CN1319910A - Rechargeable solid chromium-fluorine-lithium battery - Google Patents

Rechargeable solid chromium-fluorine-lithium battery Download PDF

Info

Publication number
CN1319910A
CN1319910A CN00120918A CN00120918A CN1319910A CN 1319910 A CN1319910 A CN 1319910A CN 00120918 A CN00120918 A CN 00120918A CN 00120918 A CN00120918 A CN 00120918A CN 1319910 A CN1319910 A CN 1319910A
Authority
CN
China
Prior art keywords
battery
plate
anode
fluorine
coating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN00120918A
Other languages
Chinese (zh)
Inventor
钟馨稼
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHUOYI INVESTMENT
Original Assignee
CHUOYI INVESTMENT
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from CN00101356A external-priority patent/CN1307376A/en
Application filed by CHUOYI INVESTMENT filed Critical CHUOYI INVESTMENT
Priority to CN00120918A priority Critical patent/CN1319910A/en
Publication of CN1319910A publication Critical patent/CN1319910A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Abstract

A rechargeable solid-state battery (10) comprises a plurality of cathode plates (8) and a plurality of anode plates (7) which are staggered with respect to each other, wherein the anode plates (7) comprise an aluminum foil (41) coated with a coating of a mixture (43) consisting of at least lithium manganate, chromium and fluorine. The cathode plate (8) includes a copper foil (47) coated with a coating of a mixture (49) containing petroleum coke. Between the anode plate (7) and the cathode plate (8) is a solid electrolyte (14) made of lithium perchlorate dissolved in ethylene carbonate and diethyl carbonate.

Description

Rechargeable solid chromium-fluorine-lithium cell
But solid chromium-fluoro-lithium (" CrFLi ") battery that the present invention relates generally to a kind of reignition and recharges, and relate to this kind battery that can be used for driving electric motor car such as electrocar.In order to reduce environmental pollution, worldwide, carried out many researchs are used to drive locomotive such as car to develop alternative fossil fuel battery.At present, lead-acid battery, nickel-cadmium cell, Ni-MH battery and sodium-sulphur battery can be used as the storage battery that drives locomotive.It has been generally acknowledged that lead-acid battery and nickel-cadmium cell may have best commerce and technical prospect, and they can be used as the appropriate candidates of the storage battery of electrical power storage.However, because the energy/weight ratio of this two classes battery is lower, recharge time is long and maintenance requirement is high, so the exploitation electrocar directly is affected.
Along with further research and development, recognize that zinc-air battery, lithium ion battery and Proton Exchange Membrane Fuel Cells also are the best electrokinetic cells that is used to drive electrocar to electrokinetic cell.Yet the interior resistance of zinc-air battery is big, and also must improve the supply technology of zinc ion and make it more practical.For lithium ion battery,, there is the danger of catching fire and exploding in the process of charging repeatedly because metallic cobalt and lithium deposition are arranged.As for pem cell, thought to drive the ideal source of electrocar by some.Yet, the difficulty that still has many needs to overcome here.Various practices and technical difficulty have also seriously hindered the electrocar industrial expansion.
The purpose of this invention is to provide a kind of rechargeable solid chromium-fluorine-lithium cell.Of the present inventionly advance a purpose and provide and be used to drive for example this kind battery of electrocar of electric motor car.
The invention provides a kind of method for preparing rechargeable solid state battery, it comprises the steps: that (a) prepares at least one positive plate; (b) make at least one minus plate; (c) between described positive plate and minus plate, place a kind of electrolyte; It is characterized in that described battery carries out initial charge under the temperature more than 48 ℃.
Below will be by way of example, and, embodiments of the present invention are described with reference to appended figure, wherein:
Fig. 1 has expressed two solid chromium-fluoro-lithiums of the present invention (" CrFLi ") battery, and cut open by part in order to illustrate better for one of them described battery;
Indicate the enlarged drawing of the circle part of " A " in Fig. 2 presentation graphs 1;
Fig. 3 represents by a plurality of battery pack that connect to form of battery shown in Fig. 1;
Fig. 4 represents connecting plate that the battery shown in Fig. 1 is electrically connected.
The expanded view of the vent valve of the battery shown in Fig. 5 A presentation graphs 1;
Fig. 5 B is the fragmentary, perspective view of the vent valve shown in Fig. 5 A;
Fig. 6 is the amplification partial side view of the positive plate of battery shown in Figure 1; With
Fig. 7 is the amplification partial side view of the minus plate of battery shown in Fig. 1.
Represented among Fig. 1 that two can be discharged and rechargeable solid chromium-fluoro-lithium (" CrFLi ") battery 10.Each battery 10 comprises a plurality of minus plates 8 and a plurality of positive plate 7 of interlaced arrangement.Though positive plate 7 and minus plate 8 are expressed as planely here, they also can be curved surface shaped, rolling shape or other suitable shape.Battery 10 has a hard shell, and it can be made by polypropylene or nickel plating metal.In addition, shell 13 also can be made by the soft shell that polyurethane, aluminium foil and polyethylene are formed.
An anode 3, a negative electrode 4 and a vent valve 9 are arranged on the top of shell 13.Anode 3 is connected with positive plate 7 in shell 13, and negative electrode 4 is connected with minus plate 8 in shell 13.Between positive plate 7 and the minus plate 8 is solid electrolyte, and its details will be introduced below.With safety cap 1 place on the anode 3, safety cap 2 places on the negative electrode 4.Both make safety cap 1,2 by polybenzothiozole.When for can provide more electric energy that many batteries 10 are connected to form battery pack the time, safety cap 1,2 can be avoided the short circuit that meets accident between negative electrode 4 and anode 3.
On the first type surface of shell 13 fin 12 is arranged, it is in the base of this first type surface and the inboard of side.On another first type surface of shell 13 incline 11 is arranged, its base and two sides along this first type surface distribute.The rib 12 that the size and the configuration of rib 11 and 12 is designed so that a battery 10 can be pressed in the incline 11 that is engaged to another battery 10, thereby with 10 engagements of two batteries be fixed together.
About the lead-in wire that uses in the present invention, under the situation of bladder, anode lug 5 the most handy fine aluminiums are made, and the cathode connection sheet the red copper of handy nickel plating make.Under the situation of hard coat, the most handy stainless aluminum is equipped with anode 3, and the red copper of handy nickel plating prepares negative electrode.
Used lead-in wire preferably adopts specific hot adhesion method in the electrode tabs of the present invention under the situation of bladder.Like this, can realize permanent connection.Hard coat 13 application chloro trifluoro-ethylenes are sealed and are insulated.
As shown in Figure 3, four battery 10A, 10B, 10C and 10D are meshing with each other and fix and form a battery pack.Battery 10A-10D can be accomplished in several ways electrical connection.A kind of mode is can be with battery 10A-10D series connection, and for example the anode 3 with battery 10A is connected with the negative electrode 4 of battery 10B, and the anode 3 of battery 10B is connected with the negative electrode 4 of battery 10C, and the rest may be inferred.The output voltage of supposing four battery 10A, 10B, 10C and 10D is identical, and then the output voltage of battery pack as shown in Figure 3 (being connected in series) will be each 4 times of output voltage among four battery 10A, 10B, 10C and the 10D.Another kind of mode is four battery 10A, 10B, 10C and 10D parallel connection can be electrically connected all anodes 3, and all negative electrodes 4 are electrically connected.And, the output voltage of supposing four battery 10A, 10B, 10C and 10D all is identical, then the output voltage of battery pack as shown in Figure 3 (being connected in parallel) will be identical with the output voltage of battery 10A, but this battery pack can supply the longer time electricity consumption with four times capacitance.
Fig. 4 has shown a link 15 of the electrode (just anode 3 and negative electrode 4) that can be used for being electrically connected battery 10.This link 15 comprises the hard terminal key of two conductions, and each all has a mesopore 19.Key 17 can connect with a branch of lead 21.Two terminal keys 17 and lead 21 all can be formed from steel.As can be seen from Figure 1, anode 3 and negative electrode 4 all have external screw thread, and nut 23 can mesh by this screw thread.The end 17 of link 15 can place on anode 3 or the negative electrode 4 thus, and is fixed with nut 23 respectively.
As for vent valve 9, detailed condition is referring to Fig. 5 A and 5B.As shown, vent valve 9 comprises three assemblies, i.e. loam cake 25, elasticity ethylene-propylene-diene monomer film 27 and base plate 29.Base plate 29 comprises that one has the central recess 31 of steam vent 33, and base plate can be connected to the inside of battery 10.The size and dimension of adjusting sheet rubber 27 makes its groove that can place base plate 29 31.Loam cake 25 comprises many steam vents 35 (Fig. 5 A has listed wherein two) on the sidewall 37 of its protruding barrel portion 39.In the time of assembling, sheet rubber 27 is placed groove 31 and closed steam vent 33, and loam cake 25 is fixed on (for example passing through laser welding) base plate 29.
In the preparation process of battery 10, electrolytical solvent (for example ethylene carbonate, diethyl carbonate) may produce gas, and it must be removed from battery 10 to avoid blast.When the internal pressure among the battery 10 surpasses preset range (for example atmospheric pressure), gas will apply by the bottom of 33 pairs of sheet rubbers 27 of steam vent and upward pressure, so that sheet rubber 27 protuberances, thereby housing 13 gas inside that make battery 10 can enter by the space between sheet rubber 27 round edges and the base plate 29 in the chamber of protruding barrel portion 39 of loam cake 25, and are discharged in the external environment condition by steam vent 35 thus.Though gas only produces in the initial shaping/preparation process of battery 10 usually, but for the sake of security, this vent valve 9 is retained in the battery 10, to guarantee if the internal pressure of battery 10 is when surpassing preset range in the process of discharge or charging, gas in the battery 10 can be discharged, and when the internal pressure of battery 10 is lower than preset range, therefore steam vent 33 (and vent valve 9 also) will be closed in time.
The vent valve of common lithium ion battery and alkaline battery (for example being used in the battery in the portable computer) mainly utilizes the structure of fracturing diaphragm, wherein when the internal pressure of battery surpasses preset range, described film will break so that gas is expelled to the external environment condition from inside battery.Yet because film breaks, battery can not re-use.For the high-energy battery of special designing high-power, vent valve is mainly spring ball closing structure, and wherein closed ball is controlled by a spring, and it is in the position of closing this valve usually.Yet when the inside battery gas pressure surpassed preset range, the deflecting force that described closed ball will overcome spring owing to the gas in the battery moved, and removes to allow that the gas the battery is expelled in the external environment condition from the position of closing.
The structure of the conventional vent valve of discussing in the paragraph is quite complicated and requires Precision Machining in front.In addition, the fracturing diaphragm structure be not suitable for big electric current repeat discharge and recharge in the battery.As for spring ball closing structure, then may be under the situation of long-term pressurized, spring deforms.In addition, the production cost height of this kind valve.
On the other hand, the used ethylene-propylene-diene monomer film 27 of the present invention has following advantage:
A. it is acid and alkali resistance and organic chemicals;
B. linear between pressure and the deformation extent;
C. after using for a long time and repeatedly, elasticity does not change.
D. lower price;
E. make easily, and do not need Precision Machining; With
F. good closure effect.
Thus, but the vent valve with closure film of being made by ethylene propylene diene rubber is best suited for being used in reignition of the present invention and the battery that recharges in.
Fig. 6 has shown the amplification partial side view of positive plate 7 of the present invention.This positive plate 7 comprises the aluminium foil 41 that 0.3mm is thick.On two first type surfaces of aluminium foil 41, be coated with the coating of making by following component 43:
-83-90.5% LiMn2O4 (be sharp brilliant formula, can buy) from Belgian UMEX company;
-1-2wt.% chromium
-1.5-3wt.% lithium fluoride;
-5-8wt.% acetylene carbon black; With
-2-4wt.% graphite.
Then above-mentioned component is mixed and be dissolved in water and/or the ethanol, and be coated to subsequently on the aluminium foil 41.When the aluminium foil 41 after will applying is heated to about 300 ℃, coating 43 will be solidified.The thickness of coating 43 is about 0.25mm.It on coating 43 another separator 45 that makes by ternary acrylic acid.It is thick that each separator 45 is 0.1min.When aluminium foil 41 is heated to once more make described separator 45 dried/cured after, just make single positive plate 7.Find that in practice aluminium foil 41 should be thicker than coating 43.Find also that in practice the existence of chromium can make battery 10 set the speed charge or discharge greater than 1C of capacity with it.The implication of symbol " C " is discussed below.As for fluoride, find that it can make battery 10 discharge above under 50 ℃ the high temperature.
As for the minus plate shown in Fig. 78, it comprises that thickness is about the Copper Foil 47 of 0.35mm.Coating thickness is about the coating 49 of 0.36mm on two first type surfaces of Copper Foil 47.Coating 49 is that the mixture by following material makes:
-be milled to the petroleum coke that particle diameter is 30-40 μ m;
-1-2wt.% graphite;
The acetylene carbon black of-0.5-1wt.%; And
These components are mixed in as the water of solvent and/or ethanol and dissolving, and subsequently it is coated on the Copper Foil 47.Then, by heat drying Copper Foil 47, just make single minus plate 8 thus.Find that in practice each coating 49 must be thicker than Copper Foil 47.After with positive plate 7 and minus plate 8 as above-mentioned interlaced arrangement, then a kind of electrolyte of dissolving is injected in the space between positive plate 7 and the minus plate 8.This electrolyte is by the liquid lithium perchlorate (LiClO of 1/3 weight 4), the liquid ethylene carbonate (HOCOOCH=CH of 1/3 weight 2) and the liquid carbon diethyl phthalate (CH of 1/3 weight 3CH 2OCOOCH 2CH 3).Described electrolyte (together with ethylene carbonate and diethyl carbonate) is about 5-10% of the weight (not comprising shell) of battery 10.To become solid after the electrolyte drying, shown in the label among Fig. 1 and 2 14.
For useful life and the capacity that makes the battery that the present invention makes reaches maximum, find in practice, after this battery 10 has just been made, should be under the temperature of the substantially constant (± 1%) more than 48 ℃, and carry out initial charge with 0.1C to 0.2C speed to the design capacity of single battery 10.The implication that is used in the symbol " C " in the battery design and the field of manufacturing can be understood from following table:
Table 1
Battery capacity Charge/discharge rates Charge/discharge current
100Ah (amp hr) ?1C ?100A
?2C ?200A
?5C ?500A
?0.1C ?10A
?0.2C ?20A
200Ah ?1C ?200A
?2C ?400A
?5C ?1000A
?0.1C ?20A
?0.2C ?40A
Can directly be used in the electrocar as the above-mentioned battery that makes as power supply.After battery is just made, the speed quick charge greater than 3C of the setting capacity that it can battery 10.
Lithium perchlorate is used in the solid conduction base-material not only obviously reduced production cost, and increased the useful life of battery, and increased its high-temperature stability as electrolyte.Finding in practice, because this battery is nontoxic, also is harmless in environment even therefore it is taken apart and abandons.Cross 2000 times but its recharge and discharge, and capacity still keeps at least 75%.
The storage temperature of battery of the present invention can be-40 ℃ to 70 ℃, and its working temperature can be-20 ℃ to 60 ℃.Usually with the speed discharge of the 2C of the design capacity of single battery 10, but if necessary, the pulsed discharge of the 5C of design capacity that also can single battery 10.
Find that in practice the solid state battery that the present invention makes is simple and closely knit, nontoxic, high electric energy, can discharges and recharge with big electric current, can charge in the short period of time, long service life, and can charge repeatedly and discharge.
Since after for example chromium and fluorine mix with other component, LiMn 2O 4Crystal structure be and stable that even at high temperature reach under the situation through charging repeatedly and discharging, described crystal structure does not change yet.Even thus monocell 10 is charged to 5V, also be safe, its cost approximately is LiCoO 2Half of battery.The petroleum coke that grinds is also greatly reduced the production cost of this battery as raw material in the preparation negative electrode.
CrFLi solid state battery of the present invention not only can be used for the electric motor car and the battery-driven vehicles of other class, and also can be assembled into by serial or parallel connection have different-energy battery pack to satisfy other power supply needs, stand-by power supply as communication device, power station and control appliance, the power supply of electronic instrument, and for remote mountain area, outlying district and working site provide illumination, and as family expenses stand-by power supply in the future.
But recharge of the present invention and discharge CrFLi battery can be made into the battery of portable phone, used small size battery such as electronic notebook, computer, video tape recorder, camera, and the battery of family expenses high energy stand-by power supply.

Claims (4)

1, the method for a kind of rechargeable solid state battery of preparation, it comprises the steps:
(a) prepare at least one positive plate;
(b) prepare at least one minus plate;
(c) between described positive plate and minus plate, place a kind of electrolyte;
It is characterized in that: described battery carries out initial charge under the temperature more than 48 ℃.
2, the method for claim 1, it is further characterized in that: described battery carries out initial charge under substantially invariable temperature.
3, method as claimed in claim 2, it is further characterized in that: the temperature fluctuation range that described battery carries out initial charge be no more than its mean temperature ± 0.1%.
4, as the described method of one of claim 1-3, it is further characterized in that: described battery is carried out initial charge with the speed of the 0.1C to 0.2C of its design capacity.
CN00120918A 2000-01-27 2000-08-01 Rechargeable solid chromium-fluorine-lithium battery Pending CN1319910A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN00120918A CN1319910A (en) 2000-01-27 2000-08-01 Rechargeable solid chromium-fluorine-lithium battery

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
CN00101356A CN1307376A (en) 2000-01-27 2000-01-27 Rechargeable solid Cr-F-Li accumulator
CN00101356.4 2000-01-27
HK00104143A HK1033534A2 (en) 2000-01-27 2000-07-05 A rechargeable solid state chromium-fluorine-lithium electric battery
HK00104143.8 2000-07-05
CN00120918A CN1319910A (en) 2000-01-27 2000-08-01 Rechargeable solid chromium-fluorine-lithium battery

Publications (1)

Publication Number Publication Date
CN1319910A true CN1319910A (en) 2001-10-31

Family

ID=27178726

Family Applications (1)

Application Number Title Priority Date Filing Date
CN00120918A Pending CN1319910A (en) 2000-01-27 2000-08-01 Rechargeable solid chromium-fluorine-lithium battery

Country Status (1)

Country Link
CN (1) CN1319910A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101238603B (en) * 2005-04-21 2010-12-15 波塔宁协会有限公司 Method for producing a solid-state power supply

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101238603B (en) * 2005-04-21 2010-12-15 波塔宁协会有限公司 Method for producing a solid-state power supply

Similar Documents

Publication Publication Date Title
KR102089264B1 (en) Device for Charge and Discharge of Secondary Battery
US6686096B1 (en) Rechargeable solid state chromium-fluorine-lithium electric battery
KR101676085B1 (en) Silicon based anode active material and lithium secondary battery comprising the same
CA2122092A1 (en) Secondary battery having non-aqueous electrolyte
CN105765766A (en) Lithium-ion secondary battery and manufacturing method thereof
US20120075771A1 (en) Coin type lithium ion capacitor
KR20110100301A (en) Non-aqueous electrolyte secondary battery, and method for charging same
KR20150133167A (en) Anode active material for lithium secondary battery and Lithium secondary battery comprising the same
KR20150066415A (en) Method of manufacturing cap-assay of litium ion battery with high capacity and power and cap-assay thereof
CN100342579C (en) Rechargeable solid chromium-fluorine-lithium battery
CN1319910A (en) Rechargeable solid chromium-fluorine-lithium battery
CN1319911A (en) Rechargeable solid chromium-fluorine-lithium battery
KR101744245B1 (en) High potential Lithium secondary battery
JP4257719B2 (en) Non-aqueous secondary battery and its system
JP2003282143A (en) Nonaqueous electrolyte secondary battery
Shukla et al. Electrochemical power sources: 1. Rechargeable batteries
KR20150037408A (en) A composition for preparing anode comprising low temperature additives and a electrochemical device comprising the same
US11769899B2 (en) Press jig and method of manufacturing secondary battery using same
KR20010077860A (en) A Rechargeable Solid State Chromium-Fluorine-Lithium Electric Battery
CN219226369U (en) Electrode assembly, battery cell, battery and electricity utilization device
KR20010077859A (en) A Rechargeable Solid State Chromium-Fluorine-Lithium Electric Battery
KR20010081934A (en) A Rechargeable Solid State Chromium-Fluorine-Lithium Electric Battery
CN2733601Y (en) Secondary battery and secondary battery pack
CN2454906Y (en) Column-like alkaline accumulator cell for electric vehicle
KR20150125377A (en) Cylinderical secondary battery

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication
REG Reference to a national code

Ref country code: HK

Ref legal event code: WD

Ref document number: 1043435

Country of ref document: HK