LITHIUM ION BATTERY AND METHOD FOR MANUFACTURING OF SUCH BATTERY
锂金属电池 隔膜离子通量

锂金属电池隔膜离子通量英文回答:Lithium metal batteries are a type of rechargeable battery that use lithium metal as the anode. Thesebatteries have gained significant attention in recent years due to their high energy density and potential for use in electric vehicles and other portable electronic devices. One of the key components in lithium metal batteries is the ion-permeable membrane, also known as the separator, which plays a crucial role in allowing the transport of lithium ions between the cathode and the anode.The ion flux through the separator is an important factor that determines the performance and safety oflithium metal batteries. The ion flux refers to the rate at which lithium ions can pass through the separator. A higher ion flux means that more lithium ions can move through the separator, resulting in faster charging and discharging rates. On the other hand, a lower ion flux can limit thebattery's performance and lead to issues such as capacity loss and increased internal resistance.There are several factors that can affect the ion flux through the separator. One of the main factors is the porosity of the separator. A more porous separator allows for a higher ion flux as it provides more pathways for the lithium ions to move through. However, if the porosity is too high, it can also lead to issues such as dendrite growth, which can cause short circuits and safety hazards.The thickness of the separator also plays a role in the ion flux. A thinner separator can result in a higher ion flux as it reduces the diffusion distance for the lithium ions. However, a thinner separator may also be more prone to mechanical damage and can increase the risk of short circuits.The choice of separator material is another important factor. Different separator materials have different ion permeability, which can affect the ion flux. For example, ceramic separators typically have lower ion permeabilitycompared to polymer separators. However, ceramic separators are more resistant to thermal and mechanical stress, making them suitable for high-temperature applications.In addition to these factors, the electrolyte composition and temperature can also influence the ion flux through the separator. A higher concentration of lithium ions in the electrolyte can result in a higher ion flux. Similarly, an increase in temperature can enhance the mobility of lithium ions and increase the ion flux.Overall, the ion flux through the separator is acritical parameter that affects the performance and safety of lithium metal batteries. By optimizing factors such as porosity, thickness, and material choice, researchers and engineers can improve the ion flux and enhance the overall efficiency and reliability of lithium metal batteries.中文回答:锂金属电池是一种使用锂金属作为阳极的可充电电池。
新高考2025版高考英语一轮复习微专题小练习练习52语法填空+阅读理解

练习52 语法填空+阅读理解Ⅰ.语法填空officially 1.________ the United Nations on November 27th, 2024. To celebrate 2.________ festival, a number of events took place at the Chinese Businessman Museum in Beijing on Thursday.The chairman of the China Culture Promotion Society 3.________ (address) the opening ceremony. “As a main promoter of the International Tea Day, the birthplace of tea and the 4.________ (large) teaprodu cing country, China has a 5.________ (responsible) to work with other countries to promote the healthy development of the tea industry. It can help to build a community with a 6.________ (share) future for mankind,” he said.The “First International Tea Day Tea Road Cooperative Initiative” issued (发布) at the ceremony calls for people working in the tea industry to come together to promote international cooperation 7.________ cultural exchanges. A fouryear tea promotion—Tea Road Cooperative Plan—was also issued in accordance with the initiative.8.________ (strengthen) the connection with young people, the event included a number of public promotional activities on social media, 9.________ (invite) twentynine tea professionals from around the world to have thirtysix hours of uninterrupted live broadcasts.The Chinese Ancient Tea Museum was officially unveiled (揭幕) at the ceremony, opening 10.________ (it) first exhibition: The Avenue of Truth—A Special Exhibition of Pu'er Tea.Ⅱ.阅读理解Atheir vehicle for more than a thousand miles on a single charge. Researchers have developed a lithiumair battery that could make that dream a reality. The new battery design could also one day power airplanes and trucks. The main new component in this lithiumair battery is a solid electrolyte (电解质) instead of the usual liquid variety.Batteries with solid electrolytes are not subject to safety problems with the liqu id electrolytes used in lithiumion and other battery types, which can overheat and catch fire. More importantly, the solid electrolyte can potentially boost the energy four times, which translates into longer driving range.For over a decade, scientists have been working overtime to develop a lithium (锂) battery that makes use of the oxygen in air. The lithiumair battery has the highest energy of any battery technology being considered for the nextgeneration of batteries beyond lithiumion.The new solid electrolyte is composed of a material made from relatively inexpensive elements, compared with the past designs. Besides, the chemical reaction in lithiumion only involves one or two electrons stored per oxygen molecule (分子), while that for t he lithiumair battery involves four electrons. More electrons stored means higher energy.The new design is the first lithiumair battery that has achieved a fourelectron reaction at room temperature. It also operates with oxygen supplied by air from the surrounding environment. The capability to run with air avoids the need for oxygen tanks to operate, a problem with earlier designs.“With further development, we expect our new design for the lithiumair battery to reach a record of 1,200 w atthours per kilogram,” said Curtiss, a researcher. “That is nearly four times better than lithiumion batteries.”1.What contributes most to the lithiumair battery?A.Lithiumion. B.Oxygen molecules.C.Solid electrolytes. D.Liquid components.2.What's the problem with lithiumion batteries?A.They burn easily if overheated.B.They are unsafe in production.C.They damage the environment.D.They require longer charging time.3.How does the author organize Paragraph 4?A.By giving examples.B.By making comparisons.C.By presenting statistics.D.By analyzing cause and effect.4.What is the best title of the text?A.How Lithiumair Batteries WorkB.What Will Be Used to Power AirplanesC.Electric Cars Are Becoming More PopularD.New Batteries Offer Longer Driving RangeBGrizzly bears, which may grow to about 2.5 m long and weigh over 400 kg, occupy a conflicted corner of the American psyche—we revere (敬畏) them even as they give us frightening dreams. Ask the tourists from around the world that flood into Yellowstone National Park what they most hope to see, and their answer is often the same: a grizzly bear.“Grizzly bears are reoccupying large areas of their former range,” says bear biologist Chris Servheen. As grizzly bears expand their range into places where they haven't been seen in a century or more, they're increasingly being sighted by humans.The western half of the U.S. was full of grizzlies when Europeans came, with a rough number of 50,000 or more living alongside Native Americans. By the early 1970s, after centuries of cruel and continuous hunting by settlers, 600 to 800 grizzlies remained on a mere 2 percent of their former range in the Northern Rockies. In 1975, grizzlies were listed under the Endangered Species Act.Today, there are about 2,000 or more grizzly bears in the U.S. Their recovery has been so successful that the U.S. Fish and Wildlife Service has twice attempted to delist grizzlies, which would loosen legal protections and allo w them to be hunted. Both efforts were overturned due to lawsuits from conservation groups. For now, grizzlies remain listed.Obviously, if precautions (预防) aren't taken, grizzlies can become troublesome, sometimes killing farm animals or walking through yards in search of food. If people remove food and attractants from their yards and campsites, grizzlies will typically pass by without trouble. Putting electric fencing around chicken houses and other farm animal quarters is also highly effective at gettin g grizzlies away. “Our hope is to have a clean, attractantfree place where bears can pass through without learning bad habits,” says James Jonkel, longtime biologist who manages bears in and around Missoula.5.How do Americans look at grizzlies?A.They cause mixed feelings in people.B.They should be kept in national parks.C.They are of high scientific value.D.They are a symbol of American culture.6.What has helped the increase of the grizzly population?A.The European settlers' behavior.B.The expansion of bears' range.C.The protection by law since 1975.D.The support of Native Americans.7.What has stopped the U. S. Fish and Wildlife Service from delisting grizzlies?A.The opposition of conservation groups.B.The successful comeback of grizzlies.C.The voice of the biologists.D.The local farmers' advocates.8.What can be inferred from the last paragraph?A.Food should be provided for grizzlies.B.People can live in harmony with grizzlies.C.A special path should be built for grizzlies.D.Technology can be introduced to protect grizzlies.答题策略语法填空——冠词练习52 语法填空+阅读理解Ⅰ.语法填空【语篇解读】本文是一篇说明文。
锂离子电池用户手册 Lithium-ion Battery User's Guide

环宇电源股份有限公司HUANYU POWER SOURCE CO., LTD锂离子电池使用手册Lithium-ion Battery User’s Guide在使用环宇锂离子电池前,请仔细阅读使用手册。
Please read all contents of this User’s Guide prior to the installation of HuanYu lithium-ion battery.安全信息safety information必须按照环宇锂离子电池的产品特性和使用手册使用,若按照使用手册合理的使用,锂离子电池将是一种安全、可靠和便利的蓄电池。
The HuanYu lithium-ion battery must be used in accordance with the manufacture’s specifications and guidelines for recommended use. When used properly and in accordance with the user’s guide, the lithium-ion battery is a safe, reliable and convenient secondary battery.警告CAUTION:不正确使用锂离子电池可能导致人身伤害或者起火!Misuse or abuse of the lithium-ion battery may result in personal injury or fire.l保证电池和电池管理系统远离危险物品或者危险材料l Keep all battery pack and battery management system away fromdangerous goods or materialsl烫伤危险l Burn hazardl不合理使用锂离子电池可能会导致冒烟(例如过充电、挤压、刺穿、过热或者潮湿),如果发生冒烟,请及时通风疏散l Abuse operation of the battery (e.g.,overcharge,crush,puncture,excessive heat or moisture )may produce smoke. In such an event,ventilate the areal用二氧化碳或者干粉灭火器灭火,或者用沙土、泥土掩埋l Extinguish any flames with a carbon dioxide,dry-powder fireextinguisher,or cover with sand or mudl禁止拆开、挤压、刺穿或者燃烧l Do not disassemble,crush,puncture or incineratel禁止短路l Do not short circuitl禁止暴露在60℃以上的温度中l Do not expose to temperature above 60℃l禁止在没有充电保护线路或者使用非环宇认可的设备充电l Never charge the battery without charge protection circuitry and equipment approved by HuanYul安装电池时请取下金属首饰或者其他金属物品l Remove all jewelry or other metallic objects during the installation of the batteryl小心取放任何电池,特别是在放入金属容器的过程中l Exercise care in handing any battery,particularly when placing it ina contains with metal objectsl禁止将电池丢弃到垃圾中l Do not throw the battery away in the trashl禁止将其他类型的电池与锂离子电池串联或者并联l Do not use with other types of batteries connected in series or parallel with the lithium-ion battery安装installation重要important!安装电池前必须关闭汽车或者设备电源,并且移除其他类型的电池。
机载锂电池SOC估算方法研究与实现

机载锂电池SOC估算方法研究与实现王顺利;尚丽平;屈维;舒思琦;葛承栋【摘要】为了解决机载锂电池的荷电状态估算问题,针对飞机应急供电这一特殊运行环境,提出了一种基于扩展卡尔曼滤波的机载锂电池荷电状态估计方法.该方法通过构建状态方程和量测方程,经历预测、修正和估算3阶段,实现对机载锂电池的荷电状态估算.基于该方法设计并实现了机载锂电池地面检测与维护设备.实验结果表明,该方法能够实现机载锂电池的荷电状态有效估算,提高了锂电池机载运行的可靠性和稳定性.【期刊名称】《实验技术与管理》【年(卷),期】2015(032)005【总页数】6页(P45-49,54)【关键词】锂电池;荷电状态;EKF;健康状态【作者】王顺利;尚丽平;屈维;舒思琦;葛承栋【作者单位】西南科技大学信息工程学院,四川绵阳 621010;特殊环境机器人技术四川省重点实验室,四川绵阳 621010;西南科技大学信息工程学院,四川绵阳621010;特殊环境机器人技术四川省重点实验室,四川绵阳 621010;西南科技大学信息工程学院,四川绵阳 621010;西南科技大学信息工程学院,四川绵阳 621010;西南科技大学信息工程学院,四川绵阳 621010【正文语种】中文【中图分类】TM912锂离子聚合物蓄电池(锂电池)相对于铅酸、镍镉等材料蓄电池具有能量密度高、安全稳定等优点,是现代洁净能源发展的趋势[1-2]。
动力锂电池组的荷电状态(state of charge,SOC)估计是锂电池应用的重点和难点之一。
锂电池SOC的估算是基于充放电电流、温度、电压等参数估算电池剩余电量[3],SOC是电池组所处状态最直接反映,电池的不一致性也最先体现在各单体电池的SOC 值不一致上[4]。
根据单体电池间SOC 值的大小差异,选择适当均衡方案,可以有效地延长锂电池的使用寿命[5]。
SOC的估算是目前蓄电池应用研究的热点[6-18],但受各种原因的限制,目前工业应用的蓄电池检测与维护系统中的SOC估计算法仍不完善,相当部分的产品也只采用比较基础的安时积分法、开路电压法等实现。
Li(NiCoMn)O2多极氧磷酸酸钠电池商品说明书

Polymer Lithium-ion Li(NiCoMn)O2 Battery Product SpecificationModel:NCM-9789182-2CAll 7 Sheets1、ScopeThis product specification describes this polymer lithium-ion battery. Please use the test methods that recommend in this specification. If you have any opinions or advices about the test items and methods, please contact us. Please read the cautions recommended in the specifications first, take the credibility measure of the cell’s using.If the cells should be using at the environment that not preferred in this document, please connect us first and get our authorization. For the reason of stable performance and better safety, battery pack with more than 2 cells connected in serial way should be charged with a balance charger.It is claimed that we should have no any responsibility with the contingency and loss due to the cells’ wrong usage (not preferred in the product specification).5.Environment Performance8. Cautions8.1Cautions of batteries’ operationThe batteries must be careful of proceed the operation for its soft package.8.1.1 Aluminum packing materialsThe aluminum packing material was easily damaged by the sharp edge part, such as nickel-tabs.⑴forbid to use the sharp part touching the battery;⑵should cleaning working condition, avoiding the sharp edge part existence;⑶forbid to pierce the battery with nail and other sharp items;⑷the battery was forbidden with metal, such as necklace, hairpin etc in transportation and storage.8.1.2 Sealed edgeSealing edge is very easily damaged and don’t bend it.Cathode Al-tabFig.1. Exterior schematic of polymer lithium-ion cellsThe folding edge is formed in batteries’processes and passed all hermetic tests, don’t open or deform it.of package has good electric performance. It’s forbiddencomponent for preventing short-circuits.Al interlayer Reverse folding insulatedFig.2. Single folding edge schematic of PL cells Fig.3. Reverse folding edge schematic of PL cells8.1.4 Tabs⑴The batteries’ tabs are not so stubborn especially for aluminum tabs. Don’t bend tabs.⑵The tab-tapes are used to isolate The anode /cathode tabs from Aluminum packing materials to preventshort-circuit, so prohibit manicuring of the tab-tapes.8.1.5 Mechanical shock⑴Don’t fall, hit, bent the batteries’ body.⑵Don’t knock on by sinker or trample the batteries.⑶Don’t sling the batteries.8.1.6 Short-circuitShort-circuit is strictly prohibited. It should damage batteries badly.⑴Don’t connect the anode and cathode of the batteries to avoid short-circuit.⑵Prohibit short-circuit of the anode (or cathode) and aluminum layer of Aluminum packing materials.8.2Standard Test Environment for polymer lithium-ion batteriesEnvironment temperature: 20±5℃Humidity: 45-85%8.3Cautions of charge & discharge8.3.1 ChargeCharging current should be lower than values that recommend below. Higher current and voltage charging may cause damage to cell electrical, mechanical, safety performance and could lead heat generation or leakage.⑴Batteries charger should charging with constant current and constant voltage mode;⑵Charging current should be lower than (or equal to )1C5A;⑶Temperature 0~45℃is preferred when charging;⑷Charging voltage must be lower than 4.25V.8.3.2 Discharge⑴Discharging current must be lower than (or equal to )2C5A;⑵Temperature -10~60℃is preferred when discharging;⑶Discharging voltage must not be lower than 2.75V.8.3.3 Over-dischargeIt should be noted that the cell would be at an over-discharge state by its self-discharge. In order to prevent over-discharge, the cell shall be charged periodically to keeping voltage between 3.6-3.9V.Over-discharge may cause loss of cell performance. It should be noted that the cell would not discharge till voltage lower than 2.5V.8.4 Storage of polymer lithium-ion batteriesThe battery should be stored with 40-60% charge state.The environment of long-time storage:Temperature: 20±5℃;Humidity: 65±20%;Batteries were 40~60% charged.In case of over-discharge, batteries should be charged for one time every 3 months while storing. Batteries should be discharged and charged after being stored more than a year in order to activate it and restore energy. Please charge the battery with constant current 0.5C5A for 1 hour so that it has some storage of charge for properly using.Charge and discharge afresh to active and renew battery energy after storage above 1 year.8.5. Transportation of polymer lithium-ion batteriesThe batteries should transportation with 10~50% charged states.8.6. OthersPlease note the following cautions to prevent cells’ leakage, heat generation and explosion.⑴Prohibit disassembly cells;(2) Prohibit immersion cells into liquid such as water or seawater;(3) Prohibition of dumping cells into fire;(4) Prohibit soldering directly the battery;(5) Prohibit charging the battery near fire or in the hot circumstance;(6) Prohibit placing battery in a microwave oven or pressurized container;(7) Prohibit use or store the battery where is exposed to extremely hot, such as under window of a car indirect sunlight in a hot day. Otherwise the battery may be overheated. This can also reduce battery performance and/or shorten service life.(8) If the battery leaks and electrolyte gets in your eyes, do not rub them. Instead, rinse eyes with cleanrunning water and immediately seek medical attention. If left as is, electrolyte can cause eye injury.(9) Prohibit using the battery if it gives off an odor, generates heat, becomes discolored or deformed, orappears abnormal in any way. If the battery is in use or being recharged, remove it from the device or charger immediately and discontinue use. If the battery leaks or gives off an odor, move it away from a fire source to avoid fire or explosion.9. Notice of Designing Battery Pack9.1 Pack designBattery pack should have sufficient strength and battery should be protected from mechanical shock. No sharp edge components should be inside the pack contains the battery.9.2 PCM designThe overcharge threshold voltage should not be exceeding 4.25V.The over-discharge threshold voltage should not be lower than 2.3V.The PCM should have short protection function built inside.9.3 Tab connectionUltrasonic welding or spot welding is recommended to connect battery with PCM or other parts.If apply manual solder method to connect tab with PCM, the notice below is very important to ensure battery performance.⑴The electric iron should be temperature controlled and ESD safe;⑵Soldering temperature should not exceed 350℃;⑶Soldering time should not be longer than 3s, keep battery tab cold down before next soldering;⑷Soldering times should not exceed 5 times;⑸Soldering Spot location should be away from the tab film to ensure the sealing of the tab film;(6) The soldering spot should be smooth and there should be no accumulation.Fig.4. Schematic of wrong assembly10. Schematic of Battery:。
Ryobi 18V Lithium-Ion Battery Pack P108 说明书

Anderson, SC 29625
(for Outdoor Products): 1-800-860-4050
Emergency Contact Number: Chemtrec (United States only): 1-800-424-9300 (International): +1-703-741-5970
wash immediately with soap and water. If fluid gets into your eyes, flush them with clean water for at least 10 minutes, then seek immediate medical attention. Following this rule will reduce the risk of serious personal injury. • Battery cells and battery pack assembly will burn if incinerated.
SECTION 2: HAZARDS IDENTIFICATION
Refer to battery cell SDS for more information. No exposure to hazards during routine handling of product.
WARNING: • To reduce the risk of injury, user must read operator’s manual. • Risk of fire and burns. • Do not open, crush, heat above 50˚C, incinerate, or short terminals. • Follow manufacturer’s instructions. • Use only with charger listed in operator’s manual. • Remove battery from tool when storing, changing attachments, or making adjustments. • To reduce the risk of explosion and possible injury, do not place battery near fire or heat. • Do not crush, drop, or damage battery pack. • Do not use a battery pack that has been dropped or received a sharp blow. A damaged battery is subject to explosion.
锂电池外文资料译文
The design of the lithium battery charger IntroductionLi-Ion rechargeable batteries are finding their way into many applications due to their size, weight and energy storage advantages.These batteries are already considered the preferred battery in portable computer applications, displacing NiMH and NiCad batteries, and cellular phones are quickly becoming the second major marketplace for Li-Ion. The reason is clear. Li-Ion batteries offer many advantages to the end consumer. In portable computers,Li-Ion battery packs offer longer run times over NiCad and NiMH packs for the same form factor and size, while reducing weight. The same advantages are true for cellular phones. A phone can be made smaller and lighter using Li-Ion batteries without sacrificing run time. As Li-Ion battery costs come down, even more applications will switch to this lighter and smaller technology. Market trends show a continual growth in all rechargeable battery types as consumers continue to demand the convenience of portability. Market data for 1997 shows that approximately 200 million cells of Li-Ion will be shipped, compared to 600 million cells of NiMH. However, it is important to note that three cells of NiMH are equivalent to one Li-Ion cell when packaged into a battery pack. Thus, the actual volume is very close to the same for both. 1997 also marked the first year Li-Ion was the battery type used in the majority of portable computers, displacing NiMH for the top spot. Data for the cellular market showed a shift to Li-Ion in the majority of phones sold in 1997 in Europe and Japan.Li-Ion batteries are an exciting battery technology that must be watched. To make sense of these new batteries, this design guide explains the fundamentals, the charging requirements andthe circuits to meet these requirements.Along with more and more the emergence of the handheld electric appliances, to the high performance, baby size, weight need of the light battery charger also more Come more big.The battery is technical to progress to also request continuously to refresh the calculate way more complicatedly is fast with the realization, safety of refresh.Therefore need Want to carry on the more accurate supervision towards refreshing the process, to shorten to refresh time and attain the biggest battery capacity, and prevent°from the batteryBad.The AVR has already led the one step in the competition, is prove is perfect control chip of the next generation charger. The microprocessor of Atmel AVR is current and can provide Flash, EEPROM and 10 ADCses by single slice on the market Of 8 RISC microprocessors of the tallest effect.Because the saving machine of procedure is a Flash, therefore can need not elephant MASK ROM Similar, have a few software editions a few model numbers of stock.The Flash can carry on again to weave the distance before deliver goods, or in the PCB Stick after pack carry on weaving the distance throughan ISP again, thus allow to carry on the software renewal in the last one minute.The EEPROM can used for conservancy mark certainly coefficient and the battery characteristic parameter, such as the conservancy refreshes record with the battery that raise the actual usage Capacity.10 A/ Ds conversion machine can provide the enough diagraph accuracy, making the capacity of the good empress even near to its biggest capacity. And other project for attaining this purpose, possible demand the ADC of the exterior, not only take up the space of PCB, but also raised the system Cost.The AVR is thus deluxe language but 8 microprocessors of the designs of unique needle object" C" currently.The AT90S4433 reference The design is with" C" to write, the elucidation carries on the software design's is what and simple with the deluxe language.Code of C this design is very Carry on adjust easily to suit current and future battery.But the ATtiny15 reference design then use edit collected materials the language to write of, with Acquire the biggest code density.An electric appliances of the modern consumption mainly uses as follows four kinds of batteries:1.Seal completely the sour battery of lead( SLA)2.The battery of NiCd3.The NiMHhydrogen battery( NiMH)4.Lithium battery( Li- Ion)At right choice battery and refresh the calculate way need to understand the background knowledge of these batteries. Seal completely the sour battery( SLA) of lead seals completely the sour battery of lead to mainly used for the more important situation of the cost ratio space and weights, such as the UPS and report to the police the backup battery of the system. The battery of SLA settles the electric voltage to carry on , assist limits to avoid with the electric current at refresh the process of early battery lead the heat.Want ~only the electricity .The pond unit electric voltage does not exceed the provision( the typical model is worth for the 2.2 Vs) of produce the company, the battery of SLA can refresh without limit. The battery of NiCd battery of NiCd use very widespread currently.Its advantage is an opposite cheapness, being easy to the usage;Weakness is from turn on electricity the rate higher.The battery of NiCd of the typical model can refresh 1,000 times.The expired mechanism mainly is a pole to turn over.The first in the battery pack drive over.The unit that all turn on electricity will take place the reversal.For prevent°froming damage the battery wrap, needing to supervise and control the electric voltage without a break.Once unit electric voltage Descend the 1.0 Vs must shut down.The battery of NiCd carries on refresh in settling the electric current by forever . The NiMH hydrogen battery( NiMH) holds to shoot the elephant machine such as the cellular phone, hand in the hand that the importance measure hold equipments, the etc. NiMHhydrogen battery is anusage the most wide.This kind of battery permit.The quantity is bigger than NiCd's.Because lead to refresh and will result in battery of NiMH lose efficacy, carry on measuring by the square in refresh process with.Stop is count for much in fit time.Similar to battery of NiCd, the pole turn over the battery also will damage.Battery of NiMH of from turn on electricity the rate and is probably 20%/ month.Similar to battery of NiCd, the battery of NiMH also settles the electric current to refresh .Other batteries says compare in lithium battery( Li- Ion) and this texts, the lithium battery has the tallest energy/ weight to compare to compare with energy/ physical volume.Lithium batterySettle the electric voltage to carry on refresh with , want to have the electric current restrict to lead the heat in the early battery of refresh the process by avoid at the same time.When refresh the electric current Descend to produce the minimum electric current of the enactment of company will stop refresh.Leading to refresh will result in battery damage, even exploding.The safety of the battery refreshes the fast charge machine( namely battery can at small be filled with the electricity in 3 hours, is usually a hour) demand of the modern.Can to the unit electric voltage, refresh the electric current and the battery temperatures to carry on to measure by the square, avoid at the time of being filled with the electricity because of leading to refresh.Result in of damage.Refresh the method SLA battery and lithium batteries refreshes the method to settle the electric voltage method to want to limit to flow for the ever ; The battery of NiCd and battery of NiMHs refresh the method.Settle the electric current method for the ever , and have severals to stop the judgment method for refresh differently. Biggest refresh the electric current biggest refresh the electric current to have relation with battery capacity( C).Biggest usually refresh the electric current to mean with the number of the battery capacity.For example,The capacity of the battery for 750 mAhs, refresh the electric current as 750 mAs, then refresh the electric current as 1 C(1 times battery capacity).IfThe electric current to flow refresh is a C/40, then refreshing the electric current for the battery capacity in addition to with 40.Lead the hot battery refresh is the process that the electric power delivers the battery.Energy by chemical reaction conservancy come down.But is not all.The electric powers all convert for the sake of the chemistry in the battery ability.Some electric power conversions became the thermal energy, having the function of the heating to the battery.When electricity.After pond be filled with, if continue to refresh, then all electric powers conversion is the thermal energy of the battery.At fast charge this will make the battery.Heat quickly, if the hour of can not compare with stop refresh and then willresult in battery damage.Therefore, while design the battery charger, to the temperature.It is count for much that carry on the supervision combine to stop refresh in time.The discretion method battery stopped refresh of different and applied situation and work environment limitted to the choice of the method that the judgment stop refresh.The sometimes temperature allow of no.Measure easily, but can measure electric voltage, or is other circumstances.This text takes the electric voltage variety rate(- dV/ dt) as the basic judgment to stopThe method for refresh, but with the temperature and absolute electric voltage be worth for assistance and backup.But the hardware support that this text describe speaks as follows.The method of the havings of say. Time of t – this method that is the decision when stop refresh most in ually used for spare project of the hour of fast charge.Sometimes also be .Refresh(14- 16 Hour) basic project of the method.Be applicable to various battery.Stop refresh when the electric voltage of V – be the electric voltage to outrun the upper ually with the forever settle the electric current refreshes the match usage.The biggest electric current is decide by the battery, usually For the 1 C.For prevent°froming refresh the electric current leads to causes battery lead greatly hot, the restrict of the electric current at this time very key.This method Is a lithium battery basic to refresh and stop project. The actual lithium battery charger usually still continues into after attain biggest electric voltage Go the second stage refresh, to attain 100% battery capacity. For battery of NiCd and battery of NiMHs are originally method can Be the spare judgment stops refreshing the project. - The method exploitation that this judgment of the dV/ dt – electric voltage variety rate stops refresh negative electric voltage variety rate.For the battery of some types, be the battery to be filled with the subsequence Refreshing continuously will cause electric voltage descend. At this time this project was very fit.This method usually useds for the ever to settle the electric current to refresh, Be applicable to to the fast charge of the battery of NiCd and battery of NiMH. The electric current of I –is to refresh the electric current small in a certain the number that set in advance stop refresh. Usually used for the ever to settle the electric voltage to refresh the method.Be applicable to the SLA Battery and lithium battery.The T – temperature absolute zero can be the basis that battery of NiCd and battery of NiMHs stop refresh, but even suited for to be the backup project.Any battery for temperature to outrun initial value have to stop refresh.The basis that the dT/ dt –temperature rising velocity fast charge variety rate of the temperature of hour can be to stop refresh.Please consult the norm that the battery produces the company( battery of NiCdOf typical model be worth for the 1 oC/ min) the –be applicable to the battery of NiCd and battery of NiMHs.Need to stop refresh when the DT – outrun the temperature value of theenvironment temperature to be the bad battery temperature and the environment temperature to exceed the certain threshold.This method can be the battery of NiCd and The project that battery of SLA stops refresh.While refreshing in the cold environment this method compares the absolute zero to judge the method better.Because bigMost systems usually only have a temperature to stretch forward, have to will refresh the previous temperature to be the environment temperature. DV/ dt=0 –s zero electric voltages differ this method with- the method of dV/ dt is very and similar, and more accurate under the condition that electric voltage will not go up again. Be applicable to the NiCd Battery and battery of NiMH.This reference design completely carried out the battery charger design of latest technique, can carry on to various popular battery type quicklyRefresh but need not to modify the hardware soon, a hardware terrace carries out a charger product line of integrity.Need only Want to will refresh the calculate way to pass lately the ISP downloads the processor of FLASH saving machine can get the new model number.Show very muchHowever, this kind of method can shorten time that new product appear on market consumedly, and need a kind of hardware of stock only.This design provide The in keeping with SLA, NiCd, NiMH of the integrity and the database function of the battery of Li- Ion.锂电池充电器的设计介绍根据其尺寸,重量和能量储存优点,锂- 离子可再充电电池正在被用于许多的应用领域。
硕士学位论文-磷酸铁形貌特征对磷酸铁锂电化学性能的影响
xx大学全日制硕士专业学位论文磷酸铁形貌特征对磷酸铁锂电化学性能的影响磷酸铁形貌特征对磷酸铁锂电化学性能的影响摘要锂离子电池是第三代可充二次电池,因具有工作电压高、比容量较高、循环寿命长、对环境污染小等特点,近年来成为化学电源领域的研究热点,具有广阔的应用前景。
相对于Ni-Cd、Ni-MH及铅酸电池这类传统的二次电池来说,锂离子电池具有不可比拟的优点。
但目前锂离子电池还存在成本过高、安全性较差、功率密度低等不足,这些都限制了锂离子电池尤其是动力锂离子电池的广泛应用。
其中起着决定性作用的是正极材料,它不仅影响着锂离子电池的成本,而且还决定了电池的总体性能。
因此,对正极材料的研究是其中的关键。
传统的锂离子电池正极材料在价格、安全性、循环性能等方面存在着缺陷,例如钴酸锂安全性能差、价格昂贵且有毒,镍酸锂制备困难、安全性差,锰酸锂循环稳定性差、容量衰减快。
橄榄石型结构的磷酸铁锂(LiFePO4)以原料来源广泛、比容量高、价格低廉、对环境污染小、循环稳定性好、安全性高等优点,受到全球学术界和产业界的极大关注。
传统的高温固相法制备LiFePO4正极材料的铁源一般为二价铁,如草酸亚铁、乙酸亚铁等,但考虑到二价铁源成本较高,且合成过程中容易氧化,而且在工业生产中,用二价铁源合成LiFePO4时,会产生大量的CO2气体,不仅污染空气,还会对生产设备造成腐蚀,因此,近年来的研究逐渐转向成本低廉且不易氧化的三价铁源,如磷酸铁、氧化铁(Fe2O3)等。
近几年,以磷酸铁为原料的碳热还原法制备磷酸铁锂工艺得到了广泛的应用。
碳热还原法是用含三价铁的试剂作为铁源,将作为还原剂和导电剂的过量的碳源加入反应物与之充分混合,在高温下将三价铁还原为二价铁,制备得到产物。
磷酸铁路线的主要优点是工艺过程简单容易控制,可以通过对原材料的有效控制来有效提高产品的批次稳定性。
此法可应用于大规模生产中,是一种实用的技术路线。
在用磷酸铁为原料制备磷酸铁锂的过程中,磷酸铁的结构及形貌对磷酸铁锂产品的性能有很大的影响,不同的磷酸铁原料合成出的磷酸铁锂电化学性能相差非常大。
专业英语-锂离子电池
no free lithium metal.
Disadvantages
1. Requires protection circuit to maintain voltage and current within safe limits.
The cylindrical 18650 cell is the most commonly used Li-ion cell. Mostly used in notebook application, it boasts the lowest cost per watt hour.
Prismatic or brick-shaped Li-ion cells often are costeffective and come in a large variety of sizes.
3.Application
Chemical name
Material Abbreviation Short form Applications
Lithium Cobalt Oxide*
LiCoO2 (60% Co)
Lithium Manganese Oxide*
LiMn2O4
Lithium Iron Phosphate* LiFePO4
electric powertrain
and grid storage
Lithium-Ion Battery
莫乔铃
CONTENTS
1 History 2 Introduction 3 Application
硅氧负极克容量测试方法
硅氧负极克容量测试方法Silicon oxide negative electrode capacity testing method is a critical process in the development and manufacturing of lithium-ion batteries. 硅氧负极容量测试方法是锂离子电池研发和生产过程中的一个关键环节。
It is essential to accurately measure the capacity of the silicon oxide negative electrode to ensure the reliability and performance of the lithium-ion battery. 准确测量硅氧负极的容量是为了确保锂离子电池的可靠性和性能。
There are several methods for testing the capacity of the silicon oxide negative electrode, including galvanostatic cycling, cyclic voltammetry, and differential capacity analysis. 对硅氧负极容量的测试方法包括恒流循环、循环伏安法和微分容量分析法等。
Galvanostatic cycling is a widely used method for capacity testing, which involves charging and discharging the electrode at a constant current to measure the specific capacity. 恒流循环是一种广泛使用的容量测试方法,它通过以恒定电流对电极进行充放电来测量比容量。
Cyclic voltammetry is another popular method that measures the electrochemical behavior of the electrode by scanning the potential in a cyclic manner. 循环伏安法是另一种流行的方法,它通过在循环过程中扫描电位来测量电极的电化学行为。
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LITHIUM ION BATTERY AND METHOD FOR MANUFACTURINGOF SUCH BATTERYInventors: Glyn Jeremy Reynolds (Largo, FL, US) Robert Mamazza, Jr. (New Port Richey, FL, US)Assignees: OERLIKON BALZERS AGIPC8 Class: AH01M464FIUSPC Class: 429322Class name: The electrolyte is solid alkali metal containingcomponent the alkali metal is lithiumPublication date: 2012-10-25Patent application number: 20120270114Abstract:The present invention provides an electrochemical cell comprising an anodic current collector in contact with an anode. A cathodic current collector is in contact with a cathode. A solid electrolyte thin-film separates the anode and the cathode.Claims:1. An electrochemical cell comprising: an anodic current collector in contact with an anode; a cathodic current collector in contact with a cathode; and a solid electrolyte thin-film separating said anode and said cathode.2. The electrochemical cell according to claim 1, wherein said anodic current collector further comprisinga metal selected from the group consisting of iron, nickel, cobalt, chromium, molybdenum, tungsten andtheir alloys.3. The electrochemical cell according to claim 1, wherein said anode further comprising lithium metal or a lithium alloy.4. The electrochemical cell according to claim 3, wherein said lithium alloy is selected from the group consisting of lithium-carbon alloys, lithium-aluminum alloys, lithium-tin alloys, lithium-silicon alloys, lithium-germanium alloys, lithium-magnesium alloys, lithium-indium alloys and lithium-gallium alloys.5. The electrochemical cell according to claim 1, wherein said anode further comprising lithium-containing oxides, lithium-containing sulfides or lithium-containing selenides.6. The electrochemical cell according to claim 1, wherein said solid electrolyte is LiPON.7. The electrochemical cell according to claim 1, wherein said solid electrolyte is selected from the group consisting of LiPONB, Li.sub.3.6Si.sub.0.6P.sub.0.4O4, Li.sub.6.1V.sub.0.61Si.sub.0.39O.sub.5.36, LiBO2, LiBP, Li2SO4--Li2O--B2O3, Li2S--SiS2--P2S5 and LiI--Li2S--P2S5--P2O.sub.5.8. The electrochemical cell according to claim 1, wherein said cathodic current collector is a metal, said metal being resistant to oxidation.9. The electrochemical cell according to claim 8, wherein said metal is selected from the group consisting of nickel, gold, platinum, rhodium, palladium, iridium and aluminum.10. The electrochemical cell according to claim 1, wherein said cathode is lithium cobalt oxide or lithium iron phosphate.11. The electrochemical cell according to claim 1, wherein said solid electrolyte is a molten salt electrolyte.12. The electrochemical cell according to claim 1, wherein said solid electrolyte is a eutectic mixture of lithium nitrate and potassium nitrate, said eutectic mixture having a melting point of about 133.degree. C.13. The electrochemical cell according to claim 12, wherein said eutectic mixture further comprising oxidizing species selected from the group consisting of nitrites, borates, sulfates, phosphates and other nitrates.14. The electrochemical cell according to claim 1, wherein said solid electrolyte having a thickness of less than or equal to 2 microns.15. A method for fabricating a lithium battery comprising: providing a substrate; coating said substrate with a cathodic current collector; depositing a cathode onto said cathodic current collector; applying a heat treatment to the substrate after said deposition of said cathode; and depositing an anodic current collector onto said cathode after said heat treatment step.16. The method according to claim 15, wherein said cathode further comprising: depositing an active electrode material; depositing a solid electrolyte material; and depositing an electronic conductor.17. The method according to claim 16, further comprising mixing nanopowders of said active electrode material with lithium nitrate and potassium nitrate.18. The method according to claim 17, further comprising adding graphite powder to said mixture.19. The method according to claim 16, wherein said solid electrolyte material is LiPON, said LiPON being deposited as a thin-film using radio-frequency physical vapor deposition from a lithium phosphate target in an ambient containing nitrogen gas.20. The method according to claim 16, further comprising: loading said substrate coated with said cathodic current collector into a vacuum load lock; evacuating the vacuum load lock; transferring said substrate to a first deposition chamber; depositing said active electrode material in said first deposition chamber; transferring said substrate with said deposited active electrode material to a second deposition chamber; depositing said solid electrolyte material in said second deposition chamber; transferring said substrate with said deposited solid electrolyte material to a third deposition chamber; depositing said electronic conductor in said third deposition chamber; transferring said substrate with said deposited electronic conductor to said the vacuum load lock; and removing said substrate from the vacuum load lock.21. The method according to claim 16, further comprising densificating said cathode by simultaneously applying heat and pressure to said cathode.22. The method according to claim 21, wherein said densification occurs at a temperature higher than a softening point of said solid electrolyte material.23. The method according to claim 21, further comprising planarizing a surface of said cathode after densification.24. The method according to claim 15, further comprising attaching an anode onto said anodic current collector.25. The method according to claim 24, wherein said anode further comprising placing lithium foil in contact with said anodic current collector.26. The method according to claim 24, wherein said anode further comprising pouring molten lithium onto said anodic current collector.27. The method according to claim 15, wherein said anodic current collector is selected from the group consisting of a metal foil, a metal container, a metal film and a combination thereof.28. The method according to claim 15, further comprising hermetically sealing the lithium battery.29. A method for fabricating a lithium battery comprising: providing a substrate; coating said substrate with a cathodic current collector; placing said substrate with said cathodic current collector into a vacuum processing system; depositing a thin layer of cathode material onto said cathodic current collector in a first processing station of said vacuum processing system; transferring under vacuum said substrate with said cathode material to a second processing station within said vacuum processing system; depositing a thin film of a solid electrolyte material onto said cathode material in said second processing station of said vacuum processing system; transferring under vacuum said substrate with said solid electrolyte material to a third processing station within said vacuum processing system; depositing a thin layer of anode material onto said solid electrolyte material in said third processing station of said vacuum processing system; removing said substrate with said anode material from said vacuum processing system; depositing an anode onto said anode material; and depositing an anodic current collector onto said anode.Description:FIELD[0001] This invention relates to the field of electrical energy storage and is particularly related to fabricating high specific energy, high specific power rechargeable electrochemical cells for mobile electronic device, automotive and renewable energy applications.BACKGROUND[0002] Over the past several decades, the number of portable electronic devices has increased dramatically. Concomitantly, there has been a need to provide lighter, rechargeable power sources with increased electrical storage capacity. Although there have been many technological improvements in the fields of photovoltaic cells, fuel cells and supercapacitors, electrochemical storage in the form of a single or multiple electrochemical cells ("batteries") is still the preferred means to provide power to most portable electronic devices. Electrochemical cells provide an excellent combination of energy capacity, power density and economy. Of the many rechargeable electrochemical cells available in the market today, lithium batteries offer the best performance in terms of specific energy and specific power. At present, the most common rechargeable lithium batteries in use in portable electronic devices are lithium-ion batteries. Lithium-ion batteries combine intercalation electrodes with a non-aqueous liquid electrolyte. Most lithium-ion batteries available today use carbon anodes and cathodes fabricated from metal oxides, phosphates, sulfides or oxysulfides. Another common form of lithium battery in use today is the lithium polymer battery. Instead of a non-aqueous liquid electrolyte, the lithium polymer battery uses a polymeric electrolyte, as its name implies. Some lithium polymer batteries use lithium metal anodes, but the majority use similar electrode materials to lithium-ion batteries.[0003] Lithium-ion and lithium polymer batteries provide premium battery performance at a premium price. However, for many applications, the number of charge-discharge cycles that they can undergo is insufficient. While the cycle life of a capacitor is often measured in millions of cycles, typical cycle lives forlithium-ion and lithium polymer batteries are measured in hundreds of cycles. For applications where large, expensive batteries are required, for example, in all-electric or hybrid-electric vehicles and to back up solar or wind power installations, the cost/lifetime ratio for lithium-ion and lithium polymer batteries is too high. Though some reduction in cost can be achieved by using less expensive materials (such as substituting lithium iron phosphate for the more expensive lithium cobalt oxide cathode material), a way to increase cycle life must be found if lithium batteries are to play a significant role in these large and growing markets.[0004] Another concern often expressed about lithium-ion batteries is their less-than-perfect safety record: there have been a number of highly publicised product recalls associated with "defective" lithium-ion batteries and there are sporadic reports of exploding lithium-ion batteries. These concerns must be addressed and overcome before lithium-ion batteries can be considered for safety-critical applications, e.g., the automotive industry.[0005] Although lithium-ion and lithium polymer batteries have limited charge-discharge cycle lives, another kind of rechargeable lithium battery, the so-called thin-film lithium battery, has a typical cycle life that is measured in thousands of cycles. These thin-film lithium cells comprising thin-film electrodes, electrolytes and current collectors deposited by physical vapor deposition (PVD) onto a substrate have undergone over 20,000 charge/discharge cycles without significant loss of capacity. See W. C. West, J. F. Whitacre and J. R. Lim, "Chemical stability enhancement of lithium conducting solid electrolyte plates using sputtered LiPON thin films", J. Power Sources, 126, 134-138 (2004). Though thin-film lithium batteries date back to 1969 (see C. C. Liang, J. Epstein and G. H. Boyle, "A High-Voltage, Solid-State Battery System", J. Electrochem. Soc., 116, 1452 (1969)), this type of battery received much attention when John Bates and his group at Oak Ridge National Laboratory discovered the `LiPON` thin-film electrolyte material in 1994. In contrast to many of the oxide and sulfide based thin-film electrolytes used previously, UPON was stable to metallic lithium and also to cathode materials that exhibited potentials of up to ˜5V versus lithium anodes. It rapidly became the standard solid electrolyte material for thin-film lithium batteries. However, to date, thin-film lithium batteries have yet to find widespread acceptance as energy storage devices. This is primarily due to their very limited energy storage capacity per unit area and the very high cost to make them.[0006] It is difficult to deposit thin-films greater than about 10 microns thick by PVD. The stresses that build up in the thin-films during deposition can cause the films to delaminate or spall from the substrate. For a 10 micron thick cathode fabricated from LiCoO2, a favorite high-performance thin-film cathode material, the theoretical cell capacity is limited to ˜0.8 mA-h cm-2, based on a film density of 5 g cm-3 and the ability to cycle 60% of the Li in LiCoO2. In practice, this probably represents an upper limit for a single thin-film electrochemical cell based on LiCoO2 as 10 micron thick films deposited by PVD are usually significantly less than 100% dense. In U.S. Pat. No. 6,168,884, Neudecker et al. cite a capacity for a thin-film lithium battery with a 1 micron thick LiCoO2 cathode of 69 μA-h cm-2 which correlates well with this estimate. See B. J. Neudecker, N. J. Dudney and J. B. Bates, "Battery with an In-Situ Activation Plated Lithium Anode", U.S. Pat. No. 6,168,884. Typically, the cost to sputter deposit metal films is ≧0.25 U.S. cents per micron per cm2. To deposit the cathode film alone for a thin-film lithium battery based on LiCoO2 would cost ˜$8,000 per kW-h, which is many orders of magnitude above the targeted figure of $150 per kW-h for automotive and other large energy storage applications. As a result, thin-film lithiumbatteries must be fabricated using much less expensive thin-film deposition techniques or they will be limited to high-end niche applications with very modest capacity requirements.OBJECTS OF THE INVENTION[0007] Based on the limitations of the prior art, there is a need for an improved Lithium Ion Battery.[0008] Nothing in the prior art provides the benefits attendant with the present invention. Therefore, it is an object of the present invention to provide an improvement which overcomes the inadequacies of the prior art.[0009] Another object of the present invention is to provide an electrochemical cell comprising: an anodic current collector in contact with an anode; a cathodic current collector in contact with a cathode; and a solid electrolyte thin-film separating said anode and said cathode.[0010] Yet another object of the present invention is to provide a method for fabricating a lithium battery comprising: providing a substrate; coating said substrate with a cathodic current collector; depositing a cathode onto said cathodic current collector; applying a heat treatment to the substrate after said deposition of said cathode; and depositing an anodic current collector onto said cathode after said heat treatment step.[0011] Still yet another object of the present invention is to provide a method for fabricating a lithium battery comprising: providing a substrate; coating said substrate with a cathodic current collector; placing said substrate with said cathodic current collector into a vacuum processing system; depositing a thin layer of cathode material onto said cathodic current collector in a first processing station of said vacuum processing system; transferring under vacuum said substrate with said cathode material to a second processing station within said vacuum processing system; depositing a thin film of a solid electrolyte material onto said cathode material in said second processing station of said vacuum processing system; transferring under vacuum said substrate with said solid electrolyte material to a third processing station within said vacuum processing system; depositing a thin layer of anode material onto said solid electrolyte material in said third processing station of said vacuum processing system; removing said substrate with said anode material from said vacuum processing system; depositing an anode onto said anode material; and depositing an anodic current collector onto said anode.[0012] The foregoing has outlined some of the pertinent objects of the present invention. These objects should be construed to be merely illustrative of some of the more prominent features and applications of the intended invention. Many other beneficial results can be attained by applying the disclosed invention in a different manner or modifying the invention within the scope of the disclosure. Accordingly, other objects and a fuller understanding of the invention may be had by referring to the summary of the invention and the detailed description of the preferred embodiment in addition to the scope of the invention defined by the claims taken in conjunction with the accompanying drawings.SUMMARY[0013] The current invention describes a method for fabricating a lithium battery that overcomes the inherent cycle life and safety issues associated with today's lithium-ion and lithium polymer batteries without incurring the excessive fabrication costs that limit the applications for thin-film lithium batteries. A suitable substrate is coated with a cathodic current collector using one of several inexpensive thick film techniques. The cathode is then fabricated from active electrode material, solid-electrolyte material and an electronic conductor such as high surface area graphite and deposited onto the substrate using an inexpensive thick film deposition technique. After suitable heat treatment to drive off any unwanted liquids or vapors, the cathode is introduced into a vacuum deposition system where first, a thin layer of cathode material is deposited. Without breaking vacuum, the substrate is transferred into a processing station where a thin film of a solid electrolyte such as lithium phosphorus oxynitride (LiPON) is deposited. Once again, without breaking vacuum, the substrate is transferred into a processing station where a thin layer of anode material such as lithium, a lithium alloy, carbon or silicon is deposited. The substrate is then removed from the vacuum deposition system and the anode is deposited by inexpensive thick film techniques. In some embodiments, the step to deposit the thick film anode is not required. Finally, an anodic current collector is deposited by inexpensive thick film techniques.[0014] A feature of the present invention is to provide an electrochemical cell comprising an anodic current collector in contact with an anode. The anodic current collector can further comprise a metal selected from the group consisting of iron, nickel, cobalt, chromium, molybdenum, tungsten and their alloys. The anode can further comprise lithium metal or a lithium alloy. The lithium alloy can be selected from the group consisting of lithium-carbon alloys, lithium-aluminum alloys, lithium-tin alloys, lithium-silicon alloys, lithium-germanium alloys, lithium-magnesium alloys, lithium-indium alloys and lithium-gallium alloys. The anode can further comprise lithium-containing oxides, lithium-containing sulfides or lithium-containing selenides. A cathodic current collector is in contact with a cathode. The cathodic current collector can be a metal where the metal can be resistant to oxidation. The metal for the cathodic current collector can be selected from the group consisting of nickel, gold, platinum, rhodium, palladium, iridium and aluminum. The cathode can be lithium cobalt oxide or lithium iron phosphate. A solid electrolyte thin-film separates the anode and the cathode. The solid electrolyte can be LiPON. The solid electrolyte can be selected from the group consisting of LiPONB, Li3.6Si0.6P0.4O4, Li6.1V0.61Si0.39O5.36, LiBO2, LiBP, Li2SO4--Li2O--B2O3, Li2S--SiS2--P2S5 and LiI--Li2S--P2S5--P2O5. The solid electrolyte can be a molten salt electrolyte. The solid electrolyte can be a eutectic mixture of lithium nitrate and potassium nitrate. The eutectic mixture can have a melting point of about 133° C. The eutectic mixture can further comprise oxidizing species selected from the group consisting of nitrites, borates, sulfates, phosphates and other nitrates. The solid electrolyte can have a thickness of less than or equal to 2 microns.[0015] Another feature of the present invention is to provide a method for fabricating a lithium battery comprising the following steps. A substrate is provided. The substrate is coated with a cathodic current collector. A cathode is deposited onto the cathodic current collector. The depositing of the cathode can further comprise depositing an active electrode material, depositing a solid electrolyte material, and depositing an electronic conductor. The cathode can be densified by simultaneously applying heat and pressure to the cathode. The densification can occur at a temperature higher than a softening point of the solid electrolyte material. A surface of the cathode can be planarized after densification. The depositing of the active electrode material can further comprise mixing nanopowders of the active electrode materialwith lithium nitrate and potassium nitrate. A graphite powder can be added to the mixture. The solid electrolyte material can be LiPON, that can be deposited as a thin-film using radio-frequency physical vapor deposition from a lithium phosphate target in an ambient containing nitrogen gas. A heat treatment is applied to the substrate after the deposition of the cathode. An anodic current collector is deposited onto the cathode after the heat treatment step. An anode can be attached onto the anodic current collector. The anode can further comprise placing lithium foil in contact with the anodic current collector. The anode can further comprise pouring molten lithium onto the anodic current collector. The anodic current collector can be selected from the group consisting of a metal foil, a metal container, a metal film and a combination thereof. The method can further comprise hermetically sealing the lithium battery.[0016] In a preferred embodiment, the substrate coated with the cathodic current collector can be loaded into a vacuum load lock. The vacuum load lock can be evacuated. Then, the substrate can be transferred to a first deposition chamber where the active electrode material can be deposited. Next, the substrate with the deposited active electrode material can be transferred to a second deposition chamber where the solid electrolyte material can be deposited. Next, the substrate with the deposited solid electrolyte material can be transferred to a third deposition chamber where the electronic conductor can be deposited. Next, the substrate with the deposited electronic conductor can be transferred to the vacuum load lock where the substrate can be removed from the vacuum load lock.[0017] Yet another feature of the present invention is to provide a method for fabricating a lithium battery comprising the following steps. A substrate is provided. The substrate is coated with a cathodic current collector. The substrate with the cathodic current collector is placed into a vacuum processing system. A thin layer of cathode material is deposited onto the cathodic current collector in a first processing station of the vacuum processing system. The substrate with the cathode material is transferred under vacuum to a second processing station within the vacuum processing system. A thin film of a solid electrolyte material is deposited onto the cathode material in the second processing station of the vacuum processing system. The substrate with the solid electrolyte material is transferred under vacuum to a third processing station within the vacuum processing system. A thin layer of anode material is deposited onto the solid electrolyte material in the third processing station of the vacuum processing system. The substrate with the anode material is removed from the vacuum processing system. An anode is deposited onto the anode material. Lastly, an anodic current collector is deposited onto the anode.[0018] The foregoing has outlined rather broadly the more pertinent and important features of the present invention in order that the detailed description of the invention that follows may be better understood so that the present contribution to the art can be more fully appreciated. Additional features of the invention will be described hereinafter which form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and the specific embodiment disclosed may be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims.BRIEF DESCRIPTION OF THE DRAWINGS[0019] FIG. 1 is a schematic view of a solid-state rechargeable lithium battery according to oneembodiment of the present invention;[0020] FIG. 2 is a schematic view of a PVD cluster system according to one embodiment of the present invention;[0021] FIG. 3 is a schematic view of a process flow for a single cell fabrication according to one embodiment of the present invention; and[0022] FIG. 4 is a schematic cross-section view of a lithium battery in a bipolar configuration according to one embodiment of the present invention.[0023] Similar reference characters refer to similar parts throughout the several views of the drawings. DETAILED DESCRIPTION[0024] In thin-film lithium batteries where the cathodes are typically ˜1 micron in thickness, it is possible to de-intercalate and re-intercalate reversibly ˜60% of the lithium ions contained in a thin-film LiCoO2 cathode such that little or no degradation in capacity occurs during charge-discharge cycling--thin-film lithium batteries have been reported to survive over 100,000 charge-discharge cycles under laboratory conditions. For thicker cathodes, it is difficult to access such a high fraction of the lithium content in this manner as the diffusion lengths involved become quite large for solid-state diffusion at ambient temperatures.[0025] In lithium-ion batteries, the cathodes are fabricated to be porous: they soak up the liquid electrolyte which is then in intimate contact with the grains of the active cathode material, thus most long range lithium ion diffusion in the cathode of a lithium-ion battery occurs through the liquid phase. Nevertheless, solid-state diffusion of lithium ions in and out of the grains of cathode material is believed to be rate-limiting for lithium-ion batteries, determining the maximum rate of charge of the batteries and their power density. This mechanism also gives rise to other concerns: the repeated de-intercalation and re-intercalation of lithium into the active cathode material causes volume changes and in some cases, phase changes. Over time, repeated cycling can cause loss of capacity, eventually leading to cell failure. There are few if any reports of lithium-ion batteries surviving 100,000 deep discharge cycles.[0026] Another problem in lithium-ion cells that is believed to be caused by the use of organic liquid electrolytes is the formation of solid electrolyte interface layers between the electrolyte and the electrodes. Because the organic electrolytes used in lithium-ion batteries are rarely thermodynamically stable with respect to the electrode materials, they react and form a mixture of various compounds at the interfaces. Although these layers are often very thin and have a finite conductivity for lithium ions, they are usually not stable over repeated cycling and constitute another potential failure mode for lithium-ion batteries.[0027] The present invention differs considerably from lithium-ion batteries in the materials and methods of construction; this is illustrated in FIG. 1. A single electrochemical cell 10 consists of five functional components: an anodic current collector 20 in contact with an anode 30, a cathodic current collector 60 in。