CN105742658B - The preparation method of electrode material for all-vanadium flow battery - Google Patents
The preparation method of electrode material for all-vanadium flow battery Download PDFInfo
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- 229910052720 vanadium Inorganic materials 0.000 title claims abstract description 33
- 239000007772 electrode material Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 238000001035 drying Methods 0.000 claims abstract description 15
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000002994 raw material Substances 0.000 claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 45
- 239000010439 graphite Substances 0.000 claims description 28
- 229910002804 graphite Inorganic materials 0.000 claims description 28
- 229910052799 carbon Inorganic materials 0.000 claims description 17
- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical compound N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 claims description 9
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 8
- 239000004202 carbamide Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000008367 deionised water Substances 0.000 claims description 6
- 229910021641 deionized water Inorganic materials 0.000 claims description 6
- 229920000877 Melamine resin Polymers 0.000 claims description 5
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 5
- 238000012986 modification Methods 0.000 claims description 5
- 230000004048 modification Effects 0.000 claims description 5
- 239000004744 fabric Substances 0.000 claims description 4
- XZMCDFZZKTWFGF-UHFFFAOYSA-N Cyanamide Chemical compound NC#N XZMCDFZZKTWFGF-UHFFFAOYSA-N 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- 150000001721 carbon Chemical class 0.000 claims 3
- 238000005255 carburizing Methods 0.000 claims 3
- 238000002791 soaking Methods 0.000 claims 1
- 238000000527 sonication Methods 0.000 claims 1
- 239000002243 precursor Substances 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 9
- 239000003575 carbonaceous material Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 125000000524 functional group Chemical group 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000003792 electrolyte Substances 0.000 abstract 1
- 238000003763 carbonization Methods 0.000 description 9
- 238000009210 therapy by ultrasound Methods 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 238000010306 acid treatment Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- SKKMWRVAJNPLFY-UHFFFAOYSA-N azanylidynevanadium Chemical compound [V]#N SKKMWRVAJNPLFY-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 229910001456 vanadium ion Inorganic materials 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
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- H01M4/90—Selection of catalytic material
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- H01M4/9083—Catalytic material supported on carriers, e.g. powder carriers on carbon or graphite
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- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
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Abstract
本发明涉及液流电池电极材料的制备方法,特别涉及全钒液流电池用电极材料的制备方法。该方法的实现过程为:将碳素类材料浸入到一定浓度的含氮类原料中,经超声、干燥处理得到一种目标电极的前驱体,然后高温碳化上述前驱体,即得目标电极。如此经过修饰的电极材料其表面的含氮官能团得到了大幅度提升,其电化学活性和导电性都得到了提高,减小了全钒液流电池用电极的反应内阻,同时增加了电极与电解液的反应活性位点,从而极大地提高了全钒液流电池的电压效率和能量效率。本发明的电极制备过程简单、原料易得、成本低廉,性能稳定可进行大批量生产。The invention relates to a preparation method of an electrode material for a liquid flow battery, in particular to a preparation method for an electrode material for an all-vanadium redox flow battery. The realization process of the method is: immerse the carbon material into a certain concentration of nitrogen-containing raw materials, obtain a precursor of the target electrode through ultrasonic and drying treatment, and then carbonize the above precursor at high temperature to obtain the target electrode. The nitrogen-containing functional groups on the surface of the modified electrode material have been greatly improved, and its electrochemical activity and conductivity have been improved, reducing the reaction internal resistance of the electrode used in the all-vanadium redox flow battery, and at the same time increasing the electrode's contact with the electrode. The reactive active sites of the electrolyte greatly improve the voltage efficiency and energy efficiency of the all-vanadium redox flow battery. The electrode preparation process of the invention is simple, the raw material is easy to obtain, the cost is low, the performance is stable and mass production can be carried out.
Description
技术领域technical field
本发明涉及液流电池电极材料的制备方法,特别涉及全钒液流电池用电极材料的制备方法。The invention relates to a preparation method of an electrode material for a liquid flow battery, in particular to a preparation method for an electrode material for an all-vanadium redox flow battery.
背景技术Background technique
液流电池因其系统设计灵活,输出功率和容量相对独立,使用寿命长,可大电流充放电,且整体性能稳定。液流电池特别是全钒液流电池被认为是解决太阳能和风能等间歇性、不稳定功率资源的一种有效方法。Due to its flexible system design, relatively independent output power and capacity, the flow battery has a long service life, can be charged and discharged with a large current, and has stable overall performance. Flow batteries, especially all-vanadium flow batteries, are considered to be an effective method to solve intermittent and unstable power resources such as solar and wind energy.
自1985年M.Skyllas-kazacos等开始研究全钒氧化还原液流电池以来,全钒液流电池得到了巨大的发展,其用VO2 +/VO2+和V2+/V3+氧化还原电对在硫酸溶液中分别作为正负极,表现出了宽的开路电压和可深度放电等电化学特性。全钒液流电池所用的典型材料为一些碳素类材料:包括碳毡、碳布和石墨毡等。该类材料具有宽的操作电压窗口,比表面积大,稳定性好以及合理的价格等优点。然而,上述碳素类材料存在电化学活性低和较差的反应动力可逆性等问题。Since M.Skyllas-kazacos et al. began to study the all-vanadium redox flow battery in 1985, the all-vanadium redox flow battery has been greatly developed. It uses VO 2 + /VO 2+ and V 2+ /V 3+ redox The electrode pair is used as positive and negative electrodes respectively in sulfuric acid solution, and exhibits electrochemical characteristics such as wide open circuit voltage and deep discharge. Typical materials used in all-vanadium redox flow batteries are some carbon materials: including carbon felt, carbon cloth and graphite felt. This type of material has the advantages of wide operating voltage window, large specific surface area, good stability and reasonable price. However, the above-mentioned carbon-based materials have problems such as low electrochemical activity and poor reversibility of reaction kinetics.
为了提高上述材料的电化学活性,国内外对其改性做了大量的研究。包括:热处理、酸处理和贵金属修饰等方法。热处理操作过程繁杂,氧化过程不易控制,过度氧化会降低电极材料的使用寿命和稳定性。酸处理主要是利用浓硫酸、浓硝酸对电极材料进行较长时间的处理,全钒液流电池的能量效率得到了大幅度提升,但是处理后产生大量废酸,对环境造成极大污染。贵金属修饰因其需要烧结且工艺复杂,成本较高,难于大规模制备。In order to improve the electrochemical activity of the above materials, a lot of research has been done on their modification at home and abroad. Including: heat treatment, acid treatment and precious metal modification and other methods. The heat treatment process is complicated, and the oxidation process is difficult to control. Excessive oxidation will reduce the service life and stability of the electrode material. Acid treatment mainly uses concentrated sulfuric acid and concentrated nitric acid to treat electrode materials for a long time. The energy efficiency of all-vanadium redox flow batteries has been greatly improved, but a large amount of waste acid is produced after treatment, which causes great pollution to the environment. Noble metal modification is difficult to prepare on a large scale due to the need for sintering and the complicated process and high cost.
石墨相氮化碳因为具有优良的化学稳定性和独特的电子结构,近年来,作为不含金属的催化剂和催化剂载体被广泛的研究。在光催化分解水,氧还原,作为绿色储能材料和硬模板剂用于H2和CO2的存储等方面都取得了重要进展。Graphite carbon nitride has been extensively studied as a metal-free catalyst and catalyst support in recent years because of its excellent chemical stability and unique electronic structure. Significant progress has been made in photocatalytic water splitting, oxygen reduction, as green energy storage materials and hard templating agents for H2 and CO2 storage.
发明内容Contents of the invention
本发明的目的是为了解决上述全钒液流电池电极材料存在的活性低和差的反应动力可逆性问题,提出了一种全钒液流电池电极的修饰方法,其电极制备工艺简单,成本低廉,可进行工业批量生产。The purpose of the present invention is to solve the problem of low activity and poor reaction kinetic reversibility of the above-mentioned all-vanadium redox flow battery electrode materials, and propose a modification method for all-vanadium redox flow battery electrodes. The electrode preparation process is simple and the cost is low. , for industrial mass production.
为了实现上述目的,本发明采用的技术方案为:一种全钒液流电池用电极材料的制备方法,其包括如下步骤:In order to achieve the above object, the technical solution adopted in the present invention is: a preparation method of an electrode material for an all-vanadium redox flow battery, which comprises the following steps:
(1)将碳素类材料浸入含氮类原料的溶液中进行超声处理5~40min;(1) Immerse the carbonaceous material in the solution of nitrogen-containing raw materials for ultrasonic treatment for 5~40min;
(2)将经步骤(1)处理的碳素类材料放在烘箱中干燥,干燥温度为80~120℃,干燥时间8~16h,得到目标电极的前驱体;(2) Dry the carbonaceous material treated in step (1) in an oven at a drying temperature of 80-120°C and a drying time of 8-16 hours to obtain the precursor of the target electrode;
(3)将步骤(2)中所得目标电极的前驱体置于管式炉或马弗炉中碳化,碳化温度为450~600℃,升温速率3~8℃/min,温度升到碳化温度后保温1~6h,即得到石墨相氮化碳修饰的全钒液流电池用目标电极材料。(3) Place the precursor of the target electrode obtained in step (2) into a tube furnace or muffle furnace for carbonization. The carbonization temperature is 450~600°C, and the heating rate is 3~8°C/min. After the temperature rises to the carbonization temperature After heat preservation for 1-6 hours, the target electrode material for all-vanadium redox flow battery modified by graphite phase carbon nitride can be obtained.
上述方案中,所述的含氮类原料为尿素、三聚氰胺或单氰胺等材料,优选尿素溶液。In the above solution, the nitrogen-containing raw materials are materials such as urea, melamine or cyanamide, preferably urea solution.
上述方案中,所述碳素类材料为碳毡、碳布、碳纸或石墨毡等,优选石墨毡。In the above solution, the carbonaceous material is carbon felt, carbon cloth, carbon paper or graphite felt, preferably graphite felt.
上述方案中,所述含氮类原料的溶液浓度为0.001~1g/ml。In the above scheme, the solution concentration of the nitrogen-containing raw materials is 0.001-1 g/ml.
上述方案中,所述含氮类原料的溶液的溶剂为去离子水。In the above scheme, the solvent of the nitrogen-containing raw material solution is deionized water.
上述方案中,步骤(1)中所述超声处理时间优选15min。In the above scheme, the ultrasonic treatment time in step (1) is preferably 15 minutes.
上述方案中,步骤(2)中所述干燥温度优选为100℃。In the above scheme, the drying temperature in step (2) is preferably 100°C.
上述方案中,步骤(3)中所述在管式炉中或马弗炉中碳化温度优选为550℃。In the above solution, the carbonization temperature in the tube furnace or muffle furnace in step (3) is preferably 550°C.
上述方案中,步骤(3)中所述在管式炉中或马弗炉中保温时间优选为1h。In the above scheme, the holding time in the tube furnace or muffle furnace in step (3) is preferably 1 h.
本发明通过高温碳化将石墨相氮化碳原位生长于目标电极表面,因为石墨相氮化碳含有丰富的四元氮结构,四元氮在酸性环境中比较稳定,又由于氮元素的电负性易对钒离子进行吸附,形成一种氮-钒过渡态,方便离子的传输与电荷的转移,从而提高了全钒液流电池电极材料的电化学活性,提升了全钒液流电池的电压效率和能量效率。The present invention grows graphite phase carbon nitride in situ on the surface of the target electrode through high temperature carbonization, because graphite phase carbon nitride contains rich quaternary nitrogen structure, quaternary nitrogen is relatively stable in acidic environment, and due to the electronegativity of nitrogen It is easy to adsorb vanadium ions to form a nitrogen-vanadium transition state, which facilitates the transport of ions and the transfer of charges, thereby improving the electrochemical activity of the electrode material of the all-vanadium redox flow battery and increasing the voltage of the all-vanadium redox flow battery efficiency and energy efficiency.
本发明具有如下优点:The present invention has the following advantages:
(1)本发明制备的电极材料,由于石墨相氮化碳的修饰增加了电极表面的含氮官能团,引入了更多的反应活性位,提升了电催化活性和反应动力可逆性。(1) The electrode material prepared by the present invention increases the nitrogen-containing functional groups on the surface of the electrode due to the modification of the graphite phase carbon nitride, introduces more reactive sites, and improves the electrocatalytic activity and the reversibility of the reaction kinetics.
(2)本发明制备的电极材料由于电极表面含氮官能团的增加,改善了碳素类材料(碳毡、碳布、碳纸或石墨毡等)的亲水性,并且增加了电极材料的导电性,从而提升了全钒液流电池的能量效率和电压效率。(2) The electrode material prepared by the present invention improves the hydrophilicity of carbon materials (carbon felt, carbon cloth, carbon paper or graphite felt, etc.) due to the increase of nitrogen-containing functional groups on the electrode surface, and increases the conductivity of the electrode material. performance, thereby improving the energy efficiency and voltage efficiency of the all-vanadium redox flow battery.
(3)本发明工艺过程简单,原料易得,且反应时间短,操作灵活方便,易于规模化生产。(3) The process of the present invention is simple, the raw materials are readily available, the reaction time is short, the operation is flexible and convenient, and it is easy for large-scale production.
附图说明Description of drawings
图1是本发明所修饰的石墨毡电极与空白石墨毡电极在100 mA/cm2电流密度下充放电曲线图,从图中可以看出,本发明利用石墨相氮化碳修饰的石墨毡电极具有非常优异的电化学性能。Fig. 1 is the graphite felt electrode modified by the present invention and the blank graphite felt electrode under 100 mA/cm Current density charge and discharge curve figure, as can be seen from the figure, the present invention utilizes the graphite felt electrode modified by graphite phase carbon nitride It has very excellent electrochemical performance.
图2是本发明所修饰的石墨毡电极与空白石墨毡电极在150 mA/cm2电流密度下充放电曲线图,从图中可以看出,本发明所制备的电极在大电流密度下相对于空白毡表现出了良好的电化学性能。Fig. 2 is the graphite felt electrode modified by the present invention and the blank graphite felt electrode under 150 mA/cm Current density charge - discharge graph, as can be seen from the figure, the prepared electrode of the present invention is relative to The blank felt showed good electrochemical performance.
图3是空白组石墨毡与本发明制成的石墨相氮化碳修饰的石墨毡扫描电镜比较图,表明氧化石墨相氮化碳成功的负载在石墨毡纤维表面。Fig. 3 is a scanning electron microscope comparison between the graphite felt of the blank group and the graphite felt modified by the graphite phase carbon nitride of the present invention, showing that the graphite oxide phase carbon nitride is successfully loaded on the surface of the graphite felt fiber.
具体实施方式detailed description
下面通过具体实例实例详述本发明。The present invention is described in detail below by specific examples.
实施实例一:Implementation example one:
取4g三聚氰胺溶于50ml去离子水中,在烧杯中搅拌溶解,将一定面积的石墨毡电极置于溶液中,使其完全浸没。然后,将烧杯放入超声仪中进行超声处理,超声时间为10min,使三聚氰胺溶液均匀分散于石墨毡电极中。随后,将石墨毡电极取出,放在蒸发皿上,在烘箱中干燥,干燥温度为80℃,干燥时间为14h,得到目标电极前驱体。然后,将该目标电极前驱体放入管式炉中碳化,升温速率为4℃/min,待温度升至550℃,保温3h,即得全钒液流电池用的电极材料。为了测试该电极的电化学性能,将该电极组装电池进行充放电测试,在50mA/cm2电流密度下,全钒液流电池的电压效率为89.7%,能量效率为88.3%。Take 4g of melamine and dissolve it in 50ml of deionized water, stir and dissolve in a beaker, place a certain area of graphite felt electrode in the solution, and make it completely submerged. Then, put the beaker into an ultrasonic instrument for ultrasonic treatment, and the ultrasonic time is 10 minutes, so that the melamine solution is uniformly dispersed in the graphite felt electrode. Subsequently, the graphite felt electrode was taken out, placed on an evaporating dish, and dried in an oven at a drying temperature of 80° C. and a drying time of 14 hours to obtain the target electrode precursor. Then, put the target electrode precursor into a tube furnace for carbonization at a heating rate of 4°C/min, wait for the temperature to rise to 550°C, and keep it warm for 3 hours to obtain the electrode material for the all-vanadium redox flow battery. In order to test the electrochemical performance of the electrode, the battery assembled with the electrode was charged and discharged. At a current density of 50mA/cm 2 , the voltage efficiency of the all-vanadium redox flow battery was 89.7%, and the energy efficiency was 88.3%.
实施实例二:Implementation example two:
取6g尿素溶于50ml去离子水中,在烧杯中搅拌溶解,将一定面积的石墨毡电极置于溶液中,使其完全浸没。然后,将烧杯放入超声仪中进行超声处理,超声时间为15min,使尿素溶液均匀分散于石墨毡电极中。随后,将石墨毡电极取出,放在蒸发皿上,在烘箱中干燥,干燥温度为100℃,干燥时间为12h,得到目标电极前驱体。然后,将该目标电极前驱体放入管式炉中碳化,升温速率为5℃/min,待温度升至550℃,保温2h,即得全钒液流电池用的电极材料。为了测试该电极的电化学性能,将该电极组装电池进行充放电测试,在100mA/cm2电流密度下,全钒液流电池的电压效率为80.2%,能量效率为78.3%。Dissolve 6g of urea in 50ml of deionized water, stir and dissolve in a beaker, place a certain area of graphite felt electrode in the solution, and make it completely submerged. Then, the beaker was put into an ultrasonic instrument for ultrasonic treatment, and the ultrasonic time was 15 minutes, so that the urea solution was uniformly dispersed in the graphite felt electrode. Subsequently, the graphite felt electrode was taken out, placed on an evaporating dish, and dried in an oven at a drying temperature of 100° C. and a drying time of 12 hours to obtain the target electrode precursor. Then, put the target electrode precursor into a tube furnace for carbonization at a heating rate of 5°C/min, wait for the temperature to rise to 550°C, and keep it warm for 2 hours to obtain an electrode material for an all-vanadium redox flow battery. In order to test the electrochemical performance of the electrode, the battery assembled with the electrode was charged and discharged. Under the current density of 100mA/cm 2 , the voltage efficiency of the all-vanadium redox flow battery was 80.2%, and the energy efficiency was 78.3%.
实施实例三:Implementation example three:
取10g尿素溶于50ml去离子水中,在烧杯中搅拌溶解,将一定面积的碳毡电极置于溶液中,使其完全浸没。然后,将烧杯放入超声仪中进行超声处理,超声时间为15min,使尿素溶液均匀分散于碳毡电极中。随后,将碳毡电极取出,放在蒸发皿上,在烘箱中干燥,干燥温度为120℃,干燥时间为10h,得到目标电极前驱体。然后,将该目标电极前驱体放入管式炉中碳化,升温速率为6℃/min,待温度升至550℃,保温1h,即得全钒液流电池用的电极材料。为了测试该电极的电化学性能,将该电极组装电池进行充放电测试,在120mA/cm2电流密度下,全钒液流电池的电压效率为75.1%,能量效率为74.2%。Dissolve 10g of urea in 50ml of deionized water, stir and dissolve in a beaker, place a certain area of carbon felt electrode in the solution, and make it completely submerged. Then, the beaker was put into an ultrasonic instrument for ultrasonic treatment, and the ultrasonic time was 15 minutes, so that the urea solution was uniformly dispersed in the carbon felt electrode. Subsequently, the carbon felt electrode was taken out, placed on an evaporating dish, and dried in an oven at a drying temperature of 120° C. and a drying time of 10 h to obtain the target electrode precursor. Then, put the target electrode precursor into a tube furnace for carbonization at a heating rate of 6°C/min, wait for the temperature to rise to 550°C, and keep it warm for 1 hour to obtain the electrode material for the all-vanadium redox flow battery. In order to test the electrochemical performance of the electrode, the battery assembled with the electrode was charged and discharged. At a current density of 120mA/cm 2 , the voltage efficiency of the all-vanadium redox flow battery was 75.1%, and the energy efficiency was 74.2%.
实施实例四:Implementation example four:
取10g三聚氰胺溶于50ml去离子水中,在烧杯中搅拌溶解,将一定面积的碳毡电极置于溶液中,使其完全浸没。然后,将烧杯放入超声仪中进行超声处理,超声时间为20min,使尿素溶液均匀分散于碳毡电极中。随后,将碳毡电极取出,放在蒸发皿上,在烘箱中干燥,干燥温度为120℃,干燥时间为10h,得到目标电极前驱体。然后,将该目标电极前驱体放入管式炉中碳化,升温速率为4℃/min,待温度升至500℃,保温2h,即得全钒液流电池用的电极材料。为了测试该电极的电化学性能,将该电极组装电池进行充放电测试,在150mA/cm2电流密度下,全钒液流电池的电压效率为66.8%,能量效率为65.6%。Take 10g of melamine and dissolve it in 50ml of deionized water, stir and dissolve in a beaker, place a certain area of carbon felt electrode in the solution, and make it completely submerged. Then, the beaker was placed in an ultrasonic instrument for ultrasonic treatment, and the ultrasonic time was 20 min, so that the urea solution was uniformly dispersed in the carbon felt electrode. Subsequently, the carbon felt electrode was taken out, placed on an evaporating dish, and dried in an oven at a drying temperature of 120° C. and a drying time of 10 h to obtain the target electrode precursor. Then, put the target electrode precursor into a tube furnace for carbonization at a heating rate of 4°C/min, wait for the temperature to rise to 500°C, and keep it warm for 2 hours to obtain an electrode material for an all-vanadium redox flow battery. In order to test the electrochemical performance of the electrode, the battery assembled with the electrode was charged and discharged. Under the current density of 150mA/cm 2 , the voltage efficiency of the all-vanadium redox flow battery was 66.8%, and the energy efficiency was 65.6%.
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