CA3052988C - System and method for a stable high temperature secondary battery - Google Patents
System and method for a stable high temperature secondary battery Download PDFInfo
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- CA3052988C CA3052988C CA3052988A CA3052988A CA3052988C CA 3052988 C CA3052988 C CA 3052988C CA 3052988 A CA3052988 A CA 3052988A CA 3052988 A CA3052988 A CA 3052988A CA 3052988 C CA3052988 C CA 3052988C
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Abstract
Description
BATTERY
[0001]
TECHNICAL FIELD
BACKGROUND
Generally, commercially available rechargeable batteries do not safely and reliably function above 70 C. Furthermore, they do not provide the high energy density used in specific markets such as oil and gas drilling equipment.
Date Recue/Date Received 2021-06-24 BRIEF DESCRIPTION OF THE FIGURES
DESCRIPTION OF THE EMBODIMENTS
Overview
This could allow the battery to be operable and safe in specific markets such as oil and gas drilling equipment, where batteries have to tolerate extreme heat.
The battery- can provide a unique combination of high temperature stability and rechargeability features while providing comparable or better energy properties than other technologies. These qualities have the potential to greatly benefit military applications, drilling applications, and/or other suitable applications.
Electrolyte
The electrolyte loo is preferably a blend of non-aqueous liquid from the ionic liquid family with high thermal stability. More specifically, the electrolyte loo for a lithium battery can be comprised of electrolyte salts, a complementary non-aqueous ionic liquid solvent, and optionally additional salts and additives to stabilize the system. The complementary nature of the solvent can allow for dissolution of the salt at preferred parameters of the system. The electrolyte loo may facilitate the use of both metallic anodes and high-voltage cathodes, thereby enabling a battery with high specific energy and/or energy density in a stable and/or rechargeable format. A preferred blend of electrolyte may be described as nonflammable, forming a thermally-stable electrolyte foo for a high-energy rechargeable battery. In some preferred variations, solvents and/or additives may improve coulombic efficiency, reduce gassing, and/or reduce side reactions with metallic anodes and/or high voltage cathodes. In preferred examples, improved coulombic efficiency, reduced gassing, and/or reduced side reactions may occur at high temperatures. In some preferred variations, the additives may promote uniform lithium deposition, thereby improving battery reliability and/or cyclability.
Cyclability may be associated with one of two potential metrics: power ability (i.e., how fast a battery can be cycled) and battery lifetime (i.e., number of cycles before reaching end of life (EOL)). Cyclability may be temperature dependent. End of life may be characterized by when retention is less than 8o% of the initial capacity. A
cycle can be characterized as a substantially complete cycle between a full state of charge and a particular depth of discharge. Cyclability may be temperature dependent. In one example, the battery can be discharged in < 5h and undergo 80 cycles at flo C;
the battery can be discharged in < foh and undergo 12 cycles at 150 C.
preferred variation of electrolyte 100 is comprised of electrolyte salts or more specifically lithium salts 120. These salts dissolve into ions that conduct charges within the liquid medium, thus making the wettability of the separator and cathode components an important factor in the battery performance. In a preferred example, the lithium salt 120 concentration is high. The electrolyte salts can be 10-30 percent of the total weight of the electrolyte 100. In one implementation, a high concentration of lithium salt 120 is greater than 15% by weight. In one implementation this may include a lithium salt 120 concentration of 18-22% by weight. At typical operating temperatures (i.e. room temperature) high lithium salt concentration may induce high viscosity in the electrolyte loo, which is commonly considered detrimental to battery performance.
However, as discovered by the applicant, high lithium salt concentration and its application in a commercial battery implementation for use cases as described herein (e.g., high temperature) may have particular benefits. Some potential benefits related to high salt concentration can include improved uniformity of lithium plating, increased ionic conductivity, higher oxidative stability, and/or other suitable benefits. For a system with preferred components, high lithium salt concentration may allow the system to function better at higher temperatures such as temperatures that are considered nonfunctional for typical rechargeable batteries (i.e. > 70 C).
[00311 As shown in FIGURE 5, the concentration of electrolytic salt can provide significant improvements compared to more conventional concentration levels.
In this exemplary chart, the battery with 22% by weight of salt retains approximately 8o% of capacity after 8o cycles while a battery with 15% by weight of salt may lose 20% of capacity after 25 cycles.
[0032]
Examples of lithium salts include: lithium bis(fluorosulfonyl)imide, lithium hexafluorophosphate, lithium bis(oxalato)borate, or lithium tetrafluoroborate.
One preferred implementation of lithium salt is lithium bis(trifluoromethanesulfonyl)imide (LiTFSI). In one implementation, the LiTFSI
accounts for 27% of the electrolyte weight.
[0033] The liquid solvent 110 is preferably a nonaqueous aprotic solvent, which may contain an alkyl-substituted pyrrolidinium or piperidinium cation and an imide anion. The anion can include a sulfonyl group. One preferred example of the ionic liquid solvent is a bis(trifluoromethanesulfonyl)imide (TFSI)-based ionic liquid solvent. A
more preferred implementation may be i-Butyl-i-methylpyrrrolidinium bis(trifluoromethanesulfonyl)imide. Alternative ionic liquid materials can include molecularly related compounds by replacing molidinium with piperidinium, replacing butyl with alkyls of different length (e.g. methyl, ethyl, and the like), replacing methyl with alkyls of different length (e.g. butyl, ethyl, and the like), replacing bis(trifluoromethanesulfonyl)imide (TFSI) with bis(fluorosulfonyflimide (FSI), and/or any of these or other suitable combinations. The ionic liquid solvent can serve as the medium for ionic flow, increase the thermal stability of the system, and promote even electroplating of ions onto the anode.
[0034]
Stabilizing salts and/or other additives 130 can function to tune the physical and chemical properties of the electrolytes (e.g. viscosity, electrochemical stability, thermal stability, transference number, diffusivity, and conductivity). In preferred variations, salts and additives stabilize the electrolyte 100 at high temperatures, which may increase battery life at high temperature cycling, increase the wettability of the various porous components (i.e. separator and cathode), and/or convey other desired properties on the electrolyte 100. In some examples, stabilizing salts 130 and additives may include sodium bis(trifluoromethanesulfonyl)imide, potassium bis(trifluoromethanesulfonyeimide, cesium bis(trifluoromethanesulfonyl)imide, magnesium bis(trifluoromethanesulfonyl)imide, and/or zinc bis(trifluoromethanesulfonyl)imide. Other suitable salts and/or additives may be used.
Separator [0035] The separator 400 of a preferred embodiment functions as a physical barrier between the anode and cathode subcomponents and facilitates desired electrochemical interactions by promoting ionic flow between the negative and positive electrodes. The separator 400 sits between the cathode and anode insuring no electrical contact between the two. The separator 400 can be an electronically insulating membrane disposed between the negative and positive electrodes, but may alternatively be any suitable type of separating structure. Separators 400 are preferably porous structures that, although ion-permeable, are not electrically conductive. In one implementation, the contact angle of the electrolyte 100 on the separator surface is less or equal to 6o , as measured 6o seconds after deposition. If the contact angle of the liquid drop on the material is lesser than 60 degrees, the interactions between the liquid and material are favorable and the material can be considered wet. In one exemplary implementation, the separator thickness is less than or equal to 35 microns.
Depending on their composition, separators 400 may have additional properties in addition to the ones previously mentioned (e.g. a ceramic coating may increase separator mechanical strength and increase separator stability at high temperatures). Possible separator examples are: surfactant-coated separators, ceramic-coated polyethylene, non-coated polypropylene, non-coated polyethylene, or polyimide (either by itself or in combination with one of the other prior options). In one preferred implementation, the separator 400 may be a ceramic-coated polypropylene separator. The ceramic coat can function to give the separator 400 additional thermal and mechanical stability.
Polypropylene can have favorable interactions with the electrolyte that enhance wettability, which promotes ion transfer and mitigates dendritic growth on the anode. In one exemplary implementation, the separator may have: pore size < 200 nm; porosity > 35%;
tensile strength > 90 kfg/cm2; Gurley number > 4 sec/loo mL; Density > 6 g/m2; and/or a melting temperature > no C. In such an exemplary implementation shrinkage at for 2h could be less than 3% and shrinkage at 105 C for ih could be less than 5%. The separator is compatible with the preferred electrolyte loo.
[0036] A separator 400 may be a single component separator as described previously. The separator 400 may alternatively be a compound separator made of multiple single component separators, layers, and/or other materials. A
compound separator may be a dual layer separator that has an anode-adjacent surface and/or a cathode adjacent surface as shown in FIGURE 6. In a preferred variation, the anode-adjacent separator is composed of the ceramic coated polypropylene layer (as described above) and the cathode-adjacent separator is composed of a polyimide layer. In this implementation the polyimide may function to provide additional mechanical robustness to the separator 400 to avoid degradation, deformations, or other forms of failures at high temperatures. In some implementations, such a separator 400 may be suitable up to at least 200 C.
Anode [0037] The anode 200, or negatively charged electrode, of a preferred embodiment is a metallic anode and more specifically a lithium metal anode. A
lithium metal anode includes a piece of lithium metal, which may be formed as a strip, plate, or piece of lithium metal foil. The lithium metal anode in some implementations may have a thickness of about 5-150 microns. In some implementations, the lithium metal is mounted on a copper foil current collector. Regardless of the exact composition of the lithium metal anode, which may vary, the level of lithium purity is preferably substantially high. Lithium metal has a high specific energy, typically an order of magnitude greater than the graphite anode of rechargeable batteries in public use.
Lithium-magnesium alloys are other preferred examples of metallic anodes. In some examples, the lithium metal anode may be stabilized by the electrolyte loo.
Stabilization of the lithium surface of the lithium metal anode may be achieved by formation of a stable and robust solid electrolyte interphase (SET). In some implementations, stable SEI formation may be achieved by reaction of the electrolyte loo with the lithium surface of the lithium metal anode. The preferred lithium rich electrolyte can partially decompose on contact with the negative electrode active material to form fluoride and sulfur-rich lithium species that enhances the lifetime of the electrode by forming an unreactive layer on the electrode that inhibits further electrolyte decomposition and formation of dendrites. In such embodiments, the SET structure, stability, and/or properties may depend on the electrolyte chemistry and physical properties.
Cathode [0038] The cathode 300, or positively charged electrode, of a preferable embodiment is typically in the form a strip comprised of an active material that may reversibly intercalate ions, at least one binder 310, and at least one conductive additive 320. The positive electrode has a thickness typically in the range of 50-120 microns and a density of at least approximately 2.4 g/cm3. By weight, the active material constitutes at least 93% of the cathode 300, the binder constitutes 0.5-5% of the cathode 300, and the conductive additive(s) constitute about 0.1-4% of the cathode 300.
[0039] The active material typically consists of a metal oxide, metal phosphate, metal fluoride, or a combination thereof. The active material typically undergoes minimal structural changes or release of gaseous byproducts at temperatures at or below 160 C. The active material may be a material composed of Li, Ni, Mn, Co and oxygen. More preferably, the material may include compounds composed of LiNixMnyCoz02, where x ranges from 0.3-0.9, y ranges from 0.05-0.3, and z ranges from 0.05-0.3. The active material secondary particle size ranges from 4 microns to microns. In one preferred implementation the ratio is 5:3:2 (i.e., LiNi0.5Mno.3Coo.202).
In alternative embodiments, the metal oxide cathode 300 may be comprised of lithium iron phosphate or lithium nickel manganese cobalt (NMC) oxide with other common ratios (e.g. 1:1:1, 6:2:2, or 8:1:1). In preferred variations, the cathode 300 composition may be specifically designed to remain stable at temperatures up to and above 160 C.
[0040] Conductive additives 320 of the cathode 300 can include electronically conductive carbon-based materials. In one variation, the conductive additive 320 can be conductive graphite and/or carbon black. Other alternatives may include other typical lithium ion carbon additives.
[0041] In addition to the active material, the cathode mixture includes a binder 310. The binder 310 functions to maintain the active material bound to the carbon additives and current collector. A preferred embodiment for the binder 310 is preferably a polyimide. Polyimide is a preferred binder 310 due to its compatibility with the preferred electrolyte foo and polyimide's specific mechanical and chemical properties.
Polyimide is novel in the field of rechargeable batteries: it is easier to process as thin cathode coats than polytetrafluoroethylene (PTFE), is mechano-stable at high temperatures, has a glass transition point of greater than 300 C, has shrinkage of less than 0.5% after 6o minutes at 150 C, does not lose function at high temperatures, and exhibits minimal swelling and softening in contact with the electrolyte foo.
Alternative binders, such as Polyamide-imide, Polyvinylidene Fluoride, Carboxymethyl cellulose, Ethylene-(propylene-diene monomer) copolymer, Polyacrylates, Styrene-butadiene rubber, Polytetrafluoroethylene, and any others binders also compatible with the desired electrolyte 100 may be chosen.
[0042] As shown in FIGURE 7, a battery such as the one described herein using a polyimide binder can achieve significant improvements in capacity retention compared to other more conventional binders like polyvinylidene fluoride (PVDF). While the polyimide binder can retain around 90% capacity after 9 cycles, more conventional approaches may lose around 30% of capacity after only 8 cycles.
Casing [0043] As discussed, the battery casing 500 can preferably function to provide a protective packaging to make the battery suitable for use. An outer casing can be formed into a variety of battery structure form factors such as a button cell battery structure, a spiral-wound battery structure, or a pouch cell battery. In particular for high temperature use, the battery preferably includes a high temperature battery casing.
[0044] A high temperature battery casing functions to package the internal battery system for high temperature usage which may include temperatures greater than 50 C, though the battery may additionally remain operational at room temperatures or below.
As shown in FIGURE 8, a high temperature battery casing can include a metal outer casing enclosing the battery internals. The metal casing in some varieties is a steel-based material and serves as the negative contact, but other suitable materials may alternatively be used. A high temperature battery casing can additionally include an electrical contact region that includes a positive contact pin circumscribed by a glass-to-metal seal as shown in FIGURE 8. The positive contact pin preferably extends out from the surface of the battery casing. A negative contact is preferably the material elsewhere in the electrical contact region, such as the metal surface surrounding the glass-to-metal seal and the metal casing itself. The glass-to-metal seal is preferably a ring that surrounds the positive contact pin. The glass-to-metal seal is preferably an electrical insulator.
The glass-to-metal seal may additionally have thermal expansion properties matched to the material used in the battery casing, at least for the desired operating temperature ranges. Matched thermal expansion can function to prevent leaks and other mechanical failures in the battery.
[0045] In certain examples, a button cell battery may be manufactured to deliver mWh as shown in FIGURE 3. In a preferred implementation, the anode 200 may be a lithium metal anode as described above. In a preferred implementation, the cathode may be a cathode as described above. In a preferred implementation, the separator 200 may be a separator system as described above. As illustrated, the button cell battery may include an aluminum spring 310, a stainless-steel spacer 320, and a stainless-steel spring 330.
[0046] In certain embodiments, a spiral-wound DD-format cell battery, as shown in FIGURE 1, may produce a nominal voltage of approximately 3.7 volts, provide approximately 8o Wh of energy, be non-flammable, operate up to 160 C or more, and be rechargeable. Alternative spiral-wound formats may alternatively be used.
[0047] In some embodiments, a pouch cell battery, as shown in FIGURE 4, may be formed by wetting and compressing electrodes to achieve good contact and low resistance.
In various embodiments, a metal foil and tabs of the pouch cell battery may be welded together. In certain embodiments, the pouch cell battery may include stacked electrodes configured to deliver from 40 mWh in a 2 X 3 cm format to 8 Wh in a 10 x 12 cm format.
In one embodiment, two to twenty electrodes of the pouch cell battery may Date Recue/Date Received 2021-06-24 be assembled and stacked following a Z fashion folding in pouch laminate or pre-formed pouch laminate. In certain embodiments, the electrolyte foo may be injected into the pouch cell battery before vacuum sealing the pouch.
[0048] As shown in the cross-sectional diagram of an exemplary battery in FIGURE 2, the battery can include a metallic anode 200, a polymer separator 400, an ionic liquid electrolyte foo, and a metal oxide cathode 300. The components of the battery may be the preferred components described herein.
[0049] The system may additionally include a charger system 600, which functions to recharge the battery as shown in FIGURE 9. The charger system 6o0 is preferably electrically coupled to the battery and then the battery is operated in a charging mode to re-energize the battery for a subsequent use in powering an electrical system. As discovered by the applicants, some variations of the battery experience enhanced rechargeability (in amount of recharge and/or number of recharge cycles) when charged at an elevated charging temperature. In some variations, the charger system 600 is an elevated temperature charging system that may include a heater element, which functions to charge the battery at an elevated temperature. The heater element can preferably be a regulated heating element controlled and configured to set and/or maintain a battery at particular temperatures while in a charging mode.
In one implementation the elevated temperature charging system 600 is configured to set the temperature of the battery between 70-120 C. For example, the elevated temperature charging system 600 may charge the battery at a temperature of at least 80 C.
The battery system may be configured to alter the charging temperature set by the heater element over a charging cycle. For example, the heater element may be configured to set a first temperature at one period in a charging cycle and a second temperature at a second period in the charging cycle. The charger system 600 may additionally be configured to apply a charging cycle tuned to the particular component materials and chemicals used in the battery.
[0050] The battery is preferably operable in at least a charging operating mode and a discharging mode (i.e., an active use mode). The battery may additionally have a standby mode where the battery is not in active use. As discussed, the battery is preferably operable at elevated temperatures during the discharging and standby operating modes. In other words, a battery not in active use can be exposed to high temperature conditions, and the same battery may be used in high temperature conditions. During a charging operating mode, the elevated temperature system may be configured to heat or maintain the temperature of the battery at least at 8o C
[00511 The system may additionally include one or more electrical devices, wherein the electrical devices function to provide some electrical based functionality at least in part powered by the rechargeable battery or powering the rechargeable battery described herein. Exemplary electrical devices can include harsh environment sensors or devices (e.g., well and mining devices), medical devices (e.g., implantable medical devices that are powered by the battery and an inductive charger that charges the battery), wearable computing devices, and/or other suitable electrical devices. In one variation, the charger system 600 can be integrated into the electrical device such that the battery can be recharged through the electrical device.
[0052] As a person skilled in the art will recognize from the previous detailed description and from the figures and claims, modifications and changes can be made to the embodiments of the invention without departing from the scope of this invention as defined in the following claims.
Claims (19)
an electrolyte, comprising an ionic liquid solvent and an electrolyte salt;
a lithium-metal anode, having a thickness less than 150 micrometers;
a cathode, comprising an intercalation active material and a binder; and a separator, having a porosity greater than 35% and separating the cathode and anode.
and 160 C.
and 160 C.
and wherein in the discharging operating mode, the lithium-metal secondary battery supplies at least 450 Wh/L over one full discharge when operated at temperatures between 70 C and 160 C.
wherein the elevated-temperature charging system comprises a charging operating mode; and wherein, in the charging operating mode, the elevated-temperature charging system is configured to set the temperature of the lithium-metal secondary battery to at least 80 C.
an electrolyte, comprising a bis(trifluoromethanesulfonyl)imide-based ionic liquid solvent, and a lithium salt, comprising lithium his(fluorosulfanyl)imide;
a lithium metal anode, hav a thickness less than 150 micrometers;
a cathode, comprising a metal oxide-based active material, a binder, and a carbon-based conductive additive;
a ceramic-coated polypropylene separator, having a thickness less than 35 micrometers and a porosity greater than 35% and disposed between the cathode and the anode; and a high-temperature battery casing, comprising a glass-to-metal seal.
Applications Claiming Priority (3)
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| US201762463194P | 2017-02-24 | 2017-02-24 | |
| US62/463,194 | 2017-02-24 | ||
| PCT/US2018/019594 WO2018157007A1 (en) | 2017-02-24 | 2018-02-24 | System and method for a stable high temperature secondary battery |
Publications (2)
| Publication Number | Publication Date |
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| CA3052988A1 CA3052988A1 (en) | 2018-08-30 |
| CA3052988C true CA3052988C (en) | 2022-07-26 |
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| CA3052988A Active CA3052988C (en) | 2017-02-24 | 2018-02-24 | System and method for a stable high temperature secondary battery |
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| EP (1) | EP3586386A4 (en) |
| CN (1) | CN110582868B (en) |
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| MX (1) | MX2019009953A (en) |
| RU (1) | RU2740794C1 (en) |
| SA (1) | SA519402472B1 (en) |
| WO (1) | WO2018157007A1 (en) |
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| US10930972B2 (en) | 2019-01-25 | 2021-02-23 | Toyota Motor Engineering & Manufacturing North America, Inc. | Metal-phosphorous sulfide additives for solid state batteries |
| US12249683B2 (en) | 2019-04-01 | 2025-03-11 | Customcells Holding Gmbh | Rechargeable lithium ion battery for wide temperature range and high temperatures |
| CN110247123A (en) * | 2019-06-17 | 2019-09-17 | 合肥国轩高科动力能源有限公司 | Battery cell structure, manufacturing method and battery |
| WO2024049763A1 (en) * | 2022-08-29 | 2024-03-07 | Wayne State University | High temperature lithium-ion battery and method of making same |
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2018
- 2018-02-24 MX MX2019009953A patent/MX2019009953A/en unknown
- 2018-02-24 US US15/904,315 patent/US20180248221A1/en not_active Abandoned
- 2018-02-24 CA CA3052988A patent/CA3052988C/en active Active
- 2018-02-24 RU RU2019128249A patent/RU2740794C1/en active
- 2018-02-24 EP EP18756708.6A patent/EP3586386A4/en not_active Withdrawn
- 2018-02-24 CN CN201880013468.0A patent/CN110582868B/en not_active Expired - Fee Related
- 2018-02-24 WO PCT/US2018/019594 patent/WO2018157007A1/en not_active Ceased
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2019
- 2019-08-18 SA SA519402472A patent/SA519402472B1/en unknown
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2020
- 2020-09-15 US US17/021,844 patent/US20210143467A1/en not_active Abandoned
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| MX2019009953A (en) | 2019-12-19 |
| WO2018157007A1 (en) | 2018-08-30 |
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| EP3586386A1 (en) | 2020-01-01 |
| CN110582868B (en) | 2022-05-10 |
| CN110582868A (en) | 2019-12-17 |
| CA3052988A1 (en) | 2018-08-30 |
| EP3586386A4 (en) | 2021-01-06 |
| SA519402472B1 (en) | 2022-10-30 |
| RU2740794C1 (en) | 2021-01-21 |
| US20210143467A1 (en) | 2021-05-13 |
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