CN111509238A - A kind of preparation method of macroscopic graphene modified electrode material - Google Patents

A kind of preparation method of macroscopic graphene modified electrode material Download PDF

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CN111509238A
CN111509238A CN202010200890.6A CN202010200890A CN111509238A CN 111509238 A CN111509238 A CN 111509238A CN 202010200890 A CN202010200890 A CN 202010200890A CN 111509238 A CN111509238 A CN 111509238A
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carbon felt
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graphene modified
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CN111509238B (en
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丁美
龙婷
孙其君
张怡琼
贾传坤
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Changsha University of Science and Technology
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/88Processes of manufacture
    • H01M4/8825Methods for deposition of the catalytic active composition
    • H01M4/8867Vapour deposition
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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    • H01M8/18Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
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Abstract

The invention discloses a preparation method of a macroscopic quantity graphene modified electrode material, relates to the field of electrode materials for all vanadium redox flow batteries (VRB), in particular to a preparation method of a high-performance macroscopic quantity graphene modified carbon felt suitable for all vanadium redox flow batteries, and solves the problems of poor conductivity, low specific surface area, low electrochemical activity, poor catalytic performance of vanadium ion electric pairs, low performance of single cells, high cost and the like of commercial carbon felts for vanadium batteries at the present stage. The invention takes a commercial carbon felt as a raw material and utilizes a Chemical Vapor Deposition (CVD) method to prepare the graphene modified carbon felt. The composite carbon felt prepared by the invention has the advantages of good conductivity, high specific surface area, good electrochemical catalytic performance, excellent chemical stability, good VRB battery performance, low cost and the like. The preparation method has the advantages of simple and easy operation, low product cost, easy industrial production, environmental protection and the like, and can be widely applied to the field of all-vanadium redox flow batteries.

Description

一种宏量石墨烯改性电极材料的制备方法A kind of preparation method of macroscopic graphene modified electrode material

技术领域:Technical field:

本发明涉及全钒氧化还原液流电池(VRB)用电极材料领域,具体是一种适用于全钒氧化还原液流电池的高性能宏量石墨烯改性电极材料的制备方法。The invention relates to the field of electrode materials for all-vanadium redox flow batteries (VRB), in particular to a preparation method of a high-performance macro-scale graphene modified electrode material suitable for all-vanadium redox flow batteries.

背景技术:Background technique:

随着全球人口的快速增长和经济的高速发展,能源危机日益严重。开发新能源是解决能源危机的有效途径。可再生清洁能源因为环境友好和可持续性是目前科学研究和工业开发的热点。风能和太阳能等可再生能源发电过程显现出不连续性和不稳定性的缺点。为此,亟待开发高效、环保、低成本和安全可靠的大规模储能技术。全钒氧化还原液流电池(VRB)因其功率和能量独立、设计简单灵活、循环寿命长、可快速充放电、运行成本低等优点,而被广泛地应用于风能、太阳能发电过程的大规模储能设备。同时,VRB近几年也是电站储能、电网调峰等领域广泛试用的大规模储能技术。然而,目前钒电池商业化进展受到高成本的制约。其中,电极材料是决定电堆成本高低的关键因素。一种适用于钒电池的电极材料应具备优良的电导率、高比表面积、优越的电化学活性和成本低廉等优点。传统金属材料电极的电化学可逆性差,且易被酸性电解液钝化;而铂、铱等贵金属虽然具有电化学活性高、催化性能好和化学稳定性好等优点,但这类材料价格昂贵,制约其在钒电池中大规模应用。现阶段,钒电池应用最广泛采用的电极材料为碳类材料,如:石墨毡、石墨、碳布和碳纤维等。然而,这类碳材料直接应用过程中存在电导率低,电化学活性差以及电池性能差等问题。鉴于此,必须对此类碳基材料进行改性处理,以提高电极的电导率和电化学活性。截至目前,仍然没有一种合适方法能够解决这些关键问题。With the rapid growth of the global population and rapid economic development, the energy crisis is becoming more and more serious. The development of new energy is an effective way to solve the energy crisis. Renewable and clean energy is currently a hot spot in scientific research and industrial development because of its environmental friendliness and sustainability. Renewable energy generation processes such as wind and solar show the disadvantages of discontinuity and instability. Therefore, it is urgent to develop efficient, environmentally friendly, low-cost, safe and reliable large-scale energy storage technologies. All-vanadium redox flow batteries (VRBs) are widely used in large-scale wind and solar power generation processes due to their power and energy independence, simple and flexible design, long cycle life, fast charge and discharge, and low operating costs. energy storage equipment. At the same time, VRB is also a large-scale energy storage technology widely tried in the fields of power station energy storage and power grid peak regulation in recent years. However, the commercialization of vanadium batteries is currently limited by high costs. Among them, the electrode material is the key factor that determines the cost of the stack. An electrode material suitable for vanadium batteries should have the advantages of excellent electrical conductivity, high specific surface area, superior electrochemical activity and low cost. Electrodes of traditional metal materials have poor electrochemical reversibility and are easily passivated by acidic electrolytes; while noble metals such as platinum and iridium have the advantages of high electrochemical activity, good catalytic performance and good chemical stability, but such materials are expensive, It restricts its large-scale application in vanadium batteries. At present, the most widely used electrode materials for vanadium batteries are carbon materials, such as graphite felt, graphite, carbon cloth and carbon fiber. However, the direct application of such carbon materials has problems such as low electrical conductivity, poor electrochemical activity, and poor battery performance. In view of this, such carbon-based materials must be modified to improve the electrical conductivity and electrochemical activity of electrodes. As of now, there is still no suitable method to solve these key problems.

发明内容:Invention content:

为了克服现有技术的不足,本发明目的在于提供一种适用于钒电池的宏量石墨烯改性电极材料的制备方法,解决现有技术中存在的碳毡电导率差、化学活性低、比表面积低、稳定性差、在VRB中性能差以及造成VRB成本高等问题。采用该方法可获得低成本高性能的复合碳毡,其具有电导率高、比表面积高、电化学活性高、对钒离子催化性能好、稳定性好,以及VRB电池应用中性能好等优点。In order to overcome the deficiencies of the prior art, the object of the present invention is to provide a method for preparing a macro-scale graphene modified electrode material suitable for vanadium batteries, which solves the problems of poor electrical conductivity, low chemical activity, and low carbon felt in the prior art. Low surface area, poor stability, poor performance in VRB and high cost of VRB. Using this method, a low-cost and high-performance composite carbon felt can be obtained, which has the advantages of high electrical conductivity, high specific surface area, high electrochemical activity, good catalytic performance for vanadium ions, good stability, and good performance in VRB battery applications.

本发明的具体技术方案:Concrete technical scheme of the present invention:

一种宏量石墨烯改性电极材料的制备方法,包括如下步骤和工艺条件:A preparation method of a macroscopic graphene modified electrode material, comprising the following steps and process conditions:

(1)将干燥处理的碳毡浸泡在酸溶液中,常温浸泡一定时间,随后超声震荡一定时间;其中,在酸溶液中浸泡碳毡的时间为12~18h,超声震荡时间为0.5~1.5h;(1) Soak the dried carbon felt in an acid solution, soak it at room temperature for a certain period of time, and then ultrasonically vibrate it for a certain period of time; wherein, the time for soaking the carbon felt in the acid solution is 12-18h, and the ultrasonic oscillation time is 0.5-1.5h ;

(2)将步骤(1)中的碳毡,反复用去离子水清洗;(2) the carbon felt in step (1) is repeatedly cleaned with deionized water;

(3)将清洗后的碳毡进行干燥处理;(3) drying the cleaned carbon felt;

(4)将20cm×20cm×5.5mm碳毡放入制备室内底部的石墨匀热样品台上,并将样品对准制备室内顶部的气体出口方向;(4) Put the 20cm×20cm×5.5mm carbon felt on the graphite uniform heating sample stage at the bottom of the preparation chamber, and align the sample with the gas outlet direction at the top of the preparation chamber;

(5)开启制备室上的H2阀门,清洗1~3min,关闭H2阀门;(5) Open the H2 valve on the preparation chamber, clean it for 1-3 minutes, and close the H2 valve;

(6)开启制备室上的CH4阀门,清洗1~3min,关闭CH4阀门;(6) Open the CH 4 valve on the preparation chamber, clean it for 1 to 3 minutes, and close the CH 4 valve;

(7)开启制备室上的高真空阀,手动开启高真空机组,抽真空4~6min,使制备室内的真空度为2.5×10-2~3×10-3Pa;关闭高真空阀,手动关闭高真空机组;(7) Open the high vacuum valve on the preparation chamber, manually open the high vacuum unit, and evacuate for 4 to 6 minutes, so that the vacuum degree in the preparation chamber is 2.5×10 -2 to 3×10 -3 Pa; close the high vacuum valve and manually Turn off the high vacuum unit;

(8)开启H2阀门,调整气体流量为150~200sccm,将制备室加热升温至温度为1000±10℃,升温时间为100~120min;( 8 ) open the H valve, adjust the gas flow to be 150~200sccm, heat the preparation chamber to a temperature of 1000±10°C, and the temperature rise time is 100~120min;

(9)在1000±10℃保温,时间5~20min;(9) Keep the temperature at 1000±10℃ for 5-20min;

(10)在保温时间内,打开CH4阀门,调整气体流量为20~30sccm,维持反应时间为5~20min;(10) During the holding time, open the CH4 valve, adjust the gas flow to 20~30sccm, and maintain the reaction time to be 5~20min;

(11)关闭CH4阀门,维持H2流量为150~200sccm,随炉冷却;(11) Close the CH 4 valve, maintain the H 2 flow at 150-200sccm, and cool with the furnace;

(12)温度降至室温后,关闭H2阀门,获得石墨烯改性碳毡样品。(12) After the temperature dropped to room temperature, the H valve was closed to obtain a graphene - modified carbon felt sample.

所述的宏量石墨烯改性电极材料的制备方法,步骤(1)中,碳毡干燥处理温度为400~500℃。In the method for preparing the macro-scale graphene-modified electrode material, in step (1), the temperature for drying the carbon felt is 400-500°C.

所述的宏量石墨烯改性电极材料的制备方法,步骤(1)中,酸溶液为硫酸、硝酸和盐酸中的一种,酸溶液浓度为1~3mol/L。In the preparation method of the described macro-scale graphene modified electrode material, in step (1), the acid solution is one of sulfuric acid, nitric acid and hydrochloric acid, and the acid solution concentration is 1-3 mol/L.

所述的宏量石墨烯改性电极材料的制备方法,步骤(2)中,清洗次数为10~15次。In the preparation method of the macro-scale graphene modified electrode material, in step (2), the cleaning times are 10-15 times.

所述的宏量石墨烯改性电极材料的制备方法,步骤(3)中,碳毡干燥温度为80~120℃。In the preparation method of the macro-scale graphene modified electrode material, in step (3), the drying temperature of the carbon felt is 80-120°C.

所述的宏量石墨烯改性电极材料的制备方法,步骤(5)中,清洗次数为3~5次。In the preparation method of the macro-scale graphene modified electrode material, in step (5), the cleaning times are 3 to 5 times.

所述的宏量石墨烯改性电极材料的制备方法,步骤(6)中,清洗次数为3~5次。In the preparation method of the macro-scale graphene modified electrode material, in step (6), the cleaning times are 3 to 5 times.

所述的宏量石墨烯改性电极材料的制备方法,石墨烯改性碳毡中,石墨烯负载量为0.3~1wt%。In the preparation method of the macro-scale graphene-modified electrode material, in the graphene-modified carbon felt, the graphene loading is 0.3-1 wt%.

本发明的设计思想是:本发明以CH4作为碳源,在H2的还原作用与高温下,使CH4裂解,从而得到石墨烯。进一步的,将制得的石墨烯均匀地包覆在碳毡上,从而得到石墨烯碳毡。The design idea of the present invention is: in the present invention, CH4 is used as a carbon source, and under the reduction effect of H2 and high temperature, CH4 is cracked to obtain graphene. Further, the prepared graphene is evenly coated on the carbon felt, thereby obtaining the graphene carbon felt.

与现有技术相比,本发明具有以下显著优点及有益效果:Compared with the prior art, the present invention has the following significant advantages and beneficial effects:

1.本发明以商业碳毡为原料,采用化学气相沉积的方法,制备石墨烯改性碳毡电极材料,该电极材料具有电导率高、比表面积大、钒离子催化性能好、稳定性好、电化学催化活性高等优点。1. the present invention takes commercial carbon felt as raw material, adopts the method for chemical vapor deposition, prepares graphene modified carbon felt electrode material, and this electrode material has high electrical conductivity, large specific surface area, good vanadium ion catalytic performance, good stability, The advantages of high electrochemical catalytic activity.

2.本发明所用制备石墨烯改性碳毡的方法,原料易得且成本低廉、操作简单易行,适合大规模发展。2. The method for preparing the graphene-modified carbon felt used in the present invention has easily available raw materials, low cost, simple and easy operation, and is suitable for large-scale development.

3.本发明整个制备过程中具有设备价格低廉、原料成本低廉易得、操作流程简单便捷等工业实用化特点,有助于VRB的商业化用电极材料的大规模生产。3. The whole preparation process of the present invention has industrial practical features such as low equipment price, low cost of raw materials and easy availability, simple and convenient operation process, etc., which is helpful for the large-scale production of electrode materials for commercialization of VRB.

总之,本发明以商业化碳毡为原料,采用气相沉积法,制备石墨烯改性碳毡复合电极,提高了碳毡的电导率、比表面积、电化学活性、稳定性和电化学催化性能。与未改性商业化碳毡组装的VRB电池对比,采用石墨烯改性碳毡的VRB电池具有高的功率密度(图1),以及高的效率、优越的倍率性能和循环性能(图2)。利用气相沉积法将高比表面积和高电导率的石墨烯均匀沉积到商业化碳毡表面,制备高性能的石墨烯改性碳毡复合电极。这类方法所用原料成本低廉易得,操作简单便捷,并适合大规模产业化发展,有望制备出一种低成本高性能的钒电池用商业化电极材料。In a word, the present invention uses commercial carbon felt as raw material and adopts vapor deposition method to prepare graphene-modified carbon felt composite electrode, which improves the electrical conductivity, specific surface area, electrochemical activity, stability and electrochemical catalytic performance of the carbon felt. Compared with the VRB battery assembled with unmodified commercial carbon felt, the VRB battery with graphene-modified carbon felt has high power density (Fig. 1), as well as high efficiency, superior rate capability and cycling performance (Fig. 2). . High-performance graphene-modified carbon felt composite electrodes were prepared by uniformly depositing graphene with high specific surface area and high conductivity on the surface of commercial carbon felt by vapor deposition method. The raw materials used in this kind of method are cheap and easy to obtain, the operation is simple and convenient, and suitable for large-scale industrial development, and it is expected to prepare a low-cost and high-performance commercial electrode material for vanadium batteries.

附图说明:Description of drawings:

图1是制得的石墨烯改性碳毡的面积。其中,(a)为20cm×20cm×5.5mm的石墨烯碳毡实物图;(b)为循环伏安曲线,横坐标Voltage代表电压(V),纵坐标Current density代表电流密度(mA/cm2),Pure CF代表原始碳毡,G-CF代表石墨烯碳毡。Figure 1 is the area of the prepared graphene-modified carbon felt. Among them, (a) is the actual graph of the graphene carbon felt of 20cm×20cm×5.5mm; (b) is the cyclic voltammetry curve, the abscissa Voltage represents the voltage (V), and the ordinate Current density represents the current density (mA/cm 2 ) . ), Pure CF stands for pristine carbon felt, and G-CF stands for graphene carbon felt.

图2是采用商业碳毡和石墨烯改性碳毡钒电池效率对比。图中,横坐标Cyclenumber代表循环次数,纵坐标Efficiency代表电池效率(%),EE:Pristine CF代表原始碳毡的能量效率,VE:Pristine CF代表原始碳毡的电压效率,EE:G/CF代表石墨烯碳毡的能量效率,VE:G/CF代表石墨烯碳毡的电压效率。Figure 2 is a comparison of the efficiency of vanadium cells using commercial carbon felt and graphene-modified carbon felt. In the figure, the abscissa Cyclenumber represents the cycle number, the ordinate Efficiency represents the battery efficiency (%), EE:Pristine CF represents the energy efficiency of the original carbon felt, VE:Pristine CF represents the voltage efficiency of the original carbon felt, EE:G/CF represents Energy efficiency of graphene carbon felt, VE:G/CF represents the voltage efficiency of graphene carbon felt.

具体实施方式:Detailed ways:

在具体实施过程中,本发明以商业化碳毡为原料,采用化学气相沉积(CVD)的方法,制备石墨烯改性碳毡电极。该电极材料具有电导率高、比表面积大、钒离子催化性能好、稳定性好、电化学催化活性高等优点。In the specific implementation process, the present invention uses commercial carbon felt as a raw material, and adopts a chemical vapor deposition (CVD) method to prepare a graphene-modified carbon felt electrode. The electrode material has the advantages of high electrical conductivity, large specific surface area, good vanadium ion catalytic performance, good stability, and high electrochemical catalytic activity.

在制备石墨烯改性碳毡电极之前,对碳毡进行如下处理:Before preparing the graphene-modified carbon felt electrode, the carbon felt is treated as follows:

(1)将干燥处理的碳毡浸泡在酸溶液中,常温浸泡一定时间,随后超声震荡一定时间;其中,碳毡干燥处理温度为400~500℃,酸溶液为硫酸、硝酸和盐酸中的一种,酸溶液浓度为1~3mol/L,在酸溶液中浸泡碳毡的时间为12~18h,超声震荡时间为0.5~1.5h;(1) soak the dried carbon felt in an acid solution, soak it at room temperature for a certain period of time, and then ultrasonically vibrate it for a certain period of time; wherein, the carbon felt drying temperature is 400 to 500 ° C, and the acid solution is one of sulfuric acid, nitric acid and hydrochloric acid. The concentration of the acid solution is 1-3 mol/L, the time for soaking the carbon felt in the acid solution is 12-18 hours, and the ultrasonic oscillation time is 0.5-1.5 hours;

(2)将步骤(1)中的碳毡,反复用去离子水清洗,清洗次数为10~15次;(2) the carbon felt in step (1) is repeatedly cleaned with deionized water, and the cleaning times are 10 to 15 times;

(3)将清洗后的碳毡进行干燥处理,碳毡干燥温度为80~120℃。(3) The cleaned carbon felt is subjected to drying treatment, and the drying temperature of the carbon felt is 80-120°C.

下面,结合实施例对本发明做进一步描述。Hereinafter, the present invention will be further described with reference to the embodiments.

实施例1Example 1

本实施例中,石墨烯改性碳毡制备方法,步骤如下:In the present embodiment, the preparation method of graphene modified carbon felt, the steps are as follows:

(1)如图1(a)所示,将20cm×20cm×5.5mm的碳毡放入制备室内底部的石墨匀热样品台上,并将样品对准制备室内顶部的气体出口方向。(1) As shown in Figure 1(a), put a 20cm×20cm×5.5mm carbon felt on the graphite uniform heating sample stage at the bottom of the preparation chamber, and align the sample with the gas outlet direction at the top of the preparation chamber.

(2)开启制备室上的H2阀门,清洗2min,关闭H2阀门;进一步地,重复清洗4次;( 2 ) open the H valve on the preparation chamber, clean for 2min , close the H valve; further, repeat the cleaning 4 times;

(3)开启制备室上的CH4阀门,清洗2min,关闭CH4阀门;进一步地,重复清洗4次;( 3 ) open the CH valve on the preparation chamber, clean for 2min, and close the CH valve; further, repeat the cleaning 4 times;

(4)开启制备室上的高真空阀,手动开启高真空机组,抽真空5min,使制备室内的真空度为2.5×10-2~3×10-3Pa;关闭高真空阀,手动关闭高真空机组;(4) Open the high vacuum valve on the preparation chamber, manually open the high vacuum unit, and evacuate for 5 minutes, so that the vacuum degree in the preparation chamber is 2.5 × 10 -2 ~ 3 × 10 -3 Pa; close the high vacuum valve, and manually close the high vacuum vacuum unit;

(5)开启H2阀门,调整气体流量为150~200sccm,将制备室加热升温至温度为1000±10℃,升温时间为100~120min;( 5 ) open the H valve, adjust the gas flow rate to be 150~200sccm, heat the preparation chamber to a temperature of 1000±10°C, and the heating time is 100~120min;

(6)在1000±10℃保温,时间5min;(6) Keep the temperature at 1000±10℃ for 5min;

(7)在保温时间内,打开CH4阀门,调整气体流量为20~30sccm,维持反应时间为5min,通过化学气相沉积在碳毡上制备石墨烯,以形成石墨烯改性碳毡;( 7 ) in the holding time, open the CH valve, adjust the gas flow to be 20~30sccm, maintain the reaction time to be 5min, prepare graphene by chemical vapor deposition on the carbon felt, to form the graphene modified carbon felt;

(8)关闭CH4阀门,维持H2流量为150~200sccm,随炉冷却;(8) Close the CH 4 valve, maintain the H 2 flow at 150-200sccm, and cool with the furnace;

(9)温度降至室温后,关闭H2阀门,即可获得石墨烯改性碳毡样品。(9) After the temperature drops to room temperature, close the H valve, and the graphene - modified carbon felt sample can be obtained.

本实施例中,石墨烯改性碳毡上的石墨烯负载量为0.3wt%,获得的改性碳毡中石墨烯分布均匀,未出现聚集现象。In this embodiment, the graphene loading on the graphene-modified carbon felt is 0.3 wt %, and the graphene in the obtained modified carbon felt is evenly distributed, and no aggregation phenomenon occurs.

本实施例的相关性能数据如下:The relevant performance data of this embodiment are as follows:

室温下测得碳毡在全钒氧化还原液流电池中的内阻为0.65Ω·cm2,此比例制备的复合电极面电阻小于商业碳毡(0.72Ω·cm2),VRB中的电池效率高于商业碳毡,适应VRB的应用要求,可以促进全钒氧化还原液流电池的工业化发展。但石墨烯的沉积量需要增加,以进一步提高电池性能。The internal resistance of the carbon felt in the all-vanadium redox flow battery was measured at room temperature to be 0.65Ω·cm 2 . The surface resistance of the composite electrode prepared in this ratio was lower than that of the commercial carbon felt (0.72Ω·cm 2 ). The battery efficiency in VRB It is higher than the commercial carbon felt, adapts to the application requirements of VRB, and can promote the industrial development of all-vanadium redox flow batteries. But the deposition amount of graphene needs to be increased to further improve the battery performance.

实施例2Example 2

与实施例1不同之处在于:The difference from Example 1 is that:

1、步骤(7)中,化学气相沉积制备石墨烯改性碳毡时间为10min。1. In step (7), the time for chemical vapor deposition to prepare the graphene-modified carbon felt is 10 min.

2、采用实施例1其余同样步骤制备石墨烯改性碳毡,石墨烯改性碳毡上的石墨烯负载量为0.6wt%。2. The graphene-modified carbon felt was prepared by the other same steps as in Example 1, and the graphene loading on the graphene-modified carbon felt was 0.6 wt%.

由于石墨烯沉积时间增加,在相同条件下,改性电极上石墨烯负载量增加,因此该复合电极电导率提高,高于实施例1。因此,室温下测得改性电极在全钒氧化还原液流电池中的内阻为0.55Ω·cm2,此比例制备的复合电极面电阻低于原碳毡(0.72Ω·cm2),VRB中的电池能量效率高于原碳毡,见图2。如图1(b)所示,与未改性商业化碳毡组装的VRB电池对比,采用石墨烯改性碳毡的VRB电池具有高的功率密度。所以,该复合碳毡能够很好的适应钒电池体系,其低廉的成本,良好的电池性能能够促进钒电池的大规模商业化生产。As the graphene deposition time increases, under the same conditions, the graphene loading on the modified electrode increases, so the electrical conductivity of the composite electrode increases, which is higher than that of Example 1. Therefore, the internal resistance of the modified electrode in the all-vanadium redox flow battery measured at room temperature is 0.55Ω·cm 2 , and the surface resistance of the composite electrode prepared in this ratio is lower than that of the original carbon felt (0.72Ω·cm 2 ), VRB The energy efficiency of the cells in the carbon felt is higher than that of the original carbon felt, see Figure 2. As shown in Figure 1(b), compared with the VRB battery assembled with unmodified commercial carbon felt, the VRB battery with graphene-modified carbon felt has a high power density. Therefore, the composite carbon felt can be well adapted to the vanadium battery system, and its low cost and good battery performance can promote the large-scale commercial production of vanadium batteries.

实施例3Example 3

与实施例1不同之处在于:The difference from Example 1 is that:

1、步骤(7)中,化学气相沉积制备石墨烯改性碳毡时间为15min。1. In step (7), the time for chemical vapor deposition to prepare the graphene-modified carbon felt is 15 min.

2、采用实施例1其余同样步骤制备石墨烯改性碳毡,石墨烯改性碳毡上的石墨烯负载量为0.8wt%。2. The graphene-modified carbon felt was prepared by the other same steps as in Example 1, and the graphene loading on the graphene-modified carbon felt was 0.8 wt%.

由于石墨烯沉积时间增加,在相同条件下,改性电极上石墨烯负载量增加,因此该复合电极电导率提高,高于实施例1和2。但由于石墨烯负载量增加,在碳毡碳纤维表面出现团聚现象,影响该改性碳毡在钒电池中性能。同时,由于沉积时间长,碳毡制备成本提高,不利于钒电池产业化发展。Due to the increase of graphene deposition time, under the same conditions, the graphene loading on the modified electrode increases, so the conductivity of the composite electrode is improved, which is higher than that of Examples 1 and 2. However, due to the increase of graphene loading, agglomeration occurs on the surface of carbon felt carbon fibers, which affects the performance of the modified carbon felt in vanadium batteries. At the same time, due to the long deposition time, the preparation cost of carbon felt increases, which is not conducive to the industrial development of vanadium batteries.

实施例4Example 4

与实施例1不同之处在于:The difference from Example 1 is that:

1、步骤(7)中,化学气相沉积制备石墨烯改性碳毡时间为20min。1. In step (7), the time for chemical vapor deposition to prepare the graphene-modified carbon felt is 20 min.

2、采用实施例1其余同样步骤制备石墨烯改性碳毡,石墨烯改性碳毡上的石墨烯负载量为1wt%。2. The graphene-modified carbon felt was prepared by the other same steps as in Example 1, and the graphene loading on the graphene-modified carbon felt was 1wt%.

由于石墨烯沉积时间进一步增加,在相同条件下,改性电极上石墨烯负载量增加,因此该复合电极电导率提高,高于实施例1,2和3。但由于石墨烯负载量增加,在碳毡碳纤维表面出现团聚现象,影响该改性碳毡在钒电池中性能。同时,由于沉积时间长,碳毡制备成本提高,不利于钒电池产业化发展。Due to the further increase of the graphene deposition time, under the same conditions, the graphene loading on the modified electrode increases, so the electrical conductivity of the composite electrode is improved, which is higher than that of Examples 1, 2 and 3. However, due to the increase of graphene loading, agglomeration occurs on the surface of carbon felt carbon fibers, which affects the performance of the modified carbon felt in vanadium batteries. At the same time, due to the long deposition time, the preparation cost of carbon felt increases, which is not conducive to the industrial development of vanadium batteries.

实施例结果表明,本发明以碳毡为原料,采用实施例2中步骤,通过化学气相沉积方法,制备石墨烯改性碳毡电极材料。本发明制备的石墨烯改性电极具有电导率高、比表面积大、钒离子催化性能好、稳定性好、电化学催化活性高等优点。本发明的制备方法操作简单易行,环境友好,原料成本低廉,易于大规模产业化生产,可广泛地应用于全钒氧化还原液流电池商业化领域。The results of the examples show that the present invention uses carbon felt as a raw material, adopts the steps in Example 2, and prepares a graphene-modified carbon felt electrode material by a chemical vapor deposition method. The graphene modified electrode prepared by the invention has the advantages of high electrical conductivity, large specific surface area, good vanadium ion catalytic performance, good stability, and high electrochemical catalytic activity. The preparation method of the invention is simple and easy to operate, environmentally friendly, low in cost of raw materials, easy for large-scale industrial production, and can be widely used in the commercial field of all-vanadium redox flow batteries.

Claims (8)

1. A preparation method of a macroscopic quantity graphene modified electrode material is characterized by comprising the following steps and process conditions:
(1) soaking the dried carbon felt in an acid solution at normal temperature for a certain time, and then ultrasonically oscillating for a certain time; wherein the carbon felt is soaked in the acid solution for 12-18 hours, and the ultrasonic oscillation time is 0.5-1.5 hours;
(2) reversely washing the carbon felt in the step (1) by using deionized water;
(3) drying the cleaned carbon felt;
(4) placing a 20cm × 20cm × 5.5.5 mm carbon felt on a graphite uniform heating sample table at the bottom in a preparation chamber, and aligning a sample to the direction of a gas outlet at the top in the preparation chamber;
(5) opening H on the preparation chamber2Cleaning the valve for 1-3 min, and closing H2A valve;
(6) opening CH on preparation Chamber4Cleaning a valve for 1-3 min, and closing CH4A valve;
(7) opening a high vacuum valve on the preparation chamber, manually opening a high vacuum unit, vacuumizing for 4-6 min to ensure that the vacuum degree in the preparation chamber is 2.5 × 10-2~3×10-3Pa; closing the high vacuum valve, and manually closing the high vacuum unit;
(8) is openedH2A valve, adjusting the gas flow to be 150-200 sccm, heating the preparation chamber to 1000 +/-10 ℃ for 100-120 min;
(9) preserving the heat at 1000 +/-10 ℃ for 5-20 min;
(10) within the holding time, CH is opened4A valve for adjusting the gas flow to 20-30 sccm and maintaining the reaction time to 5-20 min;
(11) close CH4Valve, maintenance H2Cooling along with the furnace with the flow rate of 150-200 sccm;
(12) after the temperature is reduced to room temperature, H is turned off2And (5) a valve is used for obtaining a graphene modified carbon felt sample.
2. The preparation method of the macroscopic quantity graphene modified electrode material as claimed in claim 1, wherein in the step (1), the drying temperature of the carbon felt is 400-500 ℃.
3. The method for preparing the macroscopic quantity graphene modified electrode material according to claim 1, wherein in the step (1), the acid solution is one of sulfuric acid, nitric acid and hydrochloric acid, and the concentration of the acid solution is 1-3 mol/L.
4. The method for preparing the macroscopic quantity of graphene modified electrode material according to claim 1, wherein in the step (2), the number of times of cleaning is 10-15.
5. The preparation method of the macroscopic quantity graphene modified electrode material as claimed in claim 1, wherein in the step (3), the drying temperature of the carbon felt is 80-120 ℃.
6. The method for preparing the macroscopic quantity of graphene modified electrode material according to claim 1, wherein in the step (5), the number of times of cleaning is 3-5 times.
7. The method for preparing the macroscopic quantity of graphene modified electrode material according to claim 1, wherein in the step (6), the number of times of cleaning is 3-5 times.
8. The preparation method of the macroscopic quantity of graphene modified electrode material as claimed in claim 1, wherein the graphene loading amount in the graphene modified carbon felt is 0.3-1 wt%.
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