of battery system charge and discharge cycles, vanadium ion and water may occur lateral by electrode one through ion-conductive membranes in electrolyte Opposite side is migrated, and causes volume, the vanadium ion concentration of both positive and negative polarity electrolyte, sulfate concentration to change, so as to cause battery capacity to decline Subtract.Patent EP1143546 is mentioned has liquid level difference using initial both positive and negative polarity electrolyte, while both positive and negative polarity electrolyte storage tank bottom sets connecting pipeline Compensation electrolyte migration brings capacity attenuation, although the method can to a certain extent delay the capacity attenuation of battery, the patent is not Electrolyte liquid liquid level difference height, concentration of electrolyte is aligned clearly to be limited.In the prior art, when flow battery capacity attenuation is to necessarily , it is necessary to the later stage takes the new electrolyte of supplement, readjusts both positive and negative polarity concentration of electrolyte and volume or later stage addition electrolyte addition after degree The modes such as agent realize that electrolyte volume volume recovers or delays.But above method by the extra operation for increasing battery and maintenance cost, is unfavorable for liquid again The scale application of galvanic battery.
The content of the invention
It is an object of the invention to provide a kind of all-vanadium flow battery.
A kind of all-vanadium flow battery, including anode electrolyte and electrolyte liquid, anode electrolyte are identical with the total vanadium amount in electrolyte liquid, and Vanadium ion concentration is 1.1~1.5 times of vanadium ion concentration in electrolyte liquid in anode electrolyte.
In above-mentioned technical proposal, total vanadium amount is that the concentration of vanadium ion in electrolyte is multiplied by electrolyte volume;The vanadium ion concentration is in electrolyte The summation of the concentration of the vanadium ion of existing various valence states.Total vanadium amount in all-vanadium flow battery is ensured is identical, and vanadium ion in anode electrolyte When total concentration is 1.1~1.5 times of vanadium ion total concentration in electrolyte liquid, then the volume of negative electrode liquid for anode electrolyte 1.1~ 1.5 times.
In the prior art, all-vanadium flow battery includes anode electrolyte and electrolyte liquid, and the constituent of two kinds of electrolyte is identical, and two kinds The volume of electrolyte is identical, total vanadium amount of anode electrolyte and electrolyte liquid is also identical.Be set to for all-vanadium flow battery initial electrolysis liquid by the present invention Total vanadium amount of two kinds of electrolyte is identical, meanwhile, the volume of the volume more than anode electrolyte of electrolyte liquid, because battery is during circular flow, Electrolyte reclaimed water moves to positive pole from negative pole, sets the volume of the volume more than anode electrolyte of electrolyte liquid so that electrolyte is from negative pole to just The migration of pole is improved, and improves the capacity attenuation in cyclic process.Meanwhile, the sulfate concentration of the sulfate concentration than positive pole of electrolyte liquid It is low, more conducively keep the stabilization of trivalent vanadium.
Vanadium ion concentration is 1.2~1.3 of vanadium ion concentration in electrolyte liquid in the flow battery of the present invention preferably anode electrolyte Times.
The flow battery of the present invention preferably positive pole vanadium ion concentration is 1.4~1.7 mol/Ls.
Beneficial effects of the present invention are:
1) electrolyte can slow down the speed of flow battery capacity attenuation in original state, and the reduction later stage carries out the frequency of recovery operation;
2) by the way that concentration of electrolyte, Volume Changes can be improved with the holding of capacity in charge and discharge process, external harmful substance will not be introduced, also not The later stage is needed to debug, practicality simple to operate.
Specific embodiment
Following non-limiting examples can make one of ordinary skill in the art that the present invention is more fully understood, but limit this hair never in any form It is bright.
Comparative example 1
A kind of all-vanadium flow battery, design parameter is as follows:
Pile is constituted:Nafion115 films, 48cm2 monocells, service condition:Charge and discharge process, with 80mA/cm2 current densities 1.55V is charged to, 30 seconds are stood, 1.0V is discharged to 80mA/cm2 current densities, carry out 300 charge and discharge cycles.
Anode electrolyte:Vanadium ion concentration is 1.5mol/L, and the concentration ratio of wherein V3+ and V4+ is 1:1, sulfate ion concentration is 4.5mol/L;Electrolyte volume is 80ml.
Electrolyte liquid:Vanadium ion concentration is that the concentration ratio of 1.5mol/L, V3+ and V4+ is 1:1, sulfate ion concentration is 4.5mol/L; Electrolyte volume is 80ml.
Embodiment 1
A kind of all-vanadium flow battery, design parameter is as follows:
Pile is constituted:Nafion115 films, 48cm2 monocells, service condition:Charge and discharge process, is charged to 80mA/cm2 current densities 1.55V, stands 30 seconds, and 1.0V is discharged to 80mA/cm2 current densities, carries out 300 charge and discharge cycles.
Anode electrolyte:Vanadium ion concentration is that the concentration ratio of 1.5mol/L, V3+ and V4+ is 1:1, sulfate ion concentration is 4.5mol/L; Electrolyte volume is 80ml.
Electrolyte liquid:Vanadium ion concentration is that the concentration ratio of 1.2mol/L, V3+ and V4+ is 1:1, sulfate ion concentration is 3.6mol/L; Electrolyte volume is 100ml.
The battery of comparative example 1 is by after 300 charge and discharge cycles experiments, its discharge capacity reduces by 50%, and the battery of embodiment 1 is by 300 Secondary charge and discharge cycles experiment, its discharge capacity reduction by 40%, compared to the capacity attenuation degree few 10% of comparative example, improves circulating battery process In capacity attenuation.
Embodiment 2
A kind of all-vanadium flow battery, design parameter is with embodiment 1.
Anode electrolyte:Vanadium ion concentration is that the concentration ratio of 1.5mol/L, V3+ and V4+ is 1:1, sulfate ion concentration is 4.5mol/L; Electrolyte volume is 80ml.
Electrolyte liquid:Vanadium ion concentration is that the concentration ratio of 1.1mol/L, V3+ and V4+ is 1:1, sulfate ion concentration is 3.27mol/L; Electrolyte volume is 110ml.
Result shows that the battery of comparative example 1 is tested by 300 charge and discharge cycles, its discharge capacity reduction by 50%, and the battery of embodiment 2 Tested by 300 charge and discharge cycles, its discharge capacity reduction by 40%, compared to the capacity attenuation degree few 10% of comparative example, improve electricity Capacity attenuation in the cyclic process of pond.

Claims (3)

1. a kind of all-vanadium flow battery, including anode electrolyte and electrolyte liquid, it is characterised in that:It is total in anode electrolyte and electrolyte liquid Vanadium amount is identical, and vanadium ion concentration is 1.1~1.5 times of vanadium ion concentration in electrolyte liquid in anode electrolyte.
2. battery according to claim 1, it is characterised in that:Vanadium ion concentration is vanadium ion in electrolyte liquid in the anode electrolyte 1.2~1.3 times of concentration.
3. battery according to claim 1, it is characterised in that:The positive pole vanadium ion concentration is 1.4~1.7 mol/Ls.
CN201510923780.1A 2015-12-13 2015-12-13 A kind of all-vanadium flow battery Pending CN106876763A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510923780.1A CN106876763A (en) 2015-12-13 2015-12-13 A kind of all-vanadium flow battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510923780.1A CN106876763A (en) 2015-12-13 2015-12-13 A kind of all-vanadium flow battery

Publications (1)

Publication Number Publication Date
CN106876763A true CN106876763A (en) 2017-06-20

Family

ID=59178475

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510923780.1A Pending CN106876763A (en) 2015-12-13 2015-12-13 A kind of all-vanadium flow battery

Country Status (1)

Country Link
CN (1) CN106876763A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108091914A (en) * 2018-01-30 2018-05-29 中国工程物理研究院电子工程研究所 A kind of method for slowing down all-vanadium flow battery capacity attenuation and ion permeability test device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108091914A (en) * 2018-01-30 2018-05-29 中国工程物理研究院电子工程研究所 A kind of method for slowing down all-vanadium flow battery capacity attenuation and ion permeability test device
CN108091914B (en) * 2018-01-30 2023-11-03 中国工程物理研究院电子工程研究所 Method for slowing down capacity fade of all-vanadium redox flow battery and ion permeability testing device

Similar Documents

Publication Publication Date Title
CN106450371B (en) A method of recycling failure V electrolyte
JP6231202B2 (en) All vanadium redox flow battery and operation method thereof
CN101997129B (en) Liquid flow battery
CN107112567B (en) Assembly for regenerating electrolyte of flow battery and method for regenerating electrolyte of flow battery using same
CN106299493B (en) A kind of recoverable electrochemical energy storing device
CN112786938B (en) Acid-base mixed high-voltage aqueous zinc battery and zinc flow battery with double dissolution deposition reaction
US9972859B2 (en) Method for preparing cathode electrolyte for redox flow batteries, and redox flow battery
CN109860658B (en) Method for recovering performance of zinc-bromine single flow battery
CN109273786A (en) Utilize the method for sulfuric acid system vanadium cell failure anode electrolyte regeneration V electrolyte
CN103985892B (en) A kind of all-vanadium flow battery
CN102227029B (en) High-concentration vanadium electrolyte and preparation method thereof
CN102544563B (en) Zinc-deposition type liquid flow energy-storage battery system and running way thereof
CN113820610A (en) Method and system for detecting health state of all-vanadium redox flow battery after mixing
CN102881932B (en) Vanadium redox flow battery electrolyte containing manganese
CN106876763A (en) A kind of all-vanadium flow battery
CN105428730B (en) A kind of online activation method of lead-acid accumulator
US10014545B2 (en) Method for operating redox flow battery
CN108123159A (en) A kind of method for improving all-vanadium flow battery electrolyte liquid stability
CN104300169A (en) Alkaline zinc vanadium flow battery
CN107565151A (en) A kind of renovation process of vanadium redox flow battery electrode activity
KR101861524B1 (en) Redox flow battery
CN109360997A (en) The regeneration method of sulfuric acid system failure V electrolyte
CN109449470A (en) Utilize the method for sulfuric acid system vanadium cell failure electrolyte liquid regeneration V electrolyte
KR20110092860A (en) Sn or ce ion-added electrolytes for soluble lead acid redox flow battery and batteries comprising the same
CN106340664B (en) Full electrolyte of vanadium redox battery and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20170620