Performance parameter testing methods and basic materials for vanadium flow batteries in scientific research literature
Classification:Industrial News
- Author:ZH Energy
- Release time:May-09-2024
【 Summary 】In large-scale energy storage systems, redox flow batteries are a new type of energy storage technology with long lifespan, safety, and high operating efficiency. However, they are currently mainly li
(一)Material parameters of vanadium single cell
The electrode material is the core component of VRFB, which not only provides the active sites required for vanadium ion reactions, but also affects the transport of electrons and active substances. Due to the use of strong acid electrolyte in all vanadium flow batteries, electrode materials should have excellent corrosion resistance, good catalytic activity, high conductivity, outstanding mass transfer characteristics, and certain mechanical strength. Therefore, carbon felt, graphite felt, and carbon paper have been widely studied. Usually, the cross-sectional thickness of carbon felt or graphite felt electrode materials is not less than 3 mm, resulting in a surface resistivity of the electrode in the range of 3-5 Ω cm2. For traditional graphite felt electrodes, in order to ensure high electrolyte permeability and sufficient mechanical strength, the diameter size of graphite fibers is controlled at 10 μ About m.
The diaphragm material should have high proton conductivity, low water molecule and vanadium ion permeability, excellent chemical durability, and certain mechanical strength. In today's scientific research and demonstration application projects, the most commonly used type of membrane is the perfluorinated membrane, represented by the perfluorosulfonic acid proton exchange membrane produced by DuPont in the United States, known as the Nafion membrane. At the same time, inexpensive fluorinated and non fluorinated ion exchange membranes are also widely studied, mainly including polyvinylidene fluoride (PVDF), polyether ether ketone (PEEK), polyimide (PI), polyimide (PBI), polysulfone (PSF), etc.
The electrolyte in an all vanadium flow battery system is composed of a mixture of vanadium ions with different valence states and acidic electrolyte solvents, and is stored in corrosion-resistant storage tanks. Vanadium ions with different valence states are prepared from VOSO4 or V2O5 as raw materials through chemical or electrochemical methods. Meanwhile, due to cost considerations, other vanadium sources such as NH4VO3 are being attempted as raw materials. And electrolyte solvents are usually strong acids, such as hydrochloric acid or sulfuric acid, used to increase the solubility of vanadium active species while supplying the hydrogen ions required for redox reactions. At the same time, various supporting electrolytes such as H3PO4 and CH3SO3H are also being studied, but sulfuric acid is the most commonly used supporting electrolyte in conventional applications.
A current collector is used to collect current and separate electrolytes. An ideal current collector should have good stability, conductivity, and corrosion resistance. The widely used current collectors include metals, graphite plates, and carbon composite materials. In routine laboratory tests, graphite plates and carbon composite materials are mainly used.
The following are some sources of all vanadium battery raw materials used in the scientific research field:
Device and reagent names | Purity/Model | Manufacturer | |
Electrode material | 聚丙烯腈毛毡 | KD-WD220[3] | 凯盾新材料科技有限公司 |
石墨毡 | 厚度5 mm[3] | 辽宁金谷碳材料股份有限公司 | |
聚丙烯腈基碳毡 | 孔隙率90%[2] | 辽宁金谷炭材料股份有限公司 | |
聚丙烯腈基碳毡 | 厚度3 mm/4 mm | 辽宁金谷炭材料股份有限公司 | |
碳毡电极 | /[4] | 甘肃宏伟碳 | |
Diaphragm Material | 质子交换膜 | Nafion 212[2,3] | 美国杜邦公司(美国科慕化学) |
全氟磺酸离子膜 | 55 μm[4] | 朝阳华鼎有限公司 | |
聚醚醚酮SPEEK | 55.0μm[1] | 英国Victrex公司 | |
聚砜 | P3500[4] | Solvay Advanced Polymers | |
聚苯并咪唑PBI | 99%[1] | 苏州友群塑化有限公司 | |
聚苯并咪唑PBI | AR[6] | 上海盛钧塑胶科技有限公司 | |
electrolyte | VOSO4·6H2O | 99.9 %[3] | 默克Sigma-Aldrich公司 |
VOSO4·6H2O | 99.9 %[2,4]、97%[1] | 沈阳市海中天精细化工厂 | |
浓硫酸 | AR,98%[2,3] | 国药集团化学试剂有限公司 | |
浓硫酸 | 98% | 大连海运试剂厂 | |
浓盐酸 | AR[4] | 天津市富宇精细化工有限公司 | |
Bipolar plate | 高纯石墨板 | HP-100[3] | 沈阳化学品有限公司 |
高密度石墨板 | 1.9 g cm-3[3] | 上海弘俊有限公司 | |
Battery testing system | CT-3008[2,3] | 深圳市新威尔电子有限公司 | |
Electrochemical workstation | Ref 600[2,3] | 美国Gamry公司 |
(二) Vanadium battery and stack parameters and testing
Single battery | (1) Parameters: The electrolyte composition is 1.7 M total vanadium ions+3 M sulfuric acid, with a flow rate of 40 mL/min; The volume of half cell electrolyte is 45 mL; The flow frame is made of polyvinyl chloride and PVC; | / |
(1) Parameters: Using graphite plate as the current collector and graphite felt as the electrode, the effective area of the membrane is 14 cm2. The initial electrolytes for both positive and negative electrodes are the same, consisting of H2SO4 solutions containing 1.7 mol · L-1 of VN+(where the molar ratio of V3+/V4+is 1:1) and 4.5 mol · L-1 of SO42-. The volume of both positive and negative electrolytes is 50 ml, and the electrolyte flow rate is 30 ml · min-1. | (1) For self discharge testing, a single battery with Nafion 115 as the exchange membrane takes approximately 41 hours. | |
(1) Parameters: In a single battery, two graphite felt pieces have a size of 30 mm x 30 mm x 2.2 mm. Two graphite bipolar plates and two copper plates together serve as the current collector, and all components are clamped by two carbon steel plates with bolts. The electrolyte for the positive and negative electrodes is 25 mL of 1.65 M VO2+/V3+(VO2+/V3+=1:1) in a 3 M H2SO4 solution, with a circulating flow rate of 40 mL · min-1. | (1) For self discharge testing, a single battery with Nafion 212 as the exchange membrane takes approximately 19.5 hours. | |
Laboratory Small Module | (1) Parameters: Electrolyte volume 180 mL, flow rate 160 mL/min; The electrical connection is two series and two parallel (series x parallel=2 x 2); |
|
Fuel cell stack | (1) Parameters: Electrolyte volume 160 L (32 kW stack), flow rate 5 m3/h; Number of monomers 60; (2) Charging and discharging test: The charging process adopts a stepped current method, and the discharging process adopts a constant power method. Firstly, the initial current of 405 A is used to charge the stack to a voltage of 96 V, and then the current is reduced to 155 A to continue charging until the voltage rises again to 96 V, and the charging is cut off; Discharge at a constant power of 32 kW to a voltage of 66 V, with discharge cut-off (Jiangsu Jinfan Power Technology Co., Ltd., KC-XCF08) [5]. | / |
Energy storage module | (1) Parameters: Electrolyte volume 8 m3 (250 kW energy storage module), flow rate 40 m3/h; The number of stack assemblies is 8; The electrical connection of the fuel cell stack is four series and two parallel (series x parallel=4 x 2); | The charging capacity varies significantly among different stack arrangements, with a maximum of 1491 Ah and a minimum of 1341 Ah, with a difference of nearly 10%. |
In order to promote the overall development of the liquid flow battery industry and achieve the large-scale implementation of liquid flow energy storage systems, the ZH Energy Storage Long Term Energy Storage Research Institute has launched a series of products from the liquid flow battery research and development laboratory to assist the product research and development of various universities and enterprises in the industry. ZH Energy Storage Laboratory Product Series: 3W and 20W series single batteries; 1 kW, 5 kW, and 32 kW fuel cells; 5kW/20kWh energy storage systems and specialized BMS products for liquid flow energy storage systems.
详细介绍请点击以下链接:
[1] Zhang Denghua Reasonable construction and performance study of proton channels in separators for all vanadium flow batteries [D]. University of Science and Technology of China, 2023. DOI: 10.27517/dcnki.gzkju.2023.000885
[2] Open up and enjoy Dynamics testing and performance optimization of carbon based electrodes in vanadium batteries [D]. University of Science and Technology of China, 2023. DOI: 10.27517/dcnki. gzkju. 2022-000510
[3] Xu Zeyu Structural design and preparation of electrodes for high-performance vanadium flow batteries [D]. University of Science and Technology of China, 2023. DOI: 10.27517/dcnki.gzkju.2021.001977
[4] Zhang Daishuang Design and regulation of narrow ion channel asymmetric membranes for all vanadium flow batteries [D]. Dalian University of Technology, 2022. DOI: 10.26991/dcnki.gdllu.2020.004128
[5] Chen Hui Design and optimization of energy storage modules for flow batteries [D]. University of Science and Technology of China, 2020. DOI: 10.27517/dcnki. gzkju. 2019
[6] Yang Xiaobing Performance study of proton exchange membrane for all vanadium flow battery based on phosphotungstic acid anchoring [D]. Harbin Institute of Technology, 2020. DOI: 10.27061/d. cnki. ghgdu. 2019. 000526