市場調查報告書
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LIB乾電池電極流程的技術開發的趨勢與預測<2024> Technology Development Trends and Prospects of Dry Battery Electrode Process for LIBs |
雖然電動車本身不排放溫室氣體,但有人批評電動車的製造過程會排放碳,破壞環境。一個典型的例子是電池,它約佔電動車製造成本的40%。
電池製造過程消耗大量電能,尤其是乾燥和收集NMP,會造成溫室氣體排放。根據一項研究,濕式製造過程中的溶劑乾燥每千瓦時會產生 42 公斤二氧化碳,也會將環境污染物揮發性有機化合物 (VOC) 釋放到大氣中。另一方面,乾電極不需要溶劑乾燥或回收過程,因此耗電量較少,不排放揮發性有機化合物,是一種環保製程。
為了提高能量密度,需要超過100μm的厚膜電極。在目前的濕式製程中,由於溶劑和材料的層分離現象,很難製造厚膜電極。活性物質、導電材料、黏結劑等的比重不同,因此如果塗層較厚,黏結劑和導電材料就會漂浮在電極表面。在濕式製程中,很難塗覆厚度大於約 100 μm 的電極。
透過使用乾法,活性材料、導電材料和黏合劑可以均勻分散,而不會引起這種層分離現象,從而可以製造厚膜電極並提高電池容量和能量。
2019年,特斯拉收購了擁有乾電極技術的超級電容器公司Maxwell Technologies,並在2020年9月的電池日上宣布推出乾電極。兩年後的 2021 年,特斯拉將 Maxwell 賣給了 UCAP,但卻獲得了乾電極技術。據直接拿到並分析特斯拉4680電池的專家介紹,這款電池僅在負極上應用了乾電極,在正極上採用了現有的濕電極。
目前尚不清楚特斯拉為何尚未將乾電極製程應用到正極上,但有分析指出乾電極製程良率較低,無法量產。外媒也有報導稱,4680電池的低良率正在影響Cybertruck的生產。
儘管乾沉積製程的原理很簡單,但在實施的每個階段都存在相當大的課題。在不使用溶劑的情況下,均勻地混合活性材料、導電材料和黏合劑並不容易。將非黏性粉末均勻地施加到集流體上更加困難。如果產量差,生產成本也會高。儘管引入乾電極是為了降低成本,但它們實際上會增加成本。
目前,除了特斯拉之外,國內外企業均宣布正在開發P/P規模的乾法工藝,但初期生產的直徑46毫米的圓柱電池均將採用濕法工藝生產這就是前景。 LGES將於2024年第四季以P/P規模生產的4680電池,正負極均採用濕法工藝,該電池將供應給特斯拉。近日,LGES宣布將於2024年第四季完成梧倉能源工廠的乾電極製程P/P線,並於2028年開始應用。三星SDI、SK On、松下、CATL和Kumyang近年來也宣布了乾電極技術的進展。
此外,2023年6月,德國福斯宣布正在與德國專門生產印刷設備的製造商Koenig & Bauer一起開發乾電極製程。大眾汽車計劃於 2027 年開始工業化生產。目前尚不清楚大眾汽車和 Koenig & Bauer 是如何開發乾電極的。
乾燥過程無需乾燥過程,可降低能源成本30%,乾燥所需面積可減少50%。採用乾式製程的4680電池理論上可能比磷酸鐵鋰電池便宜,但該技術尚未開發成功。
乾法製程的引入作為碳中性鋰二次電池製造製程具有巨大潛力,乾電極技術的實際應用有望對提高性能和降低電池製造成本做出巨大貢獻。雖然目前還沒有一家公司成功量產,但隨著各大公司加速技術開發,乾電極製程很可能在不久的將來成為一種趨勢。乾電極製程的開發還可應用於下一代電池、全固態電池的製造流程。事實上,國內外對全固態電池的興趣日益濃厚,量產計畫也正在進行中。
在本報告中,我們對二次電池產業進行了研究和分析,並提供了開發碳中和製程的必要性、現有濕式製程的問題以及目前乾式製程的問題等技術資訊。
優點 | 超級電容 | 緊湊 | ||
課題 | 偏旁析的風險 | 偏旁析的風險 | 偏旁析的風險 | 混合 |
主要企業 | Tesla (Maxwell Technologies) | Technical Univ. Dresden Fraunhofer IWS |
Technical Univ. Dresden Fraunhofer ISIT |
Technical Univ. Braunschweig Fraunhofer IPA |
TRL | 6 | 5 | 4->6 | 4->6 |
參考文獻 | US Patent US2006/0133012A1 10/817 590. Apr. 1. 2008. | Germany Patent DE102017208220A1. Nov. 22. 2018. | Proc. Fraunhofer ISIT - Achievements Results Annu. Rep., 2017.pp.32-33 | Energy Technol., vol. 8, no. 2. 2020. Art. no. 1900309 |
Electric vehicles themselves do not emit greenhouse gases, but the manufacturing process of electric vehicles has been criticized for emitting carbon and destroying the environment. A representative example is the battery, which accounts for about 40% of the manufacturing cost of electric vehicles.
During the battery manufacturing process, a considerable amount of electric energy is consumed, especially in drying and recovering NMP, which is a cause of greenhouse gas emissions. According to one research result, 42 kg of CO2 is generated per kWh due to solvent drying in the wet manufacturing process, and volatile organic compounds (VOCs), which are environmental pollutants, are also emitted into the atmosphere. In contrast, dry electrodes do not have a solvent drying and recovery process, so they consume less electric energy and do not emit VOCs, making them an environmentally friendly process.
In order to increase energy density, a thick film electrode of >100 micrometer or more is required. In the current wet process, it is difficult to make a thick film electrode due to the layer separation phenomenon between the solvent and the material. Since the specific gravity of each material such as the active material, conductive material, and binder is different, if the coating is thick, the binder and conductive material float to the electrode surface. In the wet process, it is difficult to coat the electrode with a thickness of about 100 micrometer or more.
By using a dry process, the active material-conductive material-binder can be evenly distributed without this layer separation phenomenon, so a thick-film electrode can be created, which can increase the capacity and energy density of the battery.
In 2019, Tesla acquired Maxwell Technologies, a supercapacitor company with dry electrode technology, and announced at Battery Day in September 2020 that it would introduce dry electrodes. Tesla sold Maxwell to UCAP in 2021, two years later, but was able to secure dry electrode technology. According to experts who directly obtained and analyzed the Tesla 4680 battery, the battery applied a dry electrode only to the anode, and the existing wet electrode was adopted for the cathode.
It is not known why Tesla has not yet applied the dry electrode process to the cathode, but there is analysis that the yield of the dry electrode process is low and cannot be mass-produced. There are also foreign media reports that the low yield of the 4680 battery is affecting the production of the Cybertruck.
The principle of the dry coating process is simple, but there are considerable challenges at each stage in implementing it in practice. It is not easy to evenly mix the active material, conductive material, and binder without using a solvent. It is even more difficult to evenly apply the non-viscous powder to the current collector. If the yield is low, the production cost increases. Dry electrodes were introduced to reduce costs, but they can actually act as a cost increase factor.
In addition to Tesla, domestic and foreign companies are currently announcing that they are developing a P/P scale dry process, but it is expected that all 46-phi cylindrical batteries to be initially produced will be produced using a wet process. The 4680 battery that LGES will produce in the fourth quarter of 2024 on a P/P scale will apply a wet process to both cathode and anode, and this battery will be supplied to Tesla. Recently, LGES announced that it will complete the construction of a dry electrode process P/P line in the Ochang Energy Plant in the fourth quarter of 2024 and will apply it starting in 2028. Samsung SDI, SK On, Panasonic, CATL, and Kumyang, which recently announced that they are also developing dry electrode technology.
In addition, Volkswagen of Germany announced in June 2023 that it was developing a dry electrode process with Koenig & Bauer, a German printing equipment specialist. Volkswagen plans to start industrial production by 2027. It is not known exactly how Volkswagen and Koenig & Bauer are developing the dry electrode.
The dry process can reduce energy costs by 30% because the drying process is unnecessary, and the area required for drying can be reduced by 50%. The 4680 battery using the dry process can theoretically be cheaper than the LFP battery, but the technology development has not been successful yet.
The introduction of the dry process has great potential as a carbon-neutral process for manufacturing lithium secondary batteries, and the commercialization of dry electrode technology is expected to greatly contribute to reducing battery manufacturing costs while improving performance. Although no company has succeeded in mass production so far, it is very likely that the dry electrode process will become a trend in the near future as major companies are spurring technology development. In addition, the development of the dry electrode process can be applied to the manufacturing process of all-solid-state batteries, which are next-generation batteries. In fact, interest in all-solid-state batteries is increasing both domestically and internationally, and plans for mass production are being established.
This report provides technical information such as the necessity of developing a carbon-neutral process in the secondary battery industry, issues with the existing wet process, and issues with the current dry process, as well as information on recent development trends in dry electrode processes and all-solid-state battery development by many companies, with the aim of forecasting the current and near-future status of the dry process.
Advantages | Super caps | compact | ||
Challenges | Risk of segregation | Risk of segregation | Risk of segregation | mixing |
Key players | Tesla(Maxwell Technologies | Technical Univ. Dresden Fraunhofer IWS | Technical Univ. Dresden Fraunhofer ISIT | Technical Univ. Braunschweig Fraunhofer IPA |
TRL | 6 | 5 | 4->6 | 4->6 |
References | US Patent US2006/0133012A1 10/817 590. Apr. 1. 2008. | Germany Patent DE102017208220A1. Nov. 22. 2018. | Proc. Fraunhofer ISIT - Achievements Results Annu. Rep., 2017.pp.32-33 | Energy Technol., vol. 8, no. 2. 2020. Art. no. 1900309 |