CN114420940A - Current collector for lithium ion secondary battery and preparation method and system thereof - Google Patents
Current collector for lithium ion secondary battery and preparation method and system thereof Download PDFInfo
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- 238000002360 preparation method Methods 0.000 title claims abstract description 41
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title abstract description 29
- 229910001416 lithium ion Inorganic materials 0.000 title abstract description 29
- 239000000835 fiber Substances 0.000 claims abstract description 76
- 238000003763 carbonization Methods 0.000 claims abstract description 28
- 229920005594 polymer fiber Polymers 0.000 claims abstract description 20
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 14
- 230000003647 oxidation Effects 0.000 claims abstract description 13
- 229920000642 polymer Polymers 0.000 claims abstract description 10
- 238000012545 processing Methods 0.000 claims abstract description 8
- 238000001523 electrospinning Methods 0.000 claims abstract description 4
- 239000004743 Polypropylene Substances 0.000 claims description 30
- -1 polypropylene Polymers 0.000 claims description 30
- 229920001155 polypropylene Polymers 0.000 claims description 30
- 238000009941 weaving Methods 0.000 claims description 21
- 238000009987 spinning Methods 0.000 claims description 14
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 4
- 229910052744 lithium Inorganic materials 0.000 claims description 4
- 229920002125 Sokalan® Polymers 0.000 claims description 2
- 239000007772 electrode material Substances 0.000 claims description 2
- 239000000155 melt Substances 0.000 claims description 2
- 239000004584 polyacrylic acid Substances 0.000 claims description 2
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 2
- 238000001179 sorption measurement Methods 0.000 description 26
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 23
- 229910052782 aluminium Inorganic materials 0.000 description 23
- 239000011888 foil Substances 0.000 description 23
- 238000004804 winding Methods 0.000 description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 13
- 229910052799 carbon Inorganic materials 0.000 description 12
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 description 12
- 239000011248 coating agent Substances 0.000 description 11
- 238000000576 coating method Methods 0.000 description 11
- 238000001816 cooling Methods 0.000 description 10
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- 229920002981 polyvinylidene fluoride Polymers 0.000 description 6
- 239000007774 positive electrode material Substances 0.000 description 6
- 239000011149 active material Substances 0.000 description 4
- 239000006258 conductive agent Substances 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
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- 238000012986 modification Methods 0.000 description 3
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- 239000006229 carbon black Substances 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 238000003486 chemical etching Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000003851 corona treatment Methods 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
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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
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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
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- 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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Abstract
本发明涉及电池集流体领域,具体涉及一种锂离子二次电池用的集流体及其制备方法与系统。该制备方法具体包括:将聚合物熔体经静电纺丝后得到聚合物纤维,而后将所述聚合物纤维制成纤维聚集体;之后将所述纤维聚集体依次进行预氧化和碳化,以得到所述集流体;其中,在所述静电纺丝中,温度为180‑230℃,速度为10~30m/min;所述聚合物纤维的直径为0.2~0.4μm。本发明还提供了一种锂离子二次电池用的集流体的加工系统。本发明制备的集流体与极片粘结力较强,极片阻抗较低;采用本发明的集流体所制备的锂离子二次电池,电池内阻较低,能够提高锂离子二次电池充放电性能及倍率性能。
The invention relates to the field of battery current collectors, in particular to a current collector for lithium ion secondary batteries and a preparation method and system thereof. The preparation method specifically includes: electrospinning a polymer melt to obtain polymer fibers, and then preparing the polymer fibers into fiber aggregates; then performing pre-oxidation and carbonization on the fiber aggregates in sequence to obtain The current collector; wherein, in the electrospinning, the temperature is 180-230° C., the speed is 10-30 m/min; the diameter of the polymer fiber is 0.2-0.4 μm. The present invention also provides a processing system for a current collector for a lithium ion secondary battery. The current collector prepared by the present invention has strong bonding force with the pole piece, and the electrode resistance is low; the lithium ion secondary battery prepared by using the current collector of the present invention has low internal resistance of the battery, and can improve the charging performance of the lithium ion secondary battery. Discharge performance and rate performance.
Description
技术领域technical field
本发明涉及电池集流体领域,具体涉及一种锂离子二次电池用的集流体及其制备方法与系统。The invention relates to the field of battery current collectors, in particular to a current collector for lithium ion secondary batteries and a preparation method and system thereof.
背景技术Background technique
铝箔是锂离子二次电池的正极集流体,但存在如下问题:铝箔与正极活性物质界面存在接触阻抗,导致充放电过程中,极化过大,发热较重;铝箔与活性物质及导电剂粘结力薄弱,随着充放电的进行,活性物质体积不断碰撞与收缩,活性物质与铝箔剥离,加速容量和寿命的衰减;而且,电解液与铝箔发生反应,也加速了电池寿命的衰减。Aluminum foil is the positive current collector of lithium ion secondary battery, but there are the following problems: the interface between aluminum foil and positive electrode active material has contact resistance, which leads to excessive polarization and heavy heating during charging and discharging; aluminum foil sticks to active material and conductive agent. The bonding force is weak. With the progress of charging and discharging, the volume of the active material continues to collide and shrink, and the active material is peeled off from the aluminum foil, which accelerates the decay of capacity and life; moreover, the reaction between the electrolyte and the aluminum foil also accelerates the decay of battery life.
为解决上述问题,近年来对铝箔进行了大量改性研究,比如化学刻蚀、电晕处理、表面涂碳等,其中表面涂碳的铝箔(简称涂碳铝箔)得到了广泛应用,原因是降低了正极集流体与活性物质的接触阻抗,减轻了极化,在一定程度上提升了电池的充放电性能及倍率性能。In order to solve the above problems, a lot of modification research on aluminum foil has been carried out in recent years, such as chemical etching, corona treatment, surface carbon coating, etc. Among them, carbon-coated aluminum foil (referred to as carbon-coated aluminum foil) has been widely used. The contact resistance between the positive electrode current collector and the active material is reduced, the polarization is reduced, and the charge-discharge performance and rate performance of the battery are improved to a certain extent.
在涂碳铝箔中,常用的导电碳材料主要有炭黑、碳纳米管等,这些导电碳材料在水中的分散性较差,因此制备涂碳铝箔过程中,涂覆时很难使涂层均匀、细腻地涂覆在铝箔上,降低了涂层和铝箔的结合强度以及集流体的稳定性,采用此类涂碳铝箔制成的锂离子二次电池循环过程中极易出现循环跳水现象。In carbon-coated aluminum foil, the commonly used conductive carbon materials mainly include carbon black, carbon nanotubes, etc. These conductive carbon materials have poor dispersibility in water, so in the process of preparing carbon-coated aluminum foil, it is difficult to make the coating uniform during coating. , Delicately coated on the aluminum foil, reducing the bonding strength of the coating and the aluminum foil and the stability of the current collector, the lithium-ion secondary battery made of this type of carbon-coated aluminum foil is prone to cycle diving during the cycle.
发明内容SUMMARY OF THE INVENTION
本发明的第一目的是提供一种集流体的制备方法,具体包括:The first object of the present invention is to provide a method for preparing a current collector, which specifically includes:
将聚合物熔体经静电纺丝后得到聚合物纤维,而后将所述聚合物纤维制成纤维聚集体;之后将所述纤维聚集体依次进行预氧化和碳化,以得到所述集流体;The polymer melt is electrospun to obtain polymer fibers, and then the polymer fibers are made into fiber aggregates; then the fiber aggregates are sequentially pre-oxidized and carbonized to obtain the current collector;
其中,在所述静电纺丝中,温度为180-230℃,速度为10~30m/min;所述聚合物纤维的直径为0.2~0.4μm。Wherein, in the electrospinning, the temperature is 180-230° C., the speed is 10-30 m/min; the diameter of the polymer fiber is 0.2-0.4 μm.
通过上述方法制备的集流体与极片粘结力较强,极片阻抗较低;采用上述集流体所制备的锂离子二次电池,电池内阻较低,能够提高锂离子二次电池充放电性能及倍率性能。The current collector prepared by the above method has strong adhesion to the pole piece, and the resistance of the pole piece is low; the lithium ion secondary battery prepared by using the above current collector has a low internal resistance of the battery, which can improve the charging and discharging of the lithium ion secondary battery. performance and rate capability.
作为本发明的一种优选实施方案,所述聚合物熔体为聚丙烯、聚丙烯酸、聚丙烯腈中任意一种或几种的熔体。As a preferred embodiment of the present invention, the polymer melt is any one or more melts of polypropylene, polyacrylic acid, and polyacrylonitrile.
作为本发明的一种优选实施方案,所述纤维聚集体的孔隙率为40~85%。As a preferred embodiment of the present invention, the porosity of the fiber aggregate is 40-85%.
本发明发现,在上述孔隙率下,正极活性物质可进入集流体孔隙内,充分与集流体接触,提高了正极活性物质和集流体的粘结强度,降低了正极活性物质与集流体的接触电阻。It is found in the present invention that under the above porosity, the positive electrode active material can enter the pores of the current collector and fully contact the current collector, thereby improving the bonding strength between the positive electrode active material and the current collector, and reducing the contact resistance between the positive electrode active material and the current collector. .
作为本发明的一种优选实施方案,所述纤维聚集体的制备具体包括:As a preferred embodiment of the present invention, the preparation of the fiber aggregates specifically includes:
在-0.1~-0.01MPa的压力和20~50kV电压下,对所述聚合物纤维进行收集,以得到所述纤维聚集体。The polymer fibers are collected under a pressure of -0.1 to -0.01 MPa and a voltage of 20 to 50 kV to obtain the fiber aggregate.
通过上述条件下进行收集,能够控制上述纤维聚集体的孔隙率为40~85%,有利于集流体性能的最大化发挥。By collecting under the above conditions, the porosity of the fiber aggregate can be controlled to 40-85%, which is beneficial to maximize the performance of the current collector.
作为优选,可选择在静电吸附元件中进行上述收集;在静电吸附元件中,静电摆丝电压为20~50kV,吸附风压力为-0.1~-0.01MPa。Preferably, the collection can be carried out in an electrostatic adsorption element; in the electrostatic adsorption element, the electrostatic pendulum voltage is 20-50 kV, and the adsorption wind pressure is -0.1--0.01 MPa.
作为本发明的一种优选实施方案,所述预氧化的温度为200~400℃;所述碳化的温度为1500~1800℃。As a preferred embodiment of the present invention, the temperature of the pre-oxidation is 200-400°C; the temperature of the carbonization is 1500-1800°C.
通过在上述预氧化温度和碳化温度下,能够控制所得集流体的孔隙率为30~70%,能够进一步提高正极活性物质和集流体的粘结强度,进一步降低正极活性物质与集流体的接触电阻,从而提升所制备电池的性能。At the above pre-oxidation temperature and carbonization temperature, the porosity of the obtained current collector can be controlled to 30-70%, the bonding strength between the positive electrode active material and the current collector can be further improved, and the contact resistance between the positive electrode active material and the current collector can be further reduced , thereby improving the performance of the prepared battery.
本发明的第二目的是提供一种由上述制备方法制得的集流体。The second object of the present invention is to provide a current collector prepared by the above preparation method.
使用本发明的集流体,在电极中不加入导电剂,所制备的电池内阻与使用涂碳铝箔制备的电池内阻相当,从而降低物料成本。By using the current collector of the present invention, no conductive agent is added to the electrodes, and the internal resistance of the prepared battery is comparable to that of the battery prepared by using carbon-coated aluminum foil, thereby reducing the material cost.
作为优选,所述集流体的孔隙率为30~70%,和/或厚度为10~20μm。Preferably, the porosity of the current collector is 30-70%, and/or the thickness is 10-20 μm.
本发明的第三目的是提供一种电极,所述电极由本发明所制备的集流体和电极活性材料制成。The third object of the present invention is to provide an electrode made of the current collector and electrode active material prepared by the present invention.
本发明的第四目的是提供一种锂电池,其电极包括上述制备方法所制得的集流体。The fourth object of the present invention is to provide a lithium battery, the electrode of which includes the current collector prepared by the above preparation method.
采用本发明的集流体所制备的锂电池,电池内阻较低,能够提高锂电池的充放电性能及倍率性能。The lithium battery prepared by using the current collector of the present invention has lower internal resistance of the battery, and can improve the charge-discharge performance and rate performance of the lithium battery.
本发明的第五目的是提供了一种实现上述集流体制备方法的加工系统,包括依次顺序连接的纤维编织装置、预氧化装置和碳化装置;The fifth object of the present invention is to provide a processing system for realizing the above-mentioned current collector preparation method, comprising a fiber weaving device, a preoxidation device and a carbonization device connected in sequence;
其中,所述纤维编织装置包括纺丝单元和纤维聚集体制备单元;Wherein, the fiber weaving device includes a spinning unit and a fiber aggregate preparation unit;
所述纺丝单元用于对聚合物熔体进行纺丝,以得到聚合物纤维;The spinning unit is used for spinning the polymer melt to obtain polymer fibers;
所述纤维聚集体制备单元用于将所述聚合物纤维制成纤维聚集体。The fiber aggregate preparation unit is used to make the polymer fibers into a fiber aggregate.
所述纺丝单元的出口与所述纤维聚集体制备单元的入口相连接;The outlet of the spinning unit is connected to the inlet of the fiber aggregate preparation unit;
所述纤维聚集体制备单元的出口与所述预氧化装置的入口相连接。The outlet of the fiber aggregate preparation unit is connected to the inlet of the preoxidation device.
通过本发明的加工系统,能够连续完整地实现上述集流体的加工制备,便于在产业中推广应用。通过纤维编织装置先制得适宜孔隙率的聚合物纤维聚集体,而后进一步通过预氧化装置和碳化装置,获得各方面性能更优的集流体。The processing system of the present invention can continuously and completely realize the processing and preparation of the current collector, which is convenient for popularization and application in the industry. Polymer fiber aggregates with suitable porosity are first prepared by a fiber weaving device, and then a current collector with better performance in all aspects is obtained through a pre-oxidation device and a carbonization device.
作为优选,所述纤维聚集体制备单元含有静电吸附元件,所述静电吸附元件用于将所述聚合物纤维通过静电作用和吸附作用制成纤维聚集体。Preferably, the fiber aggregate preparation unit contains an electrostatic adsorption element, and the electrostatic adsorption element is used to make the polymer fiber into a fiber aggregate by electrostatic action and adsorption action.
作为优选,所述纤维编织装置还包括熔融单元,所述熔融单元用于将聚合物制成聚合物熔体;Preferably, the fiber weaving device further comprises a melting unit, the melting unit is used to make the polymer into a polymer melt;
所述熔融单元的出口与纺丝单元的入口相连接。The outlet of the melting unit is connected to the inlet of the spinning unit.
在具体实施方案中,可以采用熔融纺丝机实现所述熔融单元和所述纺丝单元的功能。In particular embodiments, a melt spinning machine may be employed to perform the functions of the melting unit and the spinning unit.
作为优选,上述加工系统还包括冷却装置和收卷轴装置;在所述碳化装置的出口,依次连接设置所述冷却装置和收卷轴装置。Preferably, the above-mentioned processing system further includes a cooling device and a winding shaft device; at the outlet of the carbonization device, the cooling device and the winding shaft device are connected and arranged in sequence.
本发明的有益效果在于:本发明制备的集流体与极片粘结力较强,极片阻抗较低;采用本发明的集流体所制备的锂离子二次电池,电池内阻较低,能够提高锂离子二次电池充放电性能及倍率性能。此外,使用本发明的集流体,在电极中不加入导电剂,所制备的电池内阻与使用涂碳铝箔制备的电池内阻相当,从而降低物料成本。The beneficial effects of the present invention are as follows: the current collector prepared by the present invention has strong adhesion force with the pole piece, and the resistance of the pole piece is low; the lithium ion secondary battery prepared by using the current collector of the present invention has low internal resistance of the battery, and can Improve the charge-discharge performance and rate performance of lithium-ion secondary batteries. In addition, by using the current collector of the present invention, no conductive agent is added to the electrode, and the internal resistance of the prepared battery is comparable to that of the battery prepared by using carbon-coated aluminum foil, thereby reducing the material cost.
附图说明Description of drawings
图1为实施例5加工系统的连接关系示意图。FIG. 1 is a schematic diagram of the connection relationship of the processing system of Example 5. FIG.
图1中:1、纤维编织装置;2、预氧化装置;3、碳化装置;4、冷却装置;5、收卷轴装置;11、熔融纺丝单元;12、纤维聚集体制备单元;121、静电吸附元件。In Fig. 1: 1. Fiber weaving device; 2. Pre-oxidation device; 3. Carbonization device; 4. Cooling device; adsorption element.
具体实施方式Detailed ways
以下实施例用于说明本发明,但不用来限制本发明的范围。The following examples are intended to illustrate the present invention, but not to limit the scope of the present invention.
实施例中未注明具体技术或条件者,均为常规方法或者按照本领域的文献所描述的技术或条件进行,或者按照产品说明书进行。所用试剂和仪器等未注明生产厂商者,均为可通过正规渠道商购买得到的常规产品。If no specific technique or condition is indicated in the examples, it is performed by conventional method or according to the technique or condition described in the literature in this field, or according to the product specification. The reagents and instruments used without the manufacturer's indication are all conventional products that can be purchased through formal channels.
实施例1Example 1
本实施例提供了一种集流体,其制备方法具体步骤如下:The present embodiment provides a current collector, and the specific steps of its preparation method are as follows:
(1)将聚丙烯在纤维编织装置中熔融纺丝后得到聚丙烯纤维;其中,在纤维编织装置中,设置熔融纺丝单元的温度为210℃,设置纺丝速度为15米/分钟,控制聚丙烯纤维的直径在0.2-0.4μm;(1) Polypropylene fibers are obtained after the polypropylene is melt-spun in the fiber weaving device; wherein, in the fiber weaving device, the temperature of the melt spinning unit is set to 210° C., the spinning speed is set to 15 m/min, and the control The diameter of polypropylene fibers is 0.2-0.4 μm;
将聚丙烯纤维经过静电吸附单元的静电作用、吸附作用及自身温度作用后,形成孔隙率为82.3%,厚度为22μm的聚丙烯纤维聚集体;其中,在静电吸附单元中,控制静电摆丝电压为45kV,吸附风大小为-0.02MPa;After the polypropylene fibers are subjected to the electrostatic effect, adsorption effect and self-temperature effect of the electrostatic adsorption unit, a polypropylene fiber aggregate with a porosity of 82.3% and a thickness of 22 μm is formed; wherein, in the electrostatic adsorption unit, the electrostatic wobble voltage is controlled. It is 45kV, and the adsorption wind size is -0.02MPa;
(2)将聚丙烯纤维聚集体从纤维编织装置中传送至预氧化装置中处理;其中,处理温度为350℃,处理时间为3min;(2) transferring the polypropylene fiber aggregates from the fiber weaving device to the pre-oxidizing device for treatment; wherein, the treatment temperature is 350° C., and the treatment time is 3 minutes;
(3)聚丙烯纤维聚集体经预氧化后,传送至碳化装置进行碳化处理;其中,碳化温度为1600℃,处理时间为8min,碳化后,即形成集流体,形成的集流体孔隙率为65.4%,厚度为17.2μm;(3) After pre-oxidation, the polypropylene fiber aggregates are sent to the carbonization device for carbonization treatment; wherein, the carbonization temperature is 1600 ° C, the treatment time is 8 minutes, after carbonization, a current collector is formed, and the formed current collector has a porosity of 65.4 %, the thickness is 17.2μm;
(4)将步骤(3)中制得的集流体传送至冷却装置降温至室温,再经过收卷轴装置收集成卷。(4) The current collector prepared in step (3) is sent to a cooling device to cool down to room temperature, and then collected into a roll through a winding shaft device.
进一步,本实施例还提供了含有上述集流体的锂离子二次电池,具体制备过程如下:将磷酸铁锂正极浆料涂覆在上述集流体上,95℃下烘干、辊压、分切、卷绕后得到容量为4Ah的26650圆柱锂离子二次电池。其中,正极极片的配比为:以质量分数计,磷酸铁锂94%,Super P 3%,PVDF 3%,压实密度为2.45g/cm3。Further, this embodiment also provides a lithium ion secondary battery containing the above current collector, and the specific preparation process is as follows: coating the lithium iron phosphate positive electrode slurry on the above current collector, drying at 95 ° C, rolling, slitting , After winding, a 26650 cylindrical lithium-ion secondary battery with a capacity of 4Ah was obtained. Among them, the ratio of the positive electrode pieces is as follows: in terms of mass fraction, lithium iron phosphate is 94%, Super P is 3%, PVDF is 3%, and the compaction density is 2.45g/cm 3 .
实施例2Example 2
本实施例提供了一种集流体,其制备方法具体步骤如下:The present embodiment provides a current collector, and the specific steps of its preparation method are as follows:
(1)将聚丙烯在纤维编织装置中熔融纺丝后得到聚丙烯纤维;其中,在纤维编织装置中,设置熔融纺丝单元的温度为220℃,设置纺丝速度为10米/分钟,控制聚丙烯纤维的直径在0.2-0.4μm;(1) Polypropylene fibers are obtained after the polypropylene is melt-spun in the fiber weaving device; wherein, in the fiber weaving device, the temperature of the melt spinning unit is set to 220° C., the spinning speed is set to 10 m/min, and the control The diameter of polypropylene fibers is 0.2-0.4 μm;
将聚丙烯纤维经过静电吸附单元的静电作用、吸附作用及自身温度作用后,形成孔隙率为65.8%,厚度为15μm的聚丙烯纤维聚集体;其中,在静电吸附单元中,控制静电摆丝电压为45kV,吸附风大小为-0.06MPa;After the polypropylene fiber is subjected to the electrostatic action, adsorption action and its own temperature action of the electrostatic adsorption unit, a polypropylene fiber aggregate with a porosity of 65.8% and a thickness of 15 μm is formed; in which, in the electrostatic adsorption unit, the electrostatic pendulum voltage is controlled. It is 45kV, and the adsorption wind size is -0.06MPa;
(2)将聚丙烯纤维聚集体从纤维编织装置中传送至预氧化装置中处理;其中,处理温度为350℃,处理时间为5min;(2) Transfer the polypropylene fiber aggregates from the fiber weaving device to the pre-oxidation device for treatment; wherein, the treatment temperature is 350° C., and the treatment time is 5 minutes;
(3)聚丙烯纤维聚集体经预氧化后,传送至碳化装置进行碳化处理;其中,碳化温度为1600℃,处理时间为8min,碳化后,即形成集流体,形成的集流体孔隙率为46.1%,厚度为10.6μm;(3) After pre-oxidation, the polypropylene fiber aggregates are sent to the carbonization device for carbonization treatment; wherein the carbonization temperature is 1600 ° C, and the treatment time is 8 minutes. After carbonization, a current collector is formed, and the porosity of the formed current collector is 46.1 %, the thickness is 10.6μm;
(4)将步骤(3)中制得的集流体传送至冷却装置降温至室温,再经过收卷轴装置收集成卷。(4) The current collector prepared in step (3) is sent to a cooling device to cool down to room temperature, and then collected into a roll through a winding shaft device.
进一步,本实施例还提供了含有上述集流体的锂离子二次电池,具体制备过程如下:将磷酸铁锂正极浆料涂覆在上述集流体上,95℃下烘干、辊压、分切、卷绕后得到容量为4Ah的26650圆柱锂离子二次电池。其中,正极极片的配比为:以质量分数计,磷酸铁锂94%,Super P 3%,PVDF 3%,压实密度为2.45g/cm3。Further, this embodiment also provides a lithium ion secondary battery containing the above current collector, and the specific preparation process is as follows: coating the lithium iron phosphate positive electrode slurry on the above current collector, drying at 95 ° C, rolling, slitting , After winding, a 26650 cylindrical lithium-ion secondary battery with a capacity of 4Ah was obtained. Among them, the ratio of the positive electrode pieces is as follows: in terms of mass fraction, lithium iron phosphate is 94%, Super P is 3%, PVDF is 3%, and the compaction density is 2.45g/cm 3 .
实施例3Example 3
本实施例提供了一种集流体,其制备方法具体步骤如下:The present embodiment provides a current collector, and the specific steps of its preparation method are as follows:
(1)将聚丙烯在纤维编织装置中熔融纺丝后得到聚丙烯纤维;其中,在纤维编织装置中,设置熔融纺丝单元的温度为210℃,设置纺丝速度为18米/分钟,控制聚丙烯纤维的直径在0.2-0.4μm;(1) Polypropylene fibers are obtained after the polypropylene is melt-spun in the fiber weaving device; wherein, in the fiber weaving device, the temperature of the melt spinning unit is set to 210° C., the spinning speed is set to 18 m/min, and the control The diameter of polypropylene fibers is 0.2-0.4 μm;
将聚丙烯纤维经过静电吸附单元的静电作用、吸附作用及自身温度作用后,形成孔隙率为42.3%,厚度为20μm的聚丙烯纤维聚集体;其中,在静电吸附单元中,控制静电摆丝电压为45kV,吸附风大小为-0.09MPa;After the polypropylene fiber is subjected to the electrostatic action, adsorption action and its own temperature action of the electrostatic adsorption unit, a polypropylene fiber aggregate with a porosity of 42.3% and a thickness of 20 μm is formed; in which, in the electrostatic adsorption unit, the electrostatic wobble voltage is controlled. It is 45kV, and the adsorption wind size is -0.09MPa;
(2)将聚丙烯纤维聚集体从纤维编织装置中传送至预氧化装置中处理;其中,处理温度为350℃,处理时间为5min;(2) Transfer the polypropylene fiber aggregates from the fiber weaving device to the pre-oxidation device for treatment; wherein, the treatment temperature is 350° C., and the treatment time is 5 minutes;
(3)聚丙烯纤维聚集体经预氧化后,传送至碳化装置进行碳化处理;其中,碳化温度为1800℃,处理时间为8min,碳化后,即形成集流体,形成的集流体孔隙率为30.7%,厚度为15.2μm;(3) After pre-oxidation, the polypropylene fiber aggregates are sent to the carbonization device for carbonization treatment; wherein, the carbonization temperature is 1800 ° C, and the treatment time is 8 minutes. After carbonization, a current collector is formed, and the formed current collector has a porosity of 30.7 %, the thickness is 15.2μm;
(4)将步骤(3)中制得的集流体传送至冷却装置降温至室温,再经过收卷轴装置收集成卷。(4) The current collector prepared in step (3) is sent to a cooling device to cool down to room temperature, and then collected into a roll through a winding shaft device.
进一步,本实施例还提供了含有上述集流体的锂离子二次电池,具体制备过程如下:将磷酸铁锂正极浆料涂覆在上述集流体上,95℃下烘干、辊压、分切、卷绕后得到容量为4Ah的26650圆柱锂离子二次电池。其中,正极极片的配比为:以质量分数计,磷酸铁锂94%,Super P 3%,PVDF 3%,压实密度为2.45g/cm3。Further, this embodiment also provides a lithium ion secondary battery containing the above current collector, and the specific preparation process is as follows: coating the lithium iron phosphate positive electrode slurry on the above current collector, drying at 95 ° C, rolling, slitting , After winding, a 26650 cylindrical lithium-ion secondary battery with a capacity of 4Ah was obtained. Among them, the ratio of the positive electrode pieces is as follows: in terms of mass fraction, lithium iron phosphate is 94%, Super P is 3%, PVDF is 3%, and the compaction density is 2.45g/cm 3 .
实施例4Example 4
本实施例提供了一种集流体,其制备方法具体步骤如下:The present embodiment provides a current collector, and the specific steps of its preparation method are as follows:
(1)将聚丙烯在纤维编织装置中熔融纺丝后得到聚丙烯纤维;其中,在纤维编织装置中,设置熔融纺丝单元的温度为210℃,设置纺丝速度为15米/分钟,控制聚丙烯纤维的直径在0.2-0.4μm;(1) Polypropylene fibers are obtained after the polypropylene is melt-spun in the fiber weaving device; wherein, in the fiber weaving device, the temperature of the melt spinning unit is set to 210° C., the spinning speed is set to 15 m/min, and the control The diameter of polypropylene fibers is 0.2-0.4 μm;
将聚丙烯纤维经过静电吸附单元的静电作用、吸附作用及自身温度作用后,形成孔隙率为82.3%,厚度为22μm的聚丙烯纤维聚集体;其中,在静电吸附单元中,控制静电摆丝电压为45kV,吸附风大小为-0.02MPa;After the polypropylene fibers are subjected to the electrostatic effect, adsorption effect and self-temperature effect of the electrostatic adsorption unit, a polypropylene fiber aggregate with a porosity of 82.3% and a thickness of 22 μm is formed; wherein, in the electrostatic adsorption unit, the electrostatic wobble voltage is controlled. It is 45kV, and the adsorption wind size is -0.02MPa;
(2)将聚丙烯纤维聚集体从纤维编织装置中传送至预氧化装置中处理;其中,处理温度为350℃,处理时间为3min;(2) transferring the polypropylene fiber aggregates from the fiber weaving device to the pre-oxidizing device for treatment; wherein, the treatment temperature is 350° C., and the treatment time is 3 minutes;
(3)聚丙烯纤维聚集体经预氧化后,传送至碳化装置进行碳化处理;其中,碳化温度为1600℃,处理时间为8min,碳化后,即形成集流体,形成的集流体孔隙率为65.4%,厚度为17.2μm;(3) After pre-oxidation, the polypropylene fiber aggregates are sent to the carbonization device for carbonization treatment; wherein, the carbonization temperature is 1600 ° C, the treatment time is 8 minutes, after carbonization, a current collector is formed, and the formed current collector has a porosity of 65.4 %, the thickness is 17.2μm;
(4)将步骤(3)中制得的集流体传送至冷却装置降温至室温,再经过收卷轴装置收集成卷。(4) The current collector prepared in step (3) is sent to a cooling device to cool down to room temperature, and then collected into a roll through a winding shaft device.
进一步,本实施例还提供了含有上述集流体的锂离子二次电池,具体制备过程如下:将磷酸铁锂正极浆料涂覆在上述集流体上,95℃下烘干、辊压、分切、卷绕后得到容量为4Ah的26650圆柱锂离子二次电池。其中,正极极片的配比为:以质量分数计,磷酸铁锂97%,PVDF3%,压实密度为2.45g/cm3。Further, this embodiment also provides a lithium ion secondary battery containing the above current collector, and the specific preparation process is as follows: coating the lithium iron phosphate positive electrode slurry on the above current collector, drying at 95 ° C, rolling, slitting , After winding, a 26650 cylindrical lithium-ion secondary battery with a capacity of 4Ah was obtained. Among them, the proportion of the positive electrode piece is as follows: in terms of mass fraction, lithium iron phosphate is 97%, PVDF is 3%, and the compaction density is 2.45 g/cm 3 .
实施例5Example 5
一种锂离子二次电池用的集流体的加工系统(连接关系示意图如图1所示),包括依次顺序连接的纤维编织装置1、预氧化装置2、碳化装置3、冷却装置4和收卷轴装置5。A processing system for a current collector for a lithium ion secondary battery (a schematic diagram of the connection relationship is shown in Figure 1), comprising a
其中,纤维编织装置1包括:熔融纺丝单元11和纤维聚集体制备单元12;Wherein, the
熔融纺丝单元11用于对聚合物进行熔融和纺丝,以得到聚合物纤维;The melt spinning unit 11 is used to melt and spin polymers to obtain polymer fibers;
纤维聚集体制备单元12用于将聚合物纤维制成纤维聚集体;在纤维聚集体制备单元12中,含有静电吸附元件121,静电吸附元件121用于将聚合物纤维通过静电作用和吸附作用制成纤维聚集体;The fiber
熔融纺丝单元11的出口与纤维聚集体制备单元12的入口相连接;The outlet of the melt-spinning unit 11 is connected to the inlet of the fiber
纤维聚集体制备单元12的出口与预氧化装置2的入口相连接;The outlet of the fiber
预氧化装置2的出口与碳化装置3的入口相连接;The outlet of the
在碳化装置3的出口,依次顺序连接冷却装置4和收卷轴装置5;At the outlet of the
其中,冷却装置4将制备得到的高温集流体冷却降至室温,最后通过收卷轴装置5将冷却后的集流体收集成卷。Wherein, the
对比例1Comparative Example 1
本对比例提供了一种锂离子二次电池,具体制备过程如下:将磷酸铁锂正极浆料涂覆在普通涂碳铝箔集流体上,95℃下烘干、辊压、分切、卷绕后得到容量为4Ah的26650圆柱锂离子二次电池。其中,正极极片的配比为:以质量分数计,磷酸铁锂94%,Super P 3%,PVDF 3%,压实密度为2.45g/cm3。This comparative example provides a lithium ion secondary battery, and the specific preparation process is as follows: coating the lithium iron phosphate positive electrode slurry on an ordinary carbon-coated aluminum foil current collector, drying at 95°C, rolling, slitting, winding Afterwards, a 26650 cylindrical lithium-ion secondary battery with a capacity of 4Ah was obtained. Among them, the ratio of the positive electrode pieces is as follows: in terms of mass fraction, lithium iron phosphate is 94%, Super P is 3%, PVDF is 3%, and the compaction density is 2.45g/cm 3 .
对比例2Comparative Example 2
本对比例提供了一种锂离子二次电池,具体制备过程如下:将磷酸铁锂正极浆料涂覆在普通铝箔集流体上,95℃下烘干、辊压、分切、卷绕后得到容量为4Ah的26650圆柱锂离子二次电池。其中,正极极片的配比为:以质量分数计,磷酸铁锂94%,Super P 3%,PVDF3%,压实密度为2.45g/cm3。This comparative example provides a lithium ion secondary battery, and the specific preparation process is as follows: coating the lithium iron phosphate positive electrode slurry on an ordinary aluminum foil current collector, drying at 95°C, rolling, slitting, and winding to obtain A 26650 cylindrical lithium-ion secondary battery with a capacity of 4Ah. Among them, the proportion of the positive electrode piece is as follows: in terms of mass fraction, lithium iron phosphate is 94%, Super P is 3%, and PVDF is 3%, and the compaction density is 2.45 g/cm 3 .
试验例Test example
对上述实施例和对比例制备的锂离子二次电池性能进行测试,结果如表1所示。The performances of the lithium ion secondary batteries prepared in the above examples and comparative examples were tested, and the results are shown in Table 1.
其中,极片粘结力测试方法:将辊压后的极片裁剪成200*20mm大小,在极片表面贴有同尺寸的高温胶纸,使用万能实验机以1mm/s速度进行剥离,剥离过程中的最小值即为极片粘结力。Among them, the test method of the adhesion of the pole piece: cut the pole piece after rolling into a size of 200*20mm, paste the high temperature tape of the same size on the surface of the pole piece, use a universal testing machine to peel off at a speed of 1mm/s, peel off The minimum value in the process is the pole piece cohesion.
极片阻抗测试方法:将辊压后的极片剪切成4cm*8cm的方形尺寸,把剪切好的极片置于BER2200测试仪探头之间,施加5MPa压力,读取数值。Pole piece impedance test method: Cut the rolled pole piece into a square size of 4cm*8cm, place the cut pole piece between the probes of the BER2200 tester, apply 5MPa pressure, and read the value.
电池内阻测试方法:使用RJ3563内阻测定仪在1000Hz条件下测试电池内阻。Battery internal resistance test method: use RJ3563 internal resistance tester to test the battery internal resistance under the condition of 1000Hz.
表1性能测试结果Table 1 Performance test results
从表1可以看出,实施例1-4与对比例相比,采用本发明制备的集流体的锂离子二次电池,即使不加导电剂,极片粘结力要显著优于普通涂碳铝箔和普通铝箔,而且极片阻抗、电池内阻远低于采用普通涂碳铝箔和普通铝箔作为集流体的锂离子二次电池。可见,采用本发明制备的集流体的锂离子二次电池,其正极片粘结力、极片阻抗、电池内阻均比商用涂碳铝箔以及普通铝箔优秀。As can be seen from Table 1, compared with the comparative example, the lithium ion secondary battery using the current collector prepared by the present invention, even if no conductive agent is added, the adhesion force of the pole piece is significantly better than that of ordinary carbon coating Aluminum foil and ordinary aluminum foil, and the electrode impedance and battery internal resistance are much lower than those of lithium-ion secondary batteries using ordinary carbon-coated aluminum foil and ordinary aluminum foil as current collectors. It can be seen that the lithium ion secondary battery using the current collector prepared by the present invention has better positive electrode adhesion, electrode resistance and battery internal resistance than commercial carbon-coated aluminum foil and ordinary aluminum foil.
虽然,上文中已经用一般性说明及具体实施方案对本发明作了详尽的描述,但在本发明基础上,可以对之作一些修改或改进,这对本领域技术人员而言是显而易见的。因此,在不偏离本发明精神的基础上所做的这些修改或改进,均属于本发明要求保护的范围。Although the present invention has been described in detail above with general description and specific embodiments, some modifications or improvements can be made on the basis of the present invention, which will be obvious to those skilled in the art. Therefore, these modifications or improvements made without departing from the spirit of the present invention fall within the scope of the claimed protection of the present invention.
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CN110010860A (en) * | 2019-03-01 | 2019-07-12 | 深圳鸿鹏新能源科技有限公司 | Composite negative pole material and lithium ion battery for lithium ion battery |
CN217544661U (en) * | 2022-02-07 | 2022-10-04 | 大连中比动力电池有限公司 | Processing system of current collector for lithium ion secondary battery |
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