CN105186004B - A kind of used as negative electrode of Li-ion battery copper current collector and its preparation method and application - Google Patents
A kind of used as negative electrode of Li-ion battery copper current collector and its preparation method and application Download PDFInfo
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- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 82
- 239000010949 copper Substances 0.000 title claims abstract description 79
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 70
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 42
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims abstract description 70
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 65
- 229910021389 graphene Inorganic materials 0.000 claims abstract description 44
- 239000002184 metal Substances 0.000 claims abstract description 10
- 229910052751 metal Inorganic materials 0.000 claims abstract description 10
- 239000002082 metal nanoparticle Substances 0.000 claims abstract description 10
- 239000011889 copper foil Substances 0.000 claims abstract description 7
- 238000010791 quenching Methods 0.000 claims abstract description 4
- 230000000171 quenching effect Effects 0.000 claims abstract description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 19
- 238000000034 method Methods 0.000 claims description 11
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 9
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical group CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 claims description 3
- 239000004793 Polystyrene Substances 0.000 claims description 3
- 238000012986 modification Methods 0.000 claims description 3
- 230000004048 modification Effects 0.000 claims description 3
- 235000006408 oxalic acid Nutrition 0.000 claims description 3
- 238000005498 polishing Methods 0.000 claims description 3
- 229920002223 polystyrene Polymers 0.000 claims description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 2
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims description 2
- 229910052737 gold Inorganic materials 0.000 claims description 2
- 238000005554 pickling Methods 0.000 claims description 2
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- 238000001354 calcination Methods 0.000 claims 2
- 239000010931 gold Substances 0.000 claims 2
- 239000008246 gaseous mixture Substances 0.000 claims 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 239000003792 electrolyte Substances 0.000 abstract description 6
- 230000003628 erosive effect Effects 0.000 abstract description 3
- 238000007738 vacuum evaporation Methods 0.000 abstract description 2
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- 239000013543 active substance Substances 0.000 abstract 1
- 238000000137 annealing Methods 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 239000011247 coating layer Substances 0.000 abstract 1
- 239000002105 nanoparticle Substances 0.000 description 18
- 239000011149 active material Substances 0.000 description 14
- 229910045601 alloy Inorganic materials 0.000 description 9
- 239000000956 alloy Substances 0.000 description 9
- 238000001878 scanning electron micrograph Methods 0.000 description 8
- 229910002804 graphite Inorganic materials 0.000 description 7
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- 238000010586 diagram Methods 0.000 description 6
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- 238000009210 therapy by ultrasound Methods 0.000 description 5
- 229910001316 Ag alloy Inorganic materials 0.000 description 4
- 229910001020 Au alloy Inorganic materials 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 3
- 229910052744 lithium Inorganic materials 0.000 description 3
- 239000007773 negative electrode material Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- KUJOABUXCGVGIY-UHFFFAOYSA-N lithium zinc Chemical compound [Li].[Zn] KUJOABUXCGVGIY-UHFFFAOYSA-N 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 210000002268 wool Anatomy 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009831 deintercalation Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- -1 graphene layer-modified Cu foil Chemical class 0.000 description 1
- 238000009396 hybridization Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 125000001624 naphthyl group Chemical group 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 235000021110 pickles Nutrition 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 238000007788 roughening Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/661—Metal or alloys, e.g. alloy coatings
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/665—Composites
- H01M4/667—Composites in the form of layers, e.g. coatings
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- 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
- Y02E60/10—Energy storage using batteries
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- Electrochemistry (AREA)
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- Cell Electrode Carriers And Collectors (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
技术领域technical field
本发明属于锂离子电池技术领域,具体涉及一种锂离子电池负极用铜集流体及其制备方法和应用。The invention belongs to the technical field of lithium ion batteries, and in particular relates to a copper current collector for negative electrodes of lithium ion batteries, a preparation method and application thereof.
背景技术Background technique
锂离子电池被认为是最绿色环保的清洁能源之一,现在已经被广泛的应用在便携式电子产品上,同时被认为是很有应用前景的混合电动车和纯电动车的动力源。锂离子电池主要由活性物质、电池壳、集流体、隔膜、电解液等部件组成。其中,集流体是锂离子电池的重要组成部分之一,表面承载着活性物并与电解液接触,同时将正负极活性物质产生的电子通过它汇集到外电路形成电流。Lithium-ion batteries are considered to be one of the most green and clean energy sources, and are now widely used in portable electronic products, and are considered to be a promising power source for hybrid electric vehicles and pure electric vehicles. Lithium-ion batteries are mainly composed of active materials, battery cases, current collectors, diaphragms, electrolytes and other components. Among them, the current collector is one of the important components of the lithium-ion battery. The surface carries the active material and is in contact with the electrolyte. At the same time, the electrons generated by the positive and negative active materials are collected to the external circuit through it to form a current.
铜具有足够的机械强度,良好的导电性,不易与锂发生合金化等优点,常用于锂离子电池负极的集流体。现在商业化的锂离子电池负极Cu集流体主要采用电解Cu箔,分为双面光、双面毛、单面毛、双面粗化及高延伸率等几种类型。但是,Cu集流体表面容易生成氧化膜,氧化膜属于半导体,会影响集流体的导电性;Cu集流体在电池充放电过程中容易与电解液的溶剂和杂质发生反应溶解,使Cu不稳定,同时,Cu表面的氧化物容易和锂离子发生脱嵌反应,产生的体积膨胀收缩,使Cu表面的活性物质涂层脱落;另外,以硅为代表的高容量负极材料在充放电循环中体积发生巨大变化,造成电极材料与Cu集流体的分离。Copper has sufficient mechanical strength, good electrical conductivity, and is not easy to alloy with lithium, etc., and is often used as a current collector for the negative electrode of lithium-ion batteries. The current commercial Li-ion battery anode Cu current collector mainly uses electrolytic Cu foil, which is divided into several types such as double-sided light, double-sided wool, single-sided wool, double-sided roughening, and high elongation. However, an oxide film is easily formed on the surface of the Cu current collector, and the oxide film is a semiconductor, which will affect the conductivity of the current collector; the Cu current collector is easy to react and dissolve with the solvent and impurities of the electrolyte during the charging and discharging process of the battery, making Cu unstable. At the same time, oxides on the surface of Cu are prone to deintercalation reactions with lithium ions, resulting in volume expansion and contraction, which makes the active material coating on the surface of Cu fall off; Great changes, resulting in the separation of electrode materials and Cu current collectors.
发明内容Contents of the invention
为克服上述缺陷,本发明的目的之一在于提供一种锂离子电池负极用铜集流体,具有良好的导电性,能够缓解电解液的侵蚀,与活性物质涂层结合力强。In order to overcome the above-mentioned defects, one of the objects of the present invention is to provide a copper current collector for the negative electrode of lithium-ion batteries, which has good electrical conductivity, can alleviate the erosion of the electrolyte, and has a strong binding force with the active material coating.
本发明的第二个目的还在于提供一种锂离子电池负极用铜集流体的制备方法。The second object of the present invention is also to provide a method for preparing a copper current collector for negative electrodes of lithium ion batteries.
本发明的第三个目的还在于提供一种铜集流体在锂离子电池中的应用。The third object of the present invention is also to provide an application of a copper current collector in a lithium-ion battery.
为实现上述目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种锂离子电池负极用铜集流体,在铜集流体表面依次修饰石墨烯层和金属纳米颗粒层。A copper current collector for negative electrodes of lithium-ion batteries, in which a graphene layer and a metal nanoparticle layer are sequentially modified on the surface of the copper current collector.
根据上述的锂离子电池负极用铜集流体,所述金属为Cu、Au、Ag中的一种或者几种的合金。According to the above-mentioned copper current collector for negative electrodes of lithium-ion batteries, the metal is one or an alloy of Cu, Au, and Ag.
根据上述的锂离子电池负极用铜集流体,所述石墨烯层厚度为0.5~2 nm。According to the above-mentioned copper current collector for negative electrodes of lithium ion batteries, the thickness of the graphene layer is 0.5-2 nm.
根据上述的锂离子电池负极用铜集流体,所述金属纳米颗粒的平均粒径为10~100 nm。According to the above-mentioned copper current collector for negative electrodes of lithium-ion batteries, the average particle diameter of the metal nanoparticles is 10-100 nm.
一种上述的锂离子电池负极用铜集流体的制备方法,包括如下步骤:A kind of preparation method of above-mentioned lithium ion battery negative electrode copper current collector, comprises the steps:
(1)抛光或者酸洗Cu箔,40~60 ℃真空干燥30~60 min,得到干燥Cu箔;(1) Polish or pickle the Cu foil, and vacuum dry it at 40-60 °C for 30-60 min to obtain a dried Cu foil;
(2)将步骤(1)干燥Cu箔,置于CVD管式炉中,还原气氛下,950~1060 ℃煅烧20~70 min;(2) Put the dried Cu foil in step (1) into a CVD tube furnace and calcinate it at 950-1060 °C for 20-70 min under a reducing atmosphere;
(3)将步骤(2)煅烧后的Cu箔放入无氧反应器中,加热到950~1060 ℃,向反应器中充入碳源,恒温5~60 min,在还原性气氛下冷却到室温,得到石墨层烯修饰的Cu箔,石墨烯层厚度为0.5~2 nm;(3) Put the Cu foil calcined in step (2) into an oxygen-free reactor, heat it to 950-1060 °C, fill the reactor with carbon source, keep the temperature constant for 5-60 min, and cool it down to At room temperature, a graphene-modified Cu foil is obtained, and the thickness of the graphene layer is 0.5-2 nm;
(4)在石墨烯层表面真空蒸镀金属膜,厚度为4~20 nm;(4) Vacuum-evaporate a metal film on the surface of the graphene layer with a thickness of 4-20 nm;
(5)在还原气氛下,250~350 ℃淬火处理步骤(4)金属膜20~50 min,使石墨烯层表面形成金属纳米颗粒层,得到产品铜集流体。(5) Under reducing atmosphere, 250-350 ℃ quenching treatment step (4) metal film for 20-50 min, so that a metal nanoparticle layer is formed on the surface of the graphene layer, and the product copper current collector is obtained.
根据上述的锂离子电池负极用铜集流体的制备方法,步骤(1)所述的酸洗方法为:酸溶液超声处理5~15 min,所述酸溶液为醋酸或者草酸溶液,浓度为0.5~2 mol·L-1。According to the above-mentioned preparation method of copper current collector for negative electrode of lithium ion battery, the pickling method described in step (1) is: ultrasonic treatment of acid solution for 5-15 minutes, the acid solution is acetic acid or oxalic acid solution, the concentration is 0.5- 2 mol·L -1 .
根据上述的锂离子电池负极用铜集流体的制备方法,步骤(2)或者步骤(5)中所述的还原气氛为H2或者Ar和H2的混合气,步骤(3)所述的还原性气氛为H2。According to the above method for preparing a copper current collector for negative electrodes of lithium-ion batteries, the reducing atmosphere described in step (2) or step (5) is H2 or a mixed gas of Ar and H2 , and the reducing atmosphere described in step (3) The neutral atmosphere is H 2 .
根据上述的锂离子电池负极用铜集流体的制备方法,步骤(3)中所述的碳源为气体碳源、液体碳源或者固体碳源。According to the above method for preparing a copper current collector for negative electrodes of lithium-ion batteries, the carbon source described in step (3) is a gaseous carbon source, a liquid carbon source or a solid carbon source.
根据上述的锂离子电池负极用铜集流体的制备方法,所述的气体碳源为甲烷、乙炔或者乙烯。According to the above method for preparing a copper current collector for negative electrodes of lithium ion batteries, the gaseous carbon source is methane, acetylene or ethylene.
根据上述的锂离子电池负极用铜集流体的制备方法,所述的液体碳源为乙醇或者苯。According to the above method for preparing a copper current collector for negative electrodes of lithium ion batteries, the liquid carbon source is ethanol or benzene.
根据上述的锂离子电池负极用铜集流体的制备方法,所述的固体碳源为萘或者聚苯乙烯。According to the above method for preparing a copper current collector for negative electrodes of lithium ion batteries, the solid carbon source is naphthalene or polystyrene.
一种上述制备的铜集流体在锂离子电池中的应用。An application of the copper current collector prepared above in a lithium ion battery.
本发明的积极有益效果:Positive beneficial effect of the present invention:
1. 本发明以化学气相沉积法(CVD法)在Cu衬底上生长具有高导电性的石墨烯层,然后在石墨烯层上蒸镀导电性良好的金属膜,淬火处理之后金属膜由于表面张力的存在破裂收缩,形成金属纳米颗粒层,石墨烯和导电性好的金属纳米颗粒以及Cu衬底可以形成良好的导电网络。1. The present invention grows a graphene layer with high conductivity on a Cu substrate by chemical vapor deposition (CVD method), and then vapor-deposits a metal film with good conductivity on the graphene layer. After quenching, the metal film is due to the surface The presence of tension ruptures and shrinks to form a layer of metal nanoparticles. Graphene, metal nanoparticles with good conductivity and Cu substrate can form a good conductive network.
采用CVD法生长的石墨烯层可以很好的覆盖满Cu衬底的表面,这样可以缓解电解液对Cu集流体的侵蚀,而且石墨烯是一种碳原子按照sp2杂化排布,并相互连接成蜂窝状的网络结构,它具有高透过率、高导电性、高机械强度和大比表面积等优异性能,可以提高Cu集流体的导电性能;金属纳米颗粒可以增加Cu集流体的比表面积和粗糙程度,这样可以增强活性物质和集流体的接触面积和粘合力,进而可以提高锂离子电池的可逆比容量和循环性能。The graphene layer grown by CVD can well cover the surface of the Cu substrate, which can alleviate the erosion of the electrolyte on the Cu current collector, and graphene is a kind of carbon atoms arranged according to sp 2 hybridization, and mutually Connected into a honeycomb network structure, it has excellent properties such as high transmittance, high conductivity, high mechanical strength and large specific surface area, which can improve the conductivity of Cu current collectors; metal nanoparticles can increase the specific surface area of Cu current collectors And the degree of roughness, which can enhance the contact area and adhesion between the active material and the current collector, thereby improving the reversible specific capacity and cycle performance of the lithium-ion battery.
2. 石墨烯在生长过程中通入还原性气体,使Cu衬底的表面氧化物被还原为Cu单质,进而降低Cu衬底的电阻,将这种结构的Cu箔作为锂离子电池负极用集流体可以降低活性物和集流体界面的电荷转移阻抗,从而有利于锂离子电池电化学性能的发挥。2. During the growth process of graphene, a reducing gas is introduced to reduce the surface oxide of the Cu substrate to Cu simple substance, thereby reducing the resistance of the Cu substrate. The Cu foil with this structure is used as a collector for the negative electrode of the lithium-ion battery. The fluid can reduce the charge transfer resistance at the interface between the active material and the current collector, which is beneficial to the electrochemical performance of the lithium-ion battery.
3. 本发明锂离子电池负极用铜集流体制备方法简单,显著提高了锂离子电池的电化学性能,可广泛应用于锂离子电池。3. The preparation method of the copper current collector for the negative electrode of the lithium ion battery is simple, significantly improves the electrochemical performance of the lithium ion battery, and can be widely used in lithium ion batteries.
附图说明Description of drawings
图1为本发明锂离子电池负极用铜集流体的结构示意图;Fig. 1 is the structural representation of copper current collector for negative electrode of lithium ion battery of the present invention;
图2为实施例1锂离子电池在2 A·g-1电流下的首次充放电曲线图;Fig. 2 is the first charge and discharge curve diagram of embodiment 1 lithium-ion battery under 2 A · g -1 electric current;
图3为实施例1锂离子电池在2 A·g-1电流下的循环性能图;Fig. 3 is the cycle performance figure of embodiment 1 lithium-ion battery under 2 A · g -1 electric current;
图4为实施例1锂离子电池在4 A·g-1和6 A·g-1电流下的循环性能图;Fig. 4 is the cycle performance diagram of the lithium-ion battery of Example 1 at 4 A g -1 and 6 A g -1 current;
图5为实施例1锂离子电池负极极片的截面SEM图;Fig. 5 is the cross-sectional SEM figure of embodiment 1 lithium-ion battery negative pole sheet;
图6为对照锂离子电池负极极片的截面SEM图;Fig. 6 is the cross-sectional SEM figure of contrast lithium-ion battery negative pole piece;
图7为实施例2铜集流体的SEM图;Fig. 7 is the SEM figure of embodiment 2 copper current collector;
图8为实施例2铜集流体在超声处理15 min后的SEM图;Fig. 8 is the SEM image of the copper current collector of Example 2 after ultrasonic treatment for 15 min;
图9为实施例2锂离子电池在1 C电流下循环200次后负极极片的截面SEM图;Fig. 9 is the cross-sectional SEM diagram of the negative pole piece after the lithium-ion battery of embodiment 2 cycles 200 times under 1 C electric current;
图10为对照锂离子电池在1 C电流下循环200次后负极极片的截面SEM图;Figure 10 is a cross-sectional SEM image of the negative electrode sheet of the control lithium-ion battery after 200 cycles at a current of 1 C;
图11为实施例3制备的锂离子电池在0.5 A·g-1电流下的循环性能图。Figure 11 is a graph of the cycle performance of the lithium-ion battery prepared in Example 3 at a current of 0.5 A g -1 .
具体实施方式detailed description
下面结合一些具体实施方式,对本发明进一步说明。The present invention will be further described below in conjunction with some specific embodiments.
实施例1Example 1
参见图1~6,一种锂离子电池负极用铜集流体,在铜箔表面依次修饰石墨烯层和Au纳米颗粒层,石墨烯层厚度为1 nm,Au纳米颗粒的平均粒径为27 nm。Referring to Figures 1 to 6, a copper current collector for the negative electrode of a lithium-ion battery is sequentially decorated with a graphene layer and an Au nanoparticle layer on the surface of the copper foil. The thickness of the graphene layer is 1 nm, and the average particle size of the Au nanoparticles is 27 nm. .
上述的锂离子电池负极用铜集流体的制备方法,包括如下步骤:The preparation method of the above-mentioned copper current collector for negative electrode of lithium ion battery comprises the following steps:
(1)采用1 mol·L-1的醋酸溶液超声处理铜箔10 min,接着用水和乙醇淋洗,真空50 ℃干燥30 min,得到干燥的Cu箔;(1) The copper foil was ultrasonically treated with 1 mol L -1 acetic acid solution for 10 min, then rinsed with water and ethanol, and dried in vacuum at 50 °C for 30 min to obtain a dried Cu foil;
(2)将步骤(1)干燥的Cu箔置于CVD管式炉中在H2气流下于1045 ℃煅烧60 min,H2流量为10 sccm;(2) The Cu foil dried in step (1) was placed in a CVD tube furnace and calcined at 1045 °C for 60 min under H2 flow, and the H2 flow rate was 10 sccm;
(3)采用CH4为碳源,在1045 ℃通入CH4和H2,CH4流量为1 sccm,H2 (3) Using CH 4 as carbon source, feed CH 4 and H 2 at 1045 ℃, CH 4 flow rate is 1 sccm, H 2
流量为2 sccm,恒温15 min,在H2气氛下冷却到室温,H2流量为10 sccm,得到石墨烯层修饰的Cu箔,石墨烯层厚度为1 nm;The flow rate is 2 sccm, the temperature is kept for 15 min, cooled to room temperature under H2 atmosphere, and the H2 flow rate is 10 sccm to obtain a graphene layer-modified Cu foil with a graphene layer thickness of 1 nm;
(4)在石墨烯层表面真空蒸镀Au膜,Au膜厚度为8 nm;(4) Vacuum-deposit Au film on the surface of the graphene layer, and the thickness of the Au film is 8 nm;
(5)Au膜在H2和Ar气体保护下300 ℃淬火处理30 min,使石墨烯层表面形成Au纳米颗粒层,H2流量为600 sccm,Ar流量600 sccm,得到产品Cu集流体。(5) The Au film was quenched at 300 ℃ for 30 min under the protection of H 2 and Ar gas to form an Au nanoparticle layer on the surface of the graphene layer. The H 2 flow rate was 600 sccm and the Ar flow rate was 600 sccm to obtain the product Cu current collector.
采用扣式半电池检测本发明Cu集流体对电池性能的影响,锂离子电池采用实施例1制备的Cu箔为集流体,钛酸锂锌(Li2ZnTi3O8,LZTO)为活性物质,锂离子电池标注为Cu-G-Au-LZTO。A button half-cell was used to detect the influence of the Cu current collector of the present invention on battery performance. The Cu foil prepared in Example 1 was used as the current collector for the lithium-ion battery, and lithium zinc titanate (Li 2 ZnTi 3 O 8 , LZTO) was used as the active material. Li-ion batteries are marked as Cu-G-Au-LZTO.
作为对照锂离子电池以未用石墨烯和Au纳米颗粒修饰的Cu箔为集流体,钛酸锂锌(Li2ZnTi3O8,LZTO)为活性物质,锂离子电池标注为Cu-LZTO。As a control lithium-ion battery, Cu foil not modified with graphene and Au nanoparticles was used as the current collector, lithium zinc titanate (Li 2 ZnTi 3 O 8 , LZTO) was used as the active material, and the lithium-ion battery was marked as Cu-LZTO.
图2是本实施例锂离子电池在2 A·g-1电流下的首次充放电曲线图,Cu-LZTO和Cu-G-Au-LZTO锂离子电池的放电比容量分别为212.2和242.1 mAh·g-1,可见本发明用石墨烯和Au纳米颗粒共同修饰的Cu集流体显著提高了电池的放电比容量。Figure 2 is the first charge-discharge curve of the lithium-ion battery of this embodiment at a current of 2 A g -1 , and the discharge specific capacities of Cu-LZTO and Cu-G-Au-LZTO lithium-ion batteries are 212.2 and 242.1 mAh· g -1 , it can be seen that the Cu current collector co-modified with graphene and Au nanoparticles in the present invention significantly improves the discharge specific capacity of the battery.
图3是本实施例锂离子电池在2 A·g-1电流下的循环性能图,Cu-LZTO和Cu-G-Au-LZTO锂离子电池在第二次的放电比容量分别为160.0和219.4 mAh·g-1,循环200次后的比容量分别为136.1和204.9 mAh·g-1,相对于第二次的容量保持率分别为85.1%和93.4%,本发明用石墨烯和Au纳米颗粒共同修饰的Cu集流体显著提高了电池的循环性能。Figure 3 is the cycle performance diagram of the lithium-ion battery of this embodiment at a current of 2 A g -1 , and the specific capacities of the Cu-LZTO and Cu-G-Au-LZTO lithium-ion batteries in the second discharge are 160.0 and 219.4 respectively mAh·g -1 , the specific capacity after 200 cycles is 136.1 and 204.9 mAh·g -1 respectively, and the capacity retention rate relative to the second time is 85.1% and 93.4%, respectively. The present invention uses graphene and Au nanoparticles The co-modified Cu current collector significantly improves the cycle performance of the battery.
图4是本实施例锂离子电池在4 A·g-1和6 A·g-1电流下的循环性能图,循环100次后电池的放电比容量分别为172.2和130.0 mAh·g-1,本发明锂离子电池表现出良好的大电流充放电性能。Figure 4 is the cycle performance diagram of the lithium-ion battery of this example under the current of 4 A g -1 and 6 A g -1 . After 100 cycles, the discharge specific capacity of the battery is 172.2 and 130.0 mAh g -1 respectively, The lithium ion battery of the invention exhibits good high-current charging and discharging performance.
图5为以本实施例制备的Cu-G-Au-LZTO锂离子电池负极极片的截面SEM图,从图中可以看出活性物质涂层跟集流体之间的空隙很小,说明两者之间具有良好的粘合力;图6为对照Cu-LZTO锂离子电池负极极片的截面SEM图,从图中可以看出活性物物质涂层跟集流体间的空隙较大,说明两者间的粘附力差。Figure 5 is a cross-sectional SEM image of the Cu-G-Au-LZTO lithium-ion battery negative pole piece prepared in this example. It can be seen from the figure that the gap between the active material coating and the current collector is very small, indicating that both There is good adhesion between them; Figure 6 is a cross-sectional SEM image of the negative pole piece of the Cu-LZTO lithium-ion battery. It can be seen from the figure that the gap between the active material coating and the current collector is relatively large, indicating that both The adhesion between them is poor.
实施例2Example 2
参见图1,图7~10,一种锂离子电池负极用铜集流体,在铜箔表面依次修饰石墨烯层和合金纳米颗粒层,石墨烯层厚度为1 nm,所述的合金为Au和Ag合金,两者质量比为1:1,合金纳米颗粒平均粒径为50 nm。Referring to Fig. 1, Figs. 7-10, a copper current collector for negative electrodes of lithium-ion batteries, a graphene layer and an alloy nanoparticle layer are sequentially modified on the surface of copper foil, the thickness of the graphene layer is 1 nm, and the alloy is Au and Ag alloy, the mass ratio of the two is 1:1, and the average particle size of alloy nanoparticles is 50 nm.
上述的锂离子电池负极用铜集流体的制备方法,包括如下步骤:The preparation method of the above-mentioned copper current collector for negative electrode of lithium ion battery comprises the following steps:
(1)采用1 mol·L-1的草酸溶液超声处理Cu箔15 min,接着用水和乙醇淋洗,真空60 ℃干燥40 min,得到干燥的Cu箔;(1) Ultrasonic treatment of Cu foil with 1 mol L -1 oxalic acid solution for 15 min, followed by rinsing with water and ethanol, and vacuum drying at 60 °C for 40 min to obtain dried Cu foil;
(2)将干燥的Cu箔置于CVD管式炉中在H2气流下于1050 ℃煅烧20 min,H2流量为10sccm;(2) The dried Cu foil was calcined in a CVD tube furnace at 1050 °C for 20 min under H2 flow, and the H2 flow rate was 10 sccm;
(3)采用CH4为碳源,在1060 ℃通入CH4和H2,CH4流量为1 sccm,H2流量为2 sccm,恒温10 min,在H2保护下降到室温,H2流量为10 sccm,得到石墨烯层修饰的Cu箔,石墨烯层厚度为1 nm;(3) Using CH 4 as the carbon source, feed CH 4 and H 2 at 1060 °C, the flow rate of CH 4 is 1 sccm, the flow rate of H 2 is 2 sccm, keep the temperature for 10 min, and drop to room temperature under the protection of H 2 , the flow rate of H 2 Be 10 sccm, obtain the Cu foil of graphene layer modification, the thickness of graphene layer is 1 nm;
(4)在石墨烯层表面真空蒸镀Au和Ag合金膜,合金膜厚度为12 nm;(4) Vacuum evaporation of Au and Ag alloy film on the surface of the graphene layer, the thickness of the alloy film is 12 nm;
(5)Au和Ag合金膜在H2气体保护下250 ℃淬火处理合金膜50 min,使石墨烯层表面形成合金纳米颗粒层,H2流量为700 sccm,得到产品Cu集流体。(5) The Au and Ag alloy film was quenched at 250 ℃ for 50 min under the protection of H 2 gas to form an alloy nanoparticle layer on the surface of the graphene layer. The H 2 flow rate was 700 sccm to obtain the product Cu current collector.
采用扣式半电池检测Cu集流体对电池性能的影响,锂离子电池以实施例2制备的Cu箔为集流体,钛酸锂(Li4Ti5O12,LTO)为活性物质,锂离子电池标注为Cu-G-Au/Ag-LTO。The influence of Cu current collector on battery performance was detected by button half-cell. Lithium-ion battery uses Cu foil prepared in Example 2 as current collector, lithium titanate (Li 4 Ti 5 O 12 , LTO) as active material, lithium-ion battery Labeled as Cu-G-Au/Ag-LTO.
作为对照锂离子电池以未用石墨烯和Au/Ag合金纳米颗粒修饰的Cu箔为集流体,钛酸锂(Li4Ti5O12,LTO)为活性物质,锂离子电池标注为Cu-LTO。As a control lithium-ion battery, Cu foil not modified with graphene and Au/Ag alloy nanoparticles is used as the current collector, lithium titanate (Li 4 Ti 5 O 12 , LTO) is used as the active material, and the lithium-ion battery is marked as Cu-LTO .
图7是本实施例制备的Cu集流体的SEM图,图8是本实施例制备的Cu集流体在超声处理15 min后的SEM图,从图7和图8中可以看出超声处理后石墨烯和合金纳米颗粒没有脱落,说明采用本发明制备的石墨烯和合金纳米颗粒修饰层和Cu具有良好的结合力。Figure 7 is the SEM image of the Cu current collector prepared in this example, and Figure 8 is the SEM image of the Cu current collector prepared in this example after ultrasonic treatment for 15 min. It can be seen from Figures 7 and 8 that the graphite after ultrasonic treatment Graphene and alloy nanoparticles did not fall off, indicating that the modified layer of graphene and alloy nanoparticles prepared by the present invention has good binding force with Cu.
图9是本实施例Cu-G-Au/Ag-LTO锂离子电池在1 C电流下循环200次后负极极片的截面SEM图,图10是对照Cu-LTO锂离子电池在1 C电流下循环200次后负极极片的截面SEM图,对照Cu-LTO锂离子电池循环后负极活性物质涂层跟集流体分离现象严重,本发明Cu-G-Au/Ag-LTO锂离子电池负极活性物质涂层跟集流体间具有良好的粘合力,循环100次后两者没有明显的分离现象。Figure 9 is a cross-sectional SEM image of the negative electrode sheet of the Cu-G-Au/Ag-LTO lithium-ion battery of this example after 200 cycles at 1 C current, and Figure 10 is a contrast Cu-LTO lithium-ion battery at 1 C current After 200 cycles, the SEM image of the cross-section of the negative electrode sheet, compared with the Cu-LTO lithium ion battery, the negative electrode active material coating is seriously separated from the current collector, and the negative electrode active material of the Cu-G-Au/Ag-LTO lithium ion battery of the present invention There is good adhesion between the coating and the current collector, and there is no obvious separation between the two after 100 cycles.
实施例3Example 3
参见图1和11,一种锂离子电池负极用铜集流体,在铜箔表面依次修饰石墨烯层和Ag纳米颗粒层,石墨烯层厚度为2 nm,Ag纳米颗粒的平均粒径为22 nm。Referring to Figures 1 and 11, a copper current collector for the negative electrode of a lithium-ion battery, the graphene layer and the Ag nanoparticle layer are sequentially modified on the surface of the copper foil, the thickness of the graphene layer is 2 nm, and the average particle size of the Ag nanoparticles is 22 nm .
上述的锂离子电池负极用铜集流体的制备方法,包括如下步骤:The preparation method of the above-mentioned copper current collector for negative electrode of lithium ion battery comprises the following steps:
(1)采用机械抛光机抛光,真空40 ℃干燥30 min,得到干燥的Cu箔;(1) Polishing with a mechanical polishing machine and drying in vacuum at 40 °C for 30 min to obtain a dried Cu foil;
(2)将干燥的Cu箔置于CVD管式炉中在Ar和H2气流下于1060℃煅烧70 min,Ar流量为200 sccm,H2流量为20 sccm;(2) The dried Cu foil was calcined in a CVD tube furnace at 1060 °C for 70 min under the flow of Ar and H2 , the flow rate of Ar was 200 sccm, and the flow rate of H2 was 20 sccm;
(3)采用聚苯乙烯为碳源,在950 ℃通入H2,H2流量为2 sccm,恒温30 min,在H2保护下降到室温,H2流量为15 sccm,得到石墨烯层修饰的Cu箔,石墨烯层厚度为2 nm;(3) Using polystyrene as the carbon source, H 2 was introduced at 950 ℃, the flow rate of H 2 was 2 sccm, and the temperature was kept constant for 30 minutes, and then it was lowered to room temperature under the protection of H 2 , and the flow rate of H 2 was 15 sccm to obtain graphene layer modification Cu foil with a graphene layer thickness of 2 nm;
(4)在石墨烯层表面真空蒸镀Ag膜,Ag膜厚度为4 nm;(4) Vacuum-deposit Ag film on the surface of the graphene layer with a thickness of 4 nm;
(5)Ag金属膜在H2和Ar气体保护下350 ℃淬火处理20 min,使石墨烯层表面形成Ag纳米颗粒层,H2流量为500 sccm,Ar流量为500 sccm,得到产品Cu集流体。(5) The Ag metal film was quenched at 350 ℃ for 20 min under the protection of H 2 and Ar gas to form an Ag nanoparticle layer on the surface of the graphene layer. The H 2 flow rate was 500 sccm, and the Ar flow rate was 500 sccm to obtain the product Cu current collector .
采用扣式半电池检测Cu集流体对电池性能的影响,锂离子电池以实施例3制备的Cu箔为集流体,石墨为活性物质,锂离子电池标注为Cu-G-Ag-graphite。A button half-cell was used to detect the influence of Cu current collector on the performance of the battery. The Cu foil prepared in Example 3 was used as the current collector for the lithium-ion battery, graphite was used as the active material, and the lithium-ion battery was marked as Cu-G-Ag-graphite.
作为对照锂离子电池以未用石墨烯和Ag纳米颗粒修饰的Cu为集流体,石墨为活性物质,锂离子电池标注为Cu-graphite。As a control lithium-ion battery, Cu not modified with graphene and Ag nanoparticles was used as the current collector, graphite was used as the active material, and the lithium-ion battery was marked as Cu-graphite.
采用四探针测试仪测试空白Cu和本实施例制备的修饰的Cu的电阻分别为50和27mΩ,可见本发明采用石墨烯和Ag纳米颗粒修饰Cu箔显著提高了Cu集流体的导电性。Using a four-probe tester to test the resistance of the blank Cu and the modified Cu prepared in this example were 50 and 27 mΩ, respectively. It can be seen that the present invention uses graphene and Ag nanoparticles to modify the Cu foil to significantly improve the conductivity of the Cu current collector.
图11是本实施例Cu-G-Ag-graphite锂离子电池在0.5 A·g-1电流下的循环性能图,在整个循环过程中Cu-G-Ag-graphite锂离子电池具有较大的比容量,可以看出石墨烯和Ag纳米颗粒共同修饰的Cu集流体可以显著提高电池的可逆比容量。Figure 11 is the cycle performance diagram of the Cu-G-Ag-graphite lithium-ion battery in this embodiment at a current of 0.5 A g -1 , and the Cu-G-Ag-graphite lithium-ion battery has a larger specificity in the whole cycle. It can be seen that the Cu current collector co-modified by graphene and Ag nanoparticles can significantly improve the reversible specific capacity of the battery.
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