WO2019128865A1 - 一种复合多孔碳材料、超级电容器及超级电容器的制备方法 - Google Patents

一种复合多孔碳材料、超级电容器及超级电容器的制备方法 Download PDF

Info

Publication number
WO2019128865A1
WO2019128865A1 PCT/CN2018/122650 CN2018122650W WO2019128865A1 WO 2019128865 A1 WO2019128865 A1 WO 2019128865A1 CN 2018122650 W CN2018122650 W CN 2018122650W WO 2019128865 A1 WO2019128865 A1 WO 2019128865A1
Authority
WO
WIPO (PCT)
Prior art keywords
asphalt
aqueous solution
parts
deuterated
potassium hydroxide
Prior art date
Application number
PCT/CN2018/122650
Other languages
English (en)
French (fr)
Inventor
乔志军
阮殿波
于学文
裘剑佩
傅冠生
Original Assignee
宁波中车新能源科技有限公司
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 宁波中车新能源科技有限公司 filed Critical 宁波中车新能源科技有限公司
Publication of WO2019128865A1 publication Critical patent/WO2019128865A1/zh

Links

Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/22—Electrodes
    • H01G11/30—Electrodes characterised by their material
    • H01G11/32—Carbon-based
    • H01G11/34—Carbon-based characterised by carbonisation or activation of carbon
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/84—Processes for the manufacture of hybrid or EDL capacitors, or components thereof
    • H01G11/86—Processes for the manufacture of hybrid or EDL capacitors, or components thereof specially adapted for electrodes
    • 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
    • Y02E60/13—Energy storage using capacitors

Definitions

  • the present invention belongs to the technical field of supercapacitors, and in particular, to a method for preparing a composite porous carbon material, a supercapacitor, and a supercapacitor.
  • Supercapacitors also known as electric double layer capacitors, electrochemical capacitors, store energy by polarizing the electrolyte.
  • the supercapacitor can be regarded as two non-reactive porous electrode plates suspended in an electrolyte, which is energized on the plate, the positive plate attracts negative ions in the electrolyte, and the negative plate attracts positive ions, actually forming two capacitive stores.
  • the separated positive ions are in the vicinity of the negative electrode plate, and the negative ions are in the vicinity of the positive electrode plate, and the supercapacitor stores energy by forming an electric double layer structure of electrolyte ions on the electrode surface. Since the supercapacitor does not undergo an electrochemical reaction during charging and discharging, the number of cycles is usually more than 1 million cycles.
  • Graphene has a specific surface area of up to 263 ⁇ 111 2 and The conductivity, so it is the ideal electrode material for supercapacitors, but in fact the conjugation effect between graphene sheets makes the specific surface of industrialized graphene powder very low, which causes its application as an active material in supercapacitors. Not good. Some people have used the graphitization of graphene oxide to obtain more than 30001 ⁇ of porous graphene, which exhibits excellent electrochemical behavior. However, the bulk density of porous graphene is less than 0.2 ⁇ The energy density is low. The capacitor thus obtained is also inferior in specific energy.
  • the present invention provides a composite porous carbon material having a high density and a high specific surface, and a high specific volume, high power supercapacitor produced therefrom and a preparation method thereof.
  • a composite porous carbon material composed of the following components and their parts by weight: graphene oxide
  • Graphene oxide is a product of chemical oxidation and stripping of graphite powder, and contains a rich oxygen-containing functional group, which is easy to be modified.
  • the carrier mobility of graphene at room temperature is currently the highest known carrier mobility, and its electron mobility is less affected by temperature changes. At any temperature between 50 and 500, single-layer graphene The electron mobility is around 15000 ⁇ 11 2 / (V -). With this excellent property, graphene is widely used as an indispensable material in the development of battery capacitance.
  • Asphalt is a complex mixture of various hydrocarbons and non-metal derivatives, and has a high carbon content.
  • the sulfonated pitch used in the present invention has high carbon content and high hydrophilicity, so it is easily activated by alkali.
  • a high specific surface area, high density pitch-based porous carbon material is prepared by etching.
  • the potassium hydroxide is mixed with other components in the form of an aqueous solution.
  • Both graphene oxide and deuterated asphalt are more soluble in water, and the invention is more convenient to form a complex by forming an alkali solution for compound reaction.
  • the present invention also provides a method for preparing the above composite porous carbon material, and the preparation method comprises the following steps:
  • potassium hydroxide is firstly formulated into an aqueous solution of potassium hydroxide, and then graphene oxide and deuterated asphalt are simultaneously dissolved in an aqueous solution of potassium hydroxide to obtain a graphite oxide thin/deuterated asphalt.
  • Aqueous solution 20-100 parts of potassium hydroxide, potassium hydroxide is firstly formulated into an aqueous solution of potassium hydroxide, and then graphene oxide and deuterated asphalt are simultaneously dissolved in an aqueous solution of potassium hydroxide to obtain a graphite oxide thin/deuterated asphalt.
  • the present invention also provides a supercapacitor comprising the electrode made of the above composite porous carbon material.
  • the present invention also provides a method for preparing the supercapacitor, the preparation method comprising the following steps: ⁇ 0 2019/128865 ⁇ (:17(: ⁇ 2018/122650
  • Preparation of carbon material Weigh the raw material according to the composition of the composite porous carbon material, firstly mix potassium hydroxide with ultrapure water to form an aqueous potassium hydroxide solution, and then dissolve the graphene oxide and the deuterated asphalt simultaneously with the hydroxide. In the potassium aqueous solution, the graphite oxide thin/deuterated asphalt-: ⁇ 011 aqueous solution is obtained;
  • the mass fraction of the aqueous solution of the ⁇ 011 is: 5-30%, and the mass ratio of the deuterated asphalt to the graphene oxide is 1-8: 1, the mass ratio of potassium hydroxide to total amount of graphene oxide and deuterated asphalt is 2-5:1.
  • Potassium hydroxide is highly alkaline and can be easily etched on deuterated asphalt to form a high specific surface area, high density pitch-based porous carbon material.
  • the temperature in the drying oven is 80-100° 0 and the drying time is 1-511 during carbonization. Keeping the drying temperature at a lower level and increasing the drying time will help to stabilize the structure and properties of the carbon material and lay the foundation for subsequent operations.
  • the inert gas in the tubular furnace is one of nitrogen gas and nitrogen gas during carbonization, and the heating rate is 500-1500° (: 1-511, heat) Water temperature ⁇ 0 2019/128865 ⁇ (:17(: ⁇ 2018/122650 is 60-80° (:. (: It has strong high temperature resistance, but heating in air will cause (:Respond to oxygen to cause material loss)
  • the inert gas can block oxygen and protect the material. Controlling the heating rate can make the carbon material gradually adapt to the ambient temperature change, and avoid the failure of the surface of the carbon material due to large temperature changes.
  • the temperature is raised to 800-1200° (:, and the temperature is maintained at 2-311.
  • the mass ratio of the graphite thin/asphalt-based composite porous material to the conductive carbon black and the binder in the post-treatment is 7-9: 1: 1, wherein the bonding
  • the agent is 8-12% aqueous solution of polytetrafluoroethylene, the amount of ethanol is 0.5-1.5: ⁇ 11, and the stirring time is 5-711.
  • Proper selection of material ratios and full agitation can maximize the properties of the material itself and increase electrode life.
  • the thickness of the carbon film in the post-treatment is 40-120 ⁇ 1111, and the diameter of the circular carbon film is 10-141 ⁇ . Controlling the volume of the carbon film controls the volume of the supercapacitor and is better suited for different environments.
  • the drying treatment in the post-treatment is to place the circular electrode sheet at 100-140° (: drying in a vacuum drying oven to 6-1011. Vacuum drying can be as much as possible The residual moisture on the electrode sheets is removed, and the presence of water is prevented from affecting the performance of the capacitor electrodes.
  • the aqueous solution in the assembly is one of a 13 ⁇ 411, 011, and ⁇ 4 4 aqueous solution having a mass fraction of 20 to 40%. Selecting a common water system solution as an electrolyte can well control the production of finished products and increase the competitiveness of the product market.
  • the present invention has the following advantages:
  • the composite porous carbon material of the present invention has a simple composition and a convenient synthesis method.
  • the sulfonated pitch has high carbon content and high hydrophilicity, and is easily etched by alkali to prepare a pitch-based porous carbon material having a high specific surface area and a high density.
  • the composite porous carbon material of the present invention has a high density and a large specific surface area. ⁇ 0 2019/128865 ⁇ (:17(: ⁇ 2018/122650
  • the supercapacitor of the present invention has a high specific volume and a large power.
  • FIG. 2 is a pore size distribution diagram of a graphite lean/asphalt-based composite porous carbon material of the present invention.
  • FIG. 3 is a graph showing energy density and power density of a supercapacitor of the present invention.
  • the raw materials are weighed according to the composition of the composite porous carbon material and its parts by weight, including 30 parts of graphene oxide, 30 parts of strontized pitch, and 60 parts of potassium hydroxide, wherein potassium hydroxide is prepared into an aqueous solution when used.
  • Preparation of carbon material firstly mixing potassium hydroxide with ultrapure water to form a potassium hydroxide aqueous solution having a mass fraction of 20%, and simultaneously dissolving the deuterated pitch and the graphene oxide in a mass ratio of 1:1 in potassium hydroxide.
  • the graphite oxide thin/deuterated asphalt is obtained -
  • the aqueous solution, wherein the mass ratio of potassium hydroxide to the total amount of graphene oxide and deuterated asphalt is 3:1.
  • Carbonization Oxidizing graphite thin/deuterated asphalt -
  • the aqueous solution is placed in a dry box and the drying temperature is adjusted to 90.
  • Powder then place the powder in a tube furnace, fill with nitrogen, control the heating rate to 5 ° 0 ⁇ 11, at 800 ° (: 211, then naturally cool to room temperature, take 70 ° after removal (:
  • the hot water is cleaned to obtain a graphite thin/asphalt-based composite porous material, that is, a graphite thin/asphalt-based composite porous carbon material.
  • the X 2 adsorption-desorption curve of the obtained graphite thin/asphalt-based composite porous carbon material is as shown in the drawing.
  • FIG. 1 shows that the composite porous carbon material has good N 2 adsorption performance.
  • the pore size distribution of the graphite thin/asphalt-based composite porous carbon material is shown in Fig. 2;
  • the porous carbon material has a high density and a large specific surface area.
  • the carbon film of 0111 is punched into a plurality of circular carbon films with a diameter of 12111111 by a punching machine, and then a circular carbon film is rolled on the foamed nickel by a tableting machine to obtain a circular electrode piece, and finally a circular shape is obtained.
  • the electrode sheets were placed at 120 ° (: 811 in a vacuum oven).
  • FIG. 3 The energy density and power density of the supercapacitor fabricated in this embodiment are shown in FIG. 3. It can be seen from the figure that the supercapacitor has a high specific capacitance and a large power.
  • the cycle life of the supercapacitor is shown in Fig. 4. It can be seen from the figure that the supercapacitor has an extremely high energy density retention after 10,000 cycles, indicating that the supercapacitor has an excellent service life.
  • the raw materials are weighed according to the composition of the composite porous carbon material and its parts by weight, including 30 parts of graphene oxide, 30 parts of strontized pitch, and 60 parts of potassium hydroxide, wherein potassium hydroxide is prepared into an aqueous solution when used.
  • Preparation of carbon material firstly, potassium hydroxide is mixed with ultrapure water to form an aqueous solution of potassium hydroxide having a mass fraction of 8%, and then the deuterated asphalt with a mass ratio of 8:1 and the graphene oxide are simultaneously dissolved in potassium hydroxide. In the aqueous solution, the graphite oxide thin/deuterated asphalt is obtained - The aqueous solution, wherein the mass ratio of potassium hydroxide to the total amount of graphene oxide and deuterated asphalt is 2:1.
  • Carbonization thinning/deuterated asphalt of graphite oxide
  • the aqueous solution is placed in a dry box and the drying temperature is adjusted to 90.
  • Powder the powder is placed in a tube furnace, filled with nitrogen, and the heating rate is controlled.
  • the temperature is maintained at 900 ° (: 411, and then naturally cooled to room temperature, and then taken out and washed with 60 ° (: hot water to obtain a graphite thin/asphalt-based composite porous material, that is, a graphite thin/asphalt-based composite porous carbon material.
  • the graphite lean/asphalt-based composite porous material and the conductive carbon black and the polytetrafluoroethylene have a mass ratio of 8:
  • the raw materials are weighed according to the composition of the composite porous carbon material and its parts by weight, including 30 parts of graphene oxide, 30 parts of strontized pitch, and 60 parts of potassium hydroxide, wherein potassium hydroxide is prepared into an aqueous solution when used.
  • Preparation of carbon material firstly mixing potassium hydroxide with ultrapure water to form a potassium hydroxide aqueous solution having a mass fraction of 30%, and simultaneously dissolving the deuterated pitch and the graphene oxide in a mass ratio of 5:1 in potassium hydroxide.
  • the graphite oxide thin/deuterated asphalt is obtained -
  • Carbonization thinning or deuterated asphalt of graphite oxide
  • the aqueous solution is placed in a dry box and the drying temperature is adjusted to 90.
  • Powder the powder is placed in a tube furnace, filled with nitrogen, and the heating rate is controlled.
  • 80 ° hot water to obtain graphite thin / asphalt-based composite porous material, that is, graphite thin / pitch-based composite porous carbon material.
  • the graphite lean/asphalt-based composite porous material and the conductive carbon black and the polytetrafluoroethylene have a mass ratio of 8:
  • the circular electrode sheets of the same quality and dryness are respectively selected as two electrodes, the polypropylene film is used as a separator, and the NaOH water solution having a mass fraction of 30% is used as an electrolyte, and assembled into a supercapacitor.
  • the raw materials are weighed according to the composition of the composite porous carbon material and its parts by weight, including 30 parts of graphene oxide, 30 parts of strontized pitch, and 60 parts of potassium hydroxide, wherein potassium hydroxide is prepared into an aqueous solution when used.
  • Preparation of carbon material firstly mixing potassium hydroxide with ultrapure water to form a potassium hydroxide aqueous solution having a mass fraction of 5%
  • the deuterated asphalt with the mass ratio of 7:1 and the graphene oxide are simultaneously dissolved in the potassium hydroxide aqueous solution to obtain the graphite oxide thin/deuterated asphalt-
  • Carbonization The graphite oxide thin/deuterated asphalt-011 aqueous solution is placed in a dry box, and the drying temperature is adjusted to 90. Powder, then place the powder in the tube ⁇ 0 2019/128865 ⁇ (:17(: ⁇ 2018/122650 type furnace, filled with nitrogen, controlled heating rate is 6° (:/1 ⁇ 11, at 950° (: under 311, then naturally cooled to At room temperature, after taking out, the graphite thin/asphalt-based composite porous material, that is, the graphite thin/asphalt-based composite porous carbon material, is washed with 65° (: hot water).
  • the graphite thin/asphalt-based composite porous material is mixed with the conductive carbon black and the binder at a mass ratio of 8:1:1, and then 0.5: ⁇ 11 ethanol is added, and the mixture is stirred to form a mixture, and the mixture is rolled.
  • the raw materials are weighed according to the composition of the composite porous carbon material and its parts by weight, including 30 parts of graphene oxide, 30 parts of strontized pitch, and 60 parts of potassium hydroxide, wherein potassium hydroxide is prepared into an aqueous solution when used.
  • Preparation of carbon material firstly mixing potassium hydroxide with ultrapure water to form a potassium hydroxide aqueous solution having a mass fraction of 10%, and simultaneously dissolving the deuterated pitch and the graphene oxide in a mass ratio of 3:1 in potassium hydroxide.
  • the graphite oxide thin/deuterated asphalt is obtained -
  • the aqueous solution, wherein the mass ratio of potassium hydroxide to the total amount of graphene oxide and deuterated asphalt is 3:1.
  • Carbonization The graphite oxide diluted/deuterated asphalt-011 aqueous solution is placed in a dry box, the drying temperature is adjusted to 10 ⁇ ° ⁇ , the drying time is, and the dried graphite oxide/diluted asphalt is obtained after drying. Powder, then place the powder in a tube furnace, fill with nitrogen, control the heating rate to 8 ° 0 ⁇ 11, at 500 ° (: 211, then naturally cool to room temperature, take 75 ° after removal (: The hot water is cleaned by a graphite/asphalt-based composite porous material, that is, a graphite thin/asphalt-based composite porous carbon material.
  • the graphite lean/asphalt-based composite porous material and the conductive carbon black and the polytetrafluoroethylene have a mass ratio of 8:
  • the NaOH aqueous solution with a mass fraction of 30% is an electrolyte and assembled into a supercapacitor.
  • the raw materials are weighed according to the components of the composite porous carbon material and parts by weight thereof, including 30 parts of graphene oxide, 30 parts of strontized pitch, and 60 parts of potassium hydroxide, wherein potassium hydroxide is prepared into an aqueous solution when used.
  • Preparation of carbon material firstly mixing potassium hydroxide with ultrapure water to form a potassium hydroxide aqueous solution having a mass fraction of 25%, and simultaneously dissolving the deuterated pitch and the graphene oxide in a mass ratio of 2:1 in potassium hydroxide.
  • the graphite oxide thin/deuterated asphalt is obtained -
  • the aqueous solution, wherein the mass ratio of potassium hydroxide to the total amount of graphene oxide and deuterated asphalt is 4:1.
  • Carbonization Oxidizing graphite thin/deuterated asphalt -
  • the aqueous solution is placed in a dry box, the drying temperature is adjusted to 10 ⁇ ° ⁇ , the drying time is 511, and the dried graphite oxide/diluted asphalt is obtained after drying.
  • Powder the powder is placed in a tube furnace, filled with nitrogen, and the heating rate is controlled. After heat-insulating at 750 ° (:, then, it is naturally cooled to room temperature, and then taken out and washed with 60 ° (: hot water to obtain a graphite thin/asphalt-based composite porous material, that is, a graphite thin/asphalt-based composite porous carbon material.
  • the graphite lean/asphalt-based composite porous material and the conductive carbon black and the polytetrafluoroethylene have a mass ratio of 8:
  • Example 3 The only difference from Example 3 is that the graphene oxide in the raw material of Comparative Example 1 is changed to graphene.
  • Example 3 The only difference from Example 3 is that the mass ratio of the deuterated pitch to the graphene oxide in the preparation method of Comparative Example 2 is 10:1.
  • Example 3 The only difference from Example 3 is that in the preparation method of Comparative Example 3, the mass fraction of the aqueous solution of 011 was 50%.
  • Example 3 The only difference from Example 3 is that the mass ratio of potassium hydroxide to the total amount of graphene oxide and deuterated bitumen in the preparation method of Comparative Example 4 is 10:1.
  • the energy density in the table is measured at a current density of 0.058, and the energy density retention rate is measured at a current density of 20 8% after 10,000 cycles.

Landscapes

  • Engineering & Computer Science (AREA)
  • Power Engineering (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Electric Double-Layer Capacitors Or The Like (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

一种复合多孔碳材料、超级电容器及超级电容器的制备方法，该复合多孔碳材料由如下成分及其重量份数组成：氧化石墨烯10-50份、璜化沥青10-50份、氢氧化钾20-100份。氧化石墨烯是石墨粉末经化学氧化、剥离后的产物，含有较丰富的含氧官能团，易于改性。而璜化沥青具有高含碳量及高亲水性，因此很容易被碱活化刻蚀而制备成高比表面积、高密度的沥青基多孔碳材料。加工制备方法即对复合物简单干燥、加热后即可形成复合多孔碳材料，且复合多孔碳材料密度高、比表面积大。由此制备的超级电容器比容高、功率大。

Description

\¥0 2019/128865 卩（：17（：\2018/122650
一种复合多孔碳材料、 超级电容器及超级电容器的制备
方法
技术领域
[0001] 本发明属于超级电容器技术领域， 具体涉及一种复合多孔碳材料、 超级电容器 及超级电容器的制备方法。
背景技术
[0002] 超级电容器， 又叫双电层电容器、 电化学电容器， 通过极化电解质来储能。 超 级电容器可以被视为悬浮在电解质中的两个无反应活性的多孔电极板， 在极板 上加电， 正极板吸引电解质中的负离子， 负极板吸引正离子， 实际上形成两个 电容性存储层， 被分离开的正离子在负极板附近， 负离子在正极板附近， 超级 电容器通过在电极表面形成电解液离子的双电层结构来存储能量。 由于超级电 容器在充放电过程中不发生电化学反应， 因此其循环次数通常大于 100万次。
[0003] 石墨烯因具有高达 263〇1112 的比表面积和
Figure imgf000003_0001
的导电率， 所以是超级电容 器的理想电极材料， 然而实际上石墨烯片之间的 共轭效应使其产业化石墨烯 粉体的比表面很低， 造成其作为活性物质在超级电容器上的应用不佳。 有人利 用氧化石墨烯的水溶性， 采用碱化氧化石墨烯的方法得到了超过 30001^ 的多孔 石墨烯， 其表现了出色的电化学行为， 然而由于多孔石墨烯的堆积密度小于 0.2§ 因此其体积能量密度较低。 由此获得的电容器其比能也较为逊色。
[0004] 针对现在制备出来的电容器低比能的缺陷， 公开号 1030436636公开了一种沥青 基多孔碳材料， 由此制成的电容器具有高比能的优点。 然而电容器仅仅拥有高 比能的特点是远远不能满足日益复杂的使用环境的。
发明概述
技术问题
问题的解决方案
技术解决方案 \¥0 2019/128865 卩（：17（：\2018/122650
[0005] 针对上述存在的问题， 本发明提供一种高密度、 高比表面的复合多孔碳材料及 用其制得的高比容、 高功率超级电容器及其制备方法。
[0006] 为了实现上述目的， 本发明采用以下技术方案：
[0007] 一种复合多孔碳材料， 所述碳材料由如下成分及其重量份数组成： 氧化石墨烯
10-50份、 璜化沥青 10-50份、 氢氧化钾 20-100份。
[0008] 氧化石墨烯是石墨粉末经化学氧化、 剥离后的产物， 含有较丰富的含氧官能团 ， 易于改性。 石墨烯在室温下的载流子迁移率是目前已知载流子迁移率最高的 ， 且其电子迁移率受温度变化的影响较小， 50-500 之间的任何温度下， 单层石 墨烯的电子迁移率都在 15000^11 2/ (V -) 左右， 利用这一优良的特性， 在电池电 容的发展生产中， 石墨烯作为一种不可或缺的材料而被广泛采用。 沥青是多种 碳氢化合物及其非金属衍生物组成的复杂混合物， 具有很高的碳含量， 本发明 采用的磺化沥青具有高含碳量及高亲水性， 因此很容易被碱活化刻蚀而制备成 高比表面积、 高密度的沥青基多孔碳材料。
[0009] 作为优选， 在复合多孔碳材料中， 所述氢氧化钾以水溶液的形式与其他成分混 合。 氧化石墨烯与璜化沥青都较易溶于水， 本发明配成碱溶液进行复合反应形 成复合物更加便捷。
[0010] 本发明还提供一种上述复合多孔碳材料的制备方法， 所述的制备方法包括如下 步骤：
[0011] ( 1) 碳材料制备： 称取碳材料的原料： 氧化石墨烯 10-50份、 璜化沥青 10-50份
、 氢氧化钾 20-100份， 先将氢氧化钾配成氢氧化钾水溶液， 再将氧化石墨烯与璜 化沥青同时溶解于氢氧化钾水溶液中， 得氧化石墨稀 /璜化沥青-
Figure imgf000004_0001
水溶液；
[0012] (2) 碳化： 将氧化石墨稀 /
Figure imgf000004_0002
水溶液干燥后得氧化石墨稀 /璜化沥 青-：^011粉体， 再将粉体置于管式炉中， 在惰性气体下升温至 500-1500° (:并保温 ， 然后冷却至室温， 取出后用热水清洗得石墨稀 /沥青基复合多孔材料， 即为本 发明的复合多孔碳材料。
[0013] 本发明还提供一种超级电容器， 所述的超级电容器包括上述复合多孔碳材料制 得的电极。
[0014] 本发明还提供了该超级电容器的制备方法， 所述的制备方法包括如下步骤： \¥0 2019/128865 卩（：17（：\2018/122650
[0015] ( 1) 碳材料制备： 按复合多孔碳材料的成分称取原料， 先将氢氧化钾混合超 纯水形成氢氧化钾水溶液， 再将氧化石墨烯与璜化沥青同时溶解于氢氧化钾水 溶液中， 得氧化石墨稀 /璜化沥青-：^011水溶液；
[0016] (2) 碳化： 将氧化石墨稀 /璜化沥青-
Figure imgf000005_0001
水溶液置于干燥箱中， 干燥后得氧 化石墨稀 /璜化沥青-
Figure imgf000005_0002
粉体， 再将粉体置于管式炉中， 充入惰性气体， 控制升 温速度并保温， 然后自然冷却至室温， 取出后用热水清洗得石墨稀 /沥青基复合 多孔材料， 即复合多孔碳材料；
[0017] (3) 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 粘结剂混合， 再加 入乙醇， 搅拌形成混合料， 将混合料碾压成碳膜， 再冲成多个圆形碳膜， 然后 将圆形碳膜碾压在泡沫镍上制得圆形电极片， 最后将圆形电极片干燥处理；
[0018] (4) 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以聚丙烯膜 为隔膜， 水系溶液为电解液， 装配成超级电容器。
[0019] 传统的电容器用碳材料不仅原料繁多， 而且处理、 合成步骤复杂， 对材料有较 高的要求。 而本发明的原料极为简单， 仅仅是 3种主要原材料和水的组成， 形成 的复合物处理简单， 简单干燥、 加热后即可形成复合多孔碳材料， 不仅节省材 料成本， 也降低了人工成本。 同时， 利用制得的复合多孔碳材料经简单物理加 工后即形成电容器的电极， 超级电容器组装简便， 性能却十分优异， 具有高比 育^ 高功率、 长寿命的优点。
[0020] 作为优选， 在超级电容器的制备方法中， 碳材料制备中所述：^011占：^011水溶 液的质量分数为 5-30%， 所述璜化沥青与氧化石墨烯的质量比为 1-8: 1， 氢氧化钾 与氧化石墨烯和璜化沥青总量的质量比为 2-5: 1。 氢氧化钾的碱性较强， 可以很 容易在璜化沥青上进行活化刻蚀， 形成高比表面积、 高密度的沥青基多孔碳材 料。
[0021] 作为优选， 在超级电容器的制备方法中， 碳化时所述干燥箱内温度为 80-100°0 ， 干燥时间为 1-511。 保持干燥温度在一个较低水平而增加干燥时间， 有利于保护 碳材料的结构与性质稳定， 为后续操作奠定基础。
[0022] 作为优选， 在超级电容器的制备方法中， 碳化时所述管式炉内惰性气体为氮气 、 氮气中的一种， 升温速度为 在 500- 1500° (:下保温 1-511， 热水温度 \¥0 2019/128865 卩（：17（：\2018/122650 为 60-80° (:。 (:本身具有极强的耐高温特性， 但是在空气中加热会促使 (:与氧气反 应造成材料损失， 惰性气体能隔绝氧气， 保护材料。 控制升温速度可以使碳材 料逐渐适应周围温度变化， 避免因较大的温度变化造成碳材料表面产生裂纹而 失效。
[0023] 作为优选， 升温至 800-1200° (:， 并在该温度下保温 2-311。
[0024] 作为优选， 在超级电容器的制备方法中， 后处理中所述石墨稀 /沥青基复合多 孔材料与导电炭黑、 粘结剂的质量比为 7-9: 1: 1， 其中粘结剂为 8- 12%的聚四氟乙 烯水溶液， 乙醇用量为 0.5-1.5：〇11， 搅拌时间为 5-711。 合理选择材料配比并充分搅 拌可以尽可能发挥材料本身的特性， 增加电极使用寿命。
[0025] 作为优选， 在超级电容器的制备方法中， 后处理中所述碳膜厚度为 40- 120^1111， 圆形碳膜的直径为 10-141^。 控制碳膜的体积就能控制超级电容器的体积， 能更 好地适用于不同环境。
[0026] 作为优选， 在超级电容器的制备方法中， 后处理中所述干燥处理为将圆形电极 片置于 100-140° (:真空干燥箱中干燥 6-1011。 真空干燥可以尽可能地除去电极片上 的残留水分， 避免水的存在对电容器电极的性能造成影响。
[0027] 作为优选， 在超级电容器的制备方法中， 组装中所述水系溶液为质量分数为 20 -40%的1¾11、 011、 ^0 4水溶液中的一种。 选择常见的水系溶液作为电解 液， 能很好地控制生产成品， 增加产品市场竞争力。
发明的有益效果
有益效果
[0028] 与现有技术相比， 本发明具有如下优点：
[0029] ( 1) 本发明的复合多孔碳材料组成成分简单， 合成方法便捷。
[0030] (2) 氧化石墨烯含有丰富的含氧官能团， 易于改性。
[0031] (3) 磺化沥青具有高含碳量及高亲水性， 很容易被碱活化刻蚀而制备成高比 表面积、 高密度的沥青基多孔碳材料。
[0032] (4) 本发明复合多孔碳材料及其高功率超级电容器的制备方法过程简单， 实 用性强。
[0033] (5) 本发明的复合多孔碳材料密度高、 比表面积大。 \¥0 2019/128865 卩（：17（：\2018/122650
[0034] (6) 本发明的超级电容器比容高、 功率大。
对附图的简要说明
附图说明
[0035] 图 1为本发明的石墨稀 /沥青基复合多孔碳材料的 X 2吸脱附曲线。
[0036] 图 2为本发明的石墨稀 /沥青基复合多孔碳材料的孔径分布图。
[0037] 图 3为本发明的超级电容器的能量密度与功率密度图。
[0038] 图 4为本发明的超级电容器的循环寿命图。
发明实施例
本发明的实施方式
[0039] 以下是本发明的具体实施例， 对本发明的技术方案作进一步的描述， 但本发明 并不限于这些实施例。
[0040] 实施例 1
[0041] 配料： 按复合多孔碳材料的成分及其重量份数称取原料， 包括氧化石墨烯 30份 、 璜化沥青 30份、 氢氧化钾 60份， 其中氢氧化钾使用时调制成水溶液。
[0042] 碳材料制备： 先将氢氧化钾混合超纯水形成质量分数为 20%的氢氧化钾水溶液 ， 再将质量比为 1: 1的璜化沥青与氧化石墨烯同时溶解于氢氧化钾水溶液中， 得 氧化石墨稀 /璜化沥青-
Figure imgf000007_0001
水溶液， 其中， 氢氧化钾与氧化石墨烯和璜化沥青总 量的质量比为 3: 1。
[0043] 碳化： 将氧化石墨稀 /璜化沥青-
Figure imgf000007_0002
水溶液置于干燥箱中， 调节干燥温度为 90
Figure imgf000007_0003
粉体， 再将粉体置于管 式炉中， 充入氮气， 控制升温速度为 5°0^11， 在 800° (:下保温 211， 然后自然冷却 至室温， 取出后用 70° (:的热水清洗得石墨稀 /沥青基复合多孔材料， 即石墨稀/沥 青基复合多孔碳材料。 制得的石墨稀 /沥青基复合多孔碳材料的 X 2吸脱附曲线如 附图中的图 1所示； 从图中可得该复合多孔碳材料具有较好的 N 2吸附性能。 该石 墨稀 /沥青基复合多孔碳材料的孔径分布图如图 2所示； 从图中可得该复合多孔碳 材料的密度高、 比表面积大。
[0044] 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 聚四氟乙烯按质量比为 8:
1: 1混合， 再加入 0.51111乙醇， 搅拌 611形成混合料， 利用碾压机将混合料碾压成 80 \¥0 2019/128865 卩（：17（：\2018/122650
0111的碳膜， 再用冲片机冲成多个直径为 12111111的圆形碳膜， 然后利用压片机将圆 形碳膜碾压在泡沫镍上制得圆形电极片， 最后将圆形电极片置于 120° (:真空干燥 箱中干燥 811。
[0045] 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以聚丙烯膜为隔膜 ， 质量分数为 30%的：^〇11水系溶液为电解液， 装配成超级电容器。
[0046] 该实施例中制得的超级电容器的能量密度与功率密度如图 3所示， 从图中可见 该超级电容器比容高、 功率大。 该超级电容器的循环寿命如图 4所示， 从图中可 见该超级电容器在循环 10000次后， 能量密度的保持率极高， 说明该超级电容器 具有极好的使用寿命。
[0047] 实施例 2
[0048] 配料： 按复合多孔碳材料的成分及其重量份数称取原料， 包括氧化石墨烯 30份 、 璜化沥青 30份、 氢氧化钾 60份， 其中氢氧化钾使用时调制成水溶液。
[0049] 碳材料制备： 先将氢氧化钾混合超纯水形成质量分数为 8%的氢氧化钾水溶液 ， 再将质量比为 8: 1的璜化沥青与氧化石墨烯同时溶解于氢氧化钾水溶液中， 得 氧化石墨稀 /璜化沥青-
Figure imgf000008_0001
水溶液， 其中， 氢氧化钾与氧化石墨烯和璜化沥青总 量的质量比为 2: 1。
[0050] 碳化： 将氧化石墨稀 /璜化沥青-
Figure imgf000008_0002
水溶液置于干燥箱中， 调节干燥温度为 90
Figure imgf000008_0003
粉体， 再将粉体置于管 式炉中， 充入氮气， 控制升温速度为
Figure imgf000008_0004
在 900° (:下保温 411， 然后自然冷 却至室温， 取出后用 60° (:的热水清洗得石墨稀 /沥青基复合多孔材料， 即石墨稀/ 沥青基复合多孔碳材料。
[0051] 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 聚四氟乙烯按质量比为 8:
1: 1混合， 再加入 0.51111乙醇， 搅拌 611形成混合料， 利用碾压机将混合料碾压成 50 ^111的碳膜， 再用冲片机冲成多个直径为 12111111的圆形碳膜， 然后利用压片机将圆 形碳膜碾压在泡沫镍上制得圆形电极片， 最后将圆形电极片置于 120° (:真空干燥 箱中干燥 811。
[0052] 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以聚丙烯膜为隔膜 ， 质量分数为 30%的 Na 2S0 4水系溶液为电解液， 装配成超级电容器。 \¥0 2019/128865 卩（：17（：\2018/122650
[0053] 实施例 3
[0054] 配料： 按复合多孔碳材料的成分及其重量份数称取原料， 包括氧化石墨烯 30份 、 璜化沥青 30份、 氢氧化钾 60份， 其中氢氧化钾使用时调制成水溶液。
[0055] 碳材料制备： 先将氢氧化钾混合超纯水形成质量分数为 30%的氢氧化钾水溶液 ， 再将质量比为 5: 1的璜化沥青与氧化石墨烯同时溶解于氢氧化钾水溶液中， 得 氧化石墨稀 /璜化沥青-
Figure imgf000009_0001
水溶液， 其中， 氢氧化钾与氧化石墨烯和璜化沥青总 量的质量比为 5: 1。
[0056] 碳化： 将氧化石墨稀 /璜化沥青-
Figure imgf000009_0002
水溶液置于干燥箱中， 调节干燥温度为 90
Figure imgf000009_0003
粉体， 再将粉体置于管 式炉中， 充入氮气， 控制升温速度为
Figure imgf000009_0004
在 750° (:下保温 111， 然后自然冷却 至室温， 取出后用 80° (:的热水清洗得石墨稀 /沥青基复合多孔材料， 即石墨稀/沥 青基复合多孔碳材料。
[0057] 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 聚四氟乙烯按质量比为 8:
1: 1混合， 再加入 0.51111乙醇， 搅拌 611形成混合料， 利用碾压机将混合料碾压成 40 ^111的碳膜， 再用冲片机冲成多个直径为 12111111的圆形碳膜， 然后利用压片机将圆 形碳膜碾压在泡沫镍上制得圆形电极片， 最后将圆形电极片置于 120° (:真空干燥 箱中干燥 811。
[0058] 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以聚丙烯膜为隔膜 ， 质量分数为 30%的NaOH水系溶液为电解液， 装配成超级电容器。
[0059] 实施例 4
[0060] 配料： 按复合多孔碳材料的成分及其重量份数称取原料， 包括氧化石墨烯 30份 、 璜化沥青 30份、 氢氧化钾 60份， 其中氢氧化钾使用时调制成水溶液。
[0061] 碳材料制备： 先将氢氧化钾混合超纯水形成质量分数为 5%的氢氧化钾水溶液
， 再将质量比为 7: 1的璜化沥青与氧化石墨烯同时溶解于氢氧化钾水溶液中， 得 氧化石墨稀 /璜化沥青-
Figure imgf000009_0005
水溶液， 其中， 氢氧化钾与氧化石墨烯和璜化沥青总 量的质量比为 4: 1。
[0062] 碳化： 将氧化石墨稀 /璜化沥青- 011水溶液置于干燥箱中， 调节干燥温度为 90
Figure imgf000009_0006
粉体， 再将粉体置于管 \¥0 2019/128865 卩（：17（：\2018/122650 式炉中， 充入氮气， 控制升温速度为 6°(：/1^11， 在 950° (:下保温 311， 然后自然冷却 至室温， 取出后用 65° (:的热水清洗得石墨稀 /沥青基复合多孔材料， 即石墨稀/沥 青基复合多孔碳材料。
[0063] 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 粘结剂按质量比为 8: 1:1 混合， 再加入 0.5：〇11乙醇， 搅拌形成混合料， 利用碾压机将混合料碾压成 110^1111 的碳膜， 再用冲片机冲成多个直径为 12111111的圆形碳膜， 然后利用压片机将圆形 碳膜碾压在泡沫镍上制得圆形电极片， 最后将圆形电极片置于 120° (:真空干燥箱 中干燥 811。
[0064] 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以聚丙烯膜为隔膜 ， 质量分数为 30%的：^〇11水系溶液为电解液， 装配成超级电容器。
[0065] 实施例 5
[0066] 配料： 按复合多孔碳材料的成分及其重量份数称取原料， 包括氧化石墨烯 30份 、 璜化沥青 30份、 氢氧化钾 60份， 其中氢氧化钾使用时调制成水溶液。
[0067] 碳材料制备： 先将氢氧化钾混合超纯水形成质量分数为 10%的氢氧化钾水溶液 ， 再将质量比为 3: 1的璜化沥青与氧化石墨烯同时溶解于氢氧化钾水溶液中， 得 氧化石墨稀 /璜化沥青-
Figure imgf000010_0001
水溶液， 其中， 氢氧化钾与氧化石墨烯和璜化沥青总 量的质量比为 3: 1。
[0068] 碳化： 将氧化石墨稀 /璜化沥青- 011水溶液置于干燥箱中， 调节干燥温度为 10 〇°〇, 干燥时间为 ， 干燥后得氧化石墨稀 /璜化沥青-
Figure imgf000010_0002
粉体， 再将粉体置于 管式炉中， 充入氮气， 控制升温速度为 8°0^11， 在 500° (:下保温 211， 然后自然冷 却至室温， 取出后用 75° (:的热水清洗得石墨稀 /沥青基复合多孔材料， 即石墨稀/ 沥青基复合多孔碳材料。
[0069] 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 聚四氟乙烯按质量比为 8:
1: 1混合， 再加入 1.51111乙醇， 搅拌 611形成混合料， 利用碾压机将混合料碾压成 50 ^111的碳膜， 再用冲片机冲成多个直径为 10111111的圆形碳膜， 然后利用压片机将圆 形碳膜碾压在泡沫镍上制得圆形电极片， 最后将圆形电极片置于 100° (:真空干燥 箱中干燥 611。
[0070] 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以聚丙烯膜为隔膜 \¥0 2019/128865 卩（：17（：\2018/122650
， 质量分数为 30%的NaOH水系溶液为电解液， 装配成超级电容器。
[0071] 实施例 6
[0072] 配料： 按复合多孔碳材料的成分及其重量份数称取原料， 包括氧化石墨烯 30份 、 璜化沥青 30份、 氢氧化钾 60份， 其中氢氧化钾使用时调制成水溶液。
[0073] 碳材料制备： 先将氢氧化钾混合超纯水形成质量分数为 25%的氢氧化钾水溶液 ， 再将质量比为 2: 1的璜化沥青与氧化石墨烯同时溶解于氢氧化钾水溶液中， 得 氧化石墨稀 /璜化沥青-
Figure imgf000011_0001
水溶液， 其中， 氢氧化钾与氧化石墨烯和璜化沥青总 量的质量比为 4: 1。
[0074] 碳化： 将氧化石墨稀 /璜化沥青-
Figure imgf000011_0002
水溶液置于干燥箱中， 调节干燥温度为 10 〇°〇, 干燥时间为 511， 干燥后得氧化石墨稀 /璜化沥青-
Figure imgf000011_0003
粉体， 再将粉体置于 管式炉中， 充入氮气， 控制升温速度为
Figure imgf000011_0004
在 750° (:下保温 111， 然后自然冷 却至室温， 取出后用 60° (:的热水清洗得石墨稀 /沥青基复合多孔材料， 即石墨稀/ 沥青基复合多孔碳材料。
[0075] 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 聚四氟乙烯按质量比为 8:
1: 1混合， 再加入 11111乙醇， 搅拌 611形成混合料， 利用碾压机将混合料碾压成 9()0 111的碳膜， 再用冲片机冲成多个直径为 1401111的圆形碳膜， 然后利用压片机将圆 形碳膜碾压在泡沫镍上制得圆形电极片， 最后将圆形电极片置于 140° (:真空干燥 箱中干燥 1011。
[0076] 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以聚丙烯膜为隔膜 ， 质量分数为 30%的：^〇11水系溶液为电解液， 装配成超级电容器。
[0077] 对比例 1
[0078] 与实施例 3的区别仅在于， 对比例 1的原料中氧化石墨烯改为石墨烯。
[0079] 对比例 2
[0080] 与实施例 3的区别仅在于， 对比例 2制备方法中璜化沥青与氧化石墨烯的质量比 为 10: 1。
[0081] 对比例 3
[0082] 与实施例 3的区别仅在于， 对比例 3制备方法中：^011水溶液的质量分数为 50%。
[0083] 对比例 4 \¥0 2019/128865 卩（：17（：\2018/122650
[0084] 与实施例 3的区别仅在于， 对比例 4制备方法中氢氧化钾与氧化石墨烯和璜化沥 青总量的质量比为 10: 1。
[0085] 对比例 5
[0086] 与实施例 3的区别仅在于， 对比例 5制备方法中石墨稀 /沥青基复合多孔材料与 导电炭黑、 粘结剂的质量比为 12: 1: 1。
[0087] 对实施例 1-6与对比例 1-5制得的超级电容器进行测试， 测试其比表面积、 能量 密度、 能量密度保持率， 结果如表 1所示：
Figure imgf000012_0001
[0088] 表中的能量密度是在电流密度 0.05八 下测得， 能量密度保持率是在电流密度 20 八 下， 循环 10000次后测得。
[0089] 尽管对本发明已作出了详细的说明并引证了一些具体实施例， 但是对本领域熟 练技术人员来说， 只要不离开本发明的精神和范围可作各种变化或修正是显然 的。

Claims

\¥0 2019/128865 卩（：17（：\2018/122650 权利要求书 [权利要求 1] 一种复合多孔碳材料， 其特征在于， 所述碳材料由如下成分及其重量 份数组成： 氧化石墨烯 10-50份、 璜化沥青 10-50份、 氢氧化钾 20- 100 份。 [权利要求 2] 根据权利要求 1所述的一种复合多孔碳材料， 其特征在于， 所述氢氧 化钾以水溶液的形式与其他成分混合。 [权利要求 3] 一种超级电容器， 其特征在于， 所述的超级电容器包括由权利要求 1 所述的复合多孔碳材料制得的电极。 [权利要求 4] 一种如权利要求 3所述的超级电容器的制备方法， 其特征在于， 所述 方法包括如下步骤：
( 1) 碳材料制备： 称取碳材料的原料： 氧化石墨烯 10-50份、 璜化沥 青 10-50份、 氢氧化钾 20-100份， 先将氢氧化钾配成氢氧化钾水溶液
， 再将氧化石墨烯与璜化沥青同时溶解于氢氧化钾水溶液中， 得氧化 石墨烯 /璜化沥青-：^011水溶液；
(2) 碳化： 将氧化石墨稀 /璜化沥青-
Figure imgf000013_0001
水溶液置于干燥箱中干燥 得氧化石墨稀 /璜化沥青-
Figure imgf000013_0002
粉体， 再将粉体置于管式炉中， 充入惰 性气体， 控制升温速度并保温， 然后自然冷却至室温， 取出后用热水 清洗得石墨稀 /沥青基复合多孔材料， 即复合多孔碳材料；
(3) 后处理： 将石墨稀/沥青基复合多孔材料与导电炭黑、 粘结剂混 合， 再加入乙醇， 搅拌形成混合料， 将混合料碾压成碳膜， 再冲成多 个圆形碳膜， 然后将圆形碳膜碾压在泡沫镍上制得圆形电极片， 最后 将圆形电极片干燥处理；
(4) 组装： 选取质量相同、 干燥的圆形电极片分别为两个电极， 以 聚丙烯膜为隔膜， 水系溶液为电解液， 装配成超级电容器。
[权利要求 5] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 碳材料 制备中所述 011占 011水溶液的质量分数为 5-30% 所述璜化沥青与 氧化石墨烯的质量比为 1-8: 1， 氢氧化钾与氧化石墨烯和璜化沥青总 量的质量比为 2-5: 1。 \¥0 2019/128865 卩（：17（：\2018/122650
[权利要求 6] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 碳化时 所述干燥箱内温度为 80- 100° (:， 干燥时间为 1-511。
[权利要求 7] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 碳化时 所述管式炉内惰性气体为氮气、 氮气中的一种， 升温速度为
Figure imgf000014_0001
111, 在 500- 1500° (:下保温 1-511， 热水温度为 60-80° (:。
[权利要求 8] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 升温至 8
00-1200° (:， 并在该温度下保温 2-311。
[权利要求 9] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 后处理 中所述石墨稀 /沥青基复合多孔材料与导电炭黑、 粘结剂的质量比为 7 -9: 1:1 , 其中粘结剂为 8-12%的聚四氟乙烯水溶液， 乙醇用量为 0.5-1.5
1111， 搅拌时间为 5-711。
[权利要求 10] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 后处理 中所述碳膜厚度为 40-120(X111， 圆形碳膜的直径为 10- 14111111。
[权利要求 11] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 后处理 中所述干燥处理为将圆形电极片置于 100- 140° (:真空干燥箱中干燥 6- 1
011。
[权利要求 12] 根据权利要求 4所述的超级电容器的制备方法， 其特征在于， 组装中 所述水系溶液为质量分数为 20-40%的 011、 011、 230 4水溶液 中的一种。
PCT/CN2018/122650 2017-12-28 2018-12-21 一种复合多孔碳材料、超级电容器及超级电容器的制备方法 WO2019128865A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201711466361.5 2017-12-28
CN201711466361.5A CN108063057A (zh) 2017-12-28 2017-12-28 一种复合多孔碳材料及其高功率超级电容器的制备方法

Publications (1)

Publication Number Publication Date
WO2019128865A1 true WO2019128865A1 (zh) 2019-07-04

Family

ID=62140768

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2018/122650 WO2019128865A1 (zh) 2017-12-28 2018-12-21 一种复合多孔碳材料、超级电容器及超级电容器的制备方法

Country Status (2)

Country Link
CN (1) CN108063057A (zh)
WO (1) WO2019128865A1 (zh)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108063057A (zh) * 2017-12-28 2018-05-22 宁波中车新能源科技有限公司 一种复合多孔碳材料及其高功率超级电容器的制备方法
CN114843111B (zh) * 2022-05-17 2024-01-30 清华大学 一种多级结构碳纳米复合材料及其制备方法与应用

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110183180A1 (en) * 2010-01-25 2011-07-28 Zhenning Yu Flexible asymmetric electrochemical cells using nano graphene platelet as an electrode material
CN103043663A (zh) * 2013-01-08 2013-04-17 天津大学 磺化沥青基活性炭及其制备方法和应用
CN104319116A (zh) * 2014-09-28 2015-01-28 安徽工业大学 一种超级电容器用微孔炭/石墨烯复合电极材料的制备方法
CN106115694A (zh) * 2016-06-20 2016-11-16 山东欧铂新材料有限公司 一种复合型沥青基活性炭的制备方法以及超级电容器
CN108063057A (zh) * 2017-12-28 2018-05-22 宁波中车新能源科技有限公司 一种复合多孔碳材料及其高功率超级电容器的制备方法

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5288592B2 (ja) * 2008-06-03 2013-09-11 俊則 國府 高比表面積活性炭の製造方法

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110183180A1 (en) * 2010-01-25 2011-07-28 Zhenning Yu Flexible asymmetric electrochemical cells using nano graphene platelet as an electrode material
CN103043663A (zh) * 2013-01-08 2013-04-17 天津大学 磺化沥青基活性炭及其制备方法和应用
CN104319116A (zh) * 2014-09-28 2015-01-28 安徽工业大学 一种超级电容器用微孔炭/石墨烯复合电极材料的制备方法
CN106115694A (zh) * 2016-06-20 2016-11-16 山东欧铂新材料有限公司 一种复合型沥青基活性炭的制备方法以及超级电容器
CN108063057A (zh) * 2017-12-28 2018-05-22 宁波中车新能源科技有限公司 一种复合多孔碳材料及其高功率超级电容器的制备方法

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
GUO, YAN ET AL.: "Hierarchical Porous Carbon Derived from Sulfonated Pitch for Electrical Double Layer Capacitors", JOURNAL OF POWER SOURCES, vol. 252, 11 December 2013 (2013-12-11), pages 235 - 243, XP028670514 *
MA, YUAN ET AL.: "Nitrogen-Doped Hierarchical Porous Carbon with High Surface Area Derived from Graphene Oxide/Pitch Oxide Composite for Supercapacitors", JOURNAL OF COLLOID AND INTERFACE SCIENCE, vol. 461, 28 August 2015 (2015-08-28), pages 96 - 103, XP029298583 *

Also Published As

Publication number Publication date
CN108063057A (zh) 2018-05-22

Similar Documents

Publication Publication Date Title
CN107565086B (zh) 一种电池极板制备方法
US11634332B2 (en) Selenium-doped MXene composite nano-material, and preparation method and use thereof
CN108630920A (zh) 一种纳米金属氧化物/MXene异质结构复合材料及其制备方法
CN110330016A (zh) 一种无烟煤基多孔碳石墨微晶和孔隙的一步协同发展方法
CN107244664B (zh) 类石墨烯结构碳电极材料的制备方法及应用
Yan et al. Hierarchically porous carbon derived from wheat straw for high rate lithium ion battery anodes
CN110265711A (zh) 一种固态电解质薄膜及其制备方法和应用
CN109192523B (zh) 一种Ni(OH)2/多层石墨烯复合材料的制备方法
CN104022306B (zh) 一种固体多孔聚合物电解质及其制备方法和应用
CN115020643A (zh) 一种基于生物质的硬碳及其制备方法和在钠离子电池中的应用
CN101162773A (zh) 电池正极片的制作方法及制作的正极片以及锂离子电池
CN104064368A (zh) 用于超级电容电池的Ni/C负极浆料及负极极片制备方法
CN106356556B (zh) 一种使用寿命长的锂离子动力电池及其制备方法
WO2019128865A1 (zh) 一种复合多孔碳材料、超级电容器及超级电容器的制备方法
CN105514425B (zh) 一种高性能室温钠离子电池及其制备方法
Wang et al. High rate lithium slurry flow batteries enabled by an ionic exchange Nafion composite membrane incorporated with LLZTO fillers
CN110033961B (zh) Ni-MOF自支撑复合电极及制作方法
US20220044879A1 (en) Large-Area Continuous Flexible Free-Standing Electrode And Preparation Method And Use Thereof
CN109148841B (zh) 一种锂基蒙脱土@硫复合材料及其制备方法和应用
CN110767465A (zh) 一种基于二维碳化铌纳米复合材料超级电容器的制备方法
CN111430153B (zh) 一种用于全固态超级电容器的碳纳米气凝胶材料及其制备方法与应用
CN111584243B (zh) 一种Mn3O4-碳纳米管-聚苯胺超级电容器材料及其制法
CN108807013B (zh) 多孔花状NiCo2O4/Co3O4/NiO超级电容器电极材料的制备方法
CN114447304B (zh) 一种硬碳复合负极材料及其制备方法和应用
CN110137456A (zh) 一种Ag/SnS2@rGO、制备方法及应用

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18893783

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18893783

Country of ref document: EP

Kind code of ref document: A1