This invention relates generally to lithium metal, and, more specifically, to lithium metal foils with very low defect density, which are especially useful as anodes in secondary battery cells.
Current practice specifies a purity of about 99.9% for “battery-grade” lithium metal, which is verified through analysis of no more than about 15 elemental impurities. Such battery-grade lithium metal has been used successfully in primary batteries, which discharge once and do not undergo repeated charging and discharging.
In a secondary lithium battery, lithium metal ions leave the negative electrode (anode) and move toward the positive electrode (cathode) during discharge as they do in primary batteries. But, unlike primary batteries, in secondary batteries lithium metal ions move back to the negative electrode during charging. Secondary batteries are designed to undergo very many cycles of charging and discharging.
Currently-available battery-grade lithium metal does not include any specification as to the presence of compounds, second phases, and other morphological defects. But, it has been found that such defects in battery-grade lithium metal adversely affect uniformity in charge transfer at the anode in secondary batteries. Thus, specifications of battery grade-purity have been found to be inadequate as the performance of lithium metal anodes in secondary batteries is affected by defects that are not accounted for in analyses of solute atoms alone.
What is needed is a method to reduce the density of defects in lithium metal and secondary-battery-grade lithium metal specifications that include quantification of such defects.
In one embodiment of the invention, a material is described. The material is a lithium metal foil that includes lithium metal and crystalline defects that contain lithium and at least one other element selected from the group consisting of hydrogen, oxygen, and nitrogen. The lithium metal foil contains no more than one crystalline defect with a largest dimension at least as large as the lithium foil thickness per 1.35×10-3 cubic meters (1.35×106 cubic millimeters) of lithium metal foil.
In one embodiment of the invention, a material is described. The material is a lithium metal foil that includes lithium metal and crystalline defects that contain lithium and at least one other element selected from the group consisting of hydrogen, oxygen, and nitrogen. The total surface area of the lithium metal foil includes both a first surface area from a first surface and a second surface area from a second surface opposite the first surface. The lithium metal foil contains no more than one crystalline defect per 0.0074 meter3 of total surface area.
In another embodiment of the invention, a method of reducing defect density in a lithium metal foil is disclosed. The method involves providing molten lithium metal; adding a gettering material to the molten lithium metal; holding the molten lithium metal at a temperature of 550° C. for at least 180 minutes; separating the molten lithium from the getter material by filtration; casting the molten lithium to form an ingot; and extruding the ingot to form a foil. The foil may also undergo rolling to reduce its thickness.
The lithium metal foils described herein can be used as an anode in a lithium battery cell.
In another embodiment of the invention, a lithium battery cell is described. The cell has an anode containing any of the lithium metal foils described herein; a cathode comprising cathode active material particles, an electronically-conductive additive, and a catholyte; a current collector adjacent to an outside surface of the cathode; and a separator region between the anode and the cathode, the separator region comprising a separator electrolyte configured to facilitate movement of lithium ions back and forth between the anode and the cathode.
In some arrangements, at least one of the catholyte and the separator electrolyte contains a solid polymer electrolyte and a lithium salt. In some arrangements, at least one of the catholyte and the separator electrolyte contains a ceramic electrolyte. In some arrangements, the catholyte and the separator electrolyte are the same. The cathode electrode active material may be selected from the group consisting of lithium iron phosphate, lithium metal phosphate, divanadium pentoxide, lithium nickel cobalt aluminum oxide, lithium nickel cobalt manganese oxide, magnesium-rich lithium nickel cobalt manganese oxide, lithium manganese spinel, lithium nickel manganese spinel, and combinations thereof.
The foregoing aspects and others will be readily appreciated by the skilled artisan from the following description of illustrative embodiments when read in conjunction with the accompanying drawings.
FIG. I shows back-scatter electron images of two different exposed faceted defects in lithium metal foils.
The embodiments of the invention are illustrated in the context of lithium metal foils in secondary battery cells. The skilled artisan will readily appreciate, however, that the materials and methods disclosed herein will have application in a number of other contexts where lithium metal with very low defect density is desirable, particularly in electrochemical applications.
These and other objects and advantages of the present invention will become more fully apparent from the following description taken in conjunction with the accompanying drawings.
All ranges disclosed herein are meant to include all ranges subsumed therein unless specifically stated otherwise. As used herein, “any range subsumed therein” means any range that is within the stated range.
All publications referred to herein are incorporated by reference in their entirety for all purposes as if fully set forth herein.
Definitions—the term “lithium metal foil” is used herein to mean a very thin sheet of lithium metal, usually made by extrusion or by rolling.
Lithium foils were obtained from six industry suppliers in several countries. Various analytical methods were used to study these foils including focused ion beam (FIB) sample preparation, scanning electron microscope (SEM) imaging, x-ray tomography, μ-x-ray diffraction, fluorescence, Raman spectroscopy, and backscattered electron imaging. The results of these studies are presented below.
FIG. I shows two back-scatter electron images of faceted defects in lithium metal foils. FIB has been used to expose the defects, and much of the surrounding lithium metal material has been removed. The defects have six non-orthogonal facets.
X-ray tomography was performed using the Advanced Light Source at Lawrence Berkeley National Laboratory in Berkeley, Calif. The x-ray energy was 23 keV. Other conditions include use of a 5× objective, 180° rotation, minimum 19% transmission, and 100 mm distance between the sample and the scintillator. Battery-grade lithium foils from a variety of industrial suppliers were analyzed. Some foils were extruded and some foils were rolled. The foil thicknesses ranged from 30 μm to I00 μm, and the widths of the samples (3 to 5 mm) were significantly narrower than the lengths of the foils (55 mm to 100 mm). The foils were vacuum sealed in a laminate polymer-metal pouch. To avoid capturing material from the pouch, volumes sampled in the tomograms were smaller than the volumes of the foils. Representative results are shown in
Micro x-ray diffraction (μ-XRD) was performed using Beamline 12.3.2 at the Advanced Light Source, Lawrence Berkeley National Laboratory (ALS, LBNL). Diffraction spots were obtained from two sites within 50 μm of one another in a 60-μm-thick, rolled lithium metal foil.
Fluorescence experiments were performed on a defect in a rolled lithium metal foil using a LabRam J-Y spectrometer equipped with a BX40 Olympus microscope in backscattering geometry (180°), aHeNe laser (633 nm wavelength) with a spot size of about 1 μm, and a 600 gr/mm grating. The results are shown in the images in
Raman spectroscopy was performed on both rolled and extruded lithium foils, and the spectra are shown in
Defect densities in lithium metal foils purchased from four commercial sources, as measured using x-ray tomography, are shown in
A lithium metal symmetric cell was constructed with a 60 μm-thick, rolled lithium metal foils as anode and cathode and a polymer electrolyte as the separator. The cell was cycled at 100 μA/cm2, with 7 μm of lithium transferred throughput per cycle.
There is a disturbed region in the electrolyte adjacent to the defect in the lithium metal foil. Such disturbed regions are not observed elsewhere in the cell. As a cell continues to be cycled, the disturbed region in the electrolyte can grow and eventually can extend through the entire thickness of the electrolyte. Once the disturbed region reaches the opposite electrode (or more precisely, once numerous disturbances span the electrolyte), the cell has a short circuit pathway and may fail.
As a secondary lithium battery (with a lithium metal anode) cell cycles, lithium leaves the anode as the cell discharges and is electroplated back onto the anode as the cell charges. It has been shown that the morphology of such electroplated lithium is influenced greatly by the current density at the anode. Plated lithium metal is smoother when deposited at low current densities than at high current densities. It has been shown that as the limiting current density of an electrolyte. i.e., the current density at which the ion concentration near the electrode approaches zero, is reached and exceeded, the morphology of electroplated lithium changes drastically, becoming less dense and more uncontrolled. At this current density, the electrochemical plating rate of the ions is greater than that which can be supported by electrolyte ion transport properties, leading to salt depletion.) The mechanism for this uncontrolled plating is not well understood, but it could be that as salt concentration approaches zero, there is an overpotential to move charge across this zone that has little or no salt. This overpotential is manifested as a high local electric field, which can result in electrochemical degradation of the electrolyte in addition to the nonuniform plating. The electrolyte degradation may further influence the uncontrolled plating. It is expected that operating a lithium ion cell below the limiting current density will minimize the amount of uncontrolled lithium plating.
Defects that contain lithium hydride, lithium hydroxide, lithium carbonate, lithium nitride, and/or lithium oxide, as described above, are less electronically conductive (more insulating) than lithium metal. When such defects or insulating regions are on or near the surface of a lithium metal anode, they affect the local current density distribution during lithium plating. Because lithium ions cannot plate onto the insulating regions, the current density in in the electrolyte at those regions is zero. In general, the current density adjacent to such insulating regions may be higher than the average current density across the anode. In this way, although a cell may be operating below its limiting current density, there may be regions near such insulating defect regions in which the local current density exceeds the limiting current density. The larger the insulating regions, the larger the local current density adjacent to them. Factors that contribute to determining a largest acceptable defect size include average applied current density and transport properties of the electrolyte. It is advantageous if there is no local current density that exceeds the limiting current density for the cell. Thus a largest acceptable insulating defect size, i.e., a largest size below which cell shorting is unlikely to occur as a cell cycles, can be determined.
As shown in Table I below, the electronic conductivities of materials that most likely make up the faceted defects are different from the electronic conductivity in lithium metal. Such a difference changes the distribution of potential across the lithium metal electrode surface and affects the uniformity of transfer of charge in the region of the defect. Such differences may cause undesirable electrochemical reactions and/or inconsistent plating and stripping of lithium around the defects.
Lithium metal is commonly purified either electrolytically or by evaporation (sometimes described as distillation). Both processes target total purity based on a moderate number of elements, usually no more than 12. The most commonly-identified elements included in manufacturers' purity specifications include some or all of Li, Na, K, Ca, Fe, N, Si, Cl, Al, Ni, and Cu. For example, the following are specification for battery grade lithium offered by some major suppliers:
In spite of control of these impurities, faceted defects, which may include lithium hydride, lithium hydroxide, lithium carbonate, lithium nitride, and/or lithium oxide, are still found in such commercially-available lithium metal foils. As can be seen from the exemplary specifications above, hydrogen, carbon, nitrogen, and oxygen are not elements whose concentrations are specified, implying that such elements are not specifically controlled, measured, or removed.
In some embodiments of the invention, methods are provided to reduce the hydrogen, carbon, nitrogen, and/or oxygen concentration in a lithium metal foil. Examples or methods that can be used include, but are not limited to, distillation, melt-separation, electrolysis, and gettering reactions (hot traps). Several getter materials, such as yttrium, zirconium, and calcium, can reduce the amount of hydrogen, nitrogen, and oxygen in a lithium melt. Temperature, vacuum pressure, mass ratios, surface area ratios, and the design and dimensions of the apparatus are conditions that affect the gettering processing. In various embodiments, temperatures between 350° C. and 550° C. and pressures less than 10-5 mbar are used in a gettering process. In various embodiments, a mass ratio of getter material to lithium ratio ranges from 0.1 to 0.25.
There are several materials that can getter impurities from molten lithium. An Ellingham diagram of a reaction's free energy versus temperature can identify the best candidates. Hot-trap metals, directly or indirectly exposed to molten lithium, preferentially react with unwanted impurities in lithium such as oxygen, nitrogen, and hydrogen. The mechanism may be the chemical reaction of lithium hydrides, nitrides, and/or oxides by metals that are more reactive.
In an exemplary embodiment, a simple hot trap process was used at a temperature of 550° C. with molten lithium that contained a yttrium to lithium mass ratio of 0.25 to 1. Some of the molten lithium was processed for 60 minutes, and some molten lithium was processed for 180 minutes. The pure yttrium and the reacted yttrium were separated from the lithium by gravity settling. The molten lithium was then cooled and the yttrium-containing material that had settled out was removed, leaving only purified lithium. Lithium metal foils were formed by pressing the purified lithium. X-ray tomography was performed on the lithium metal foils to determine their crystalline defect densities. The results are shown in
In another embodiment of the invention, techniques for removing crystalline defects with getter materials involves mechanical mixing of molten lithium with particles of getter material (e.g., calcium, zirconium, yttrium, and others as discussed above) and then filtering to remove the getter particles. Similarly, molten lithium may be passed through a packed bed of getter material or pumped through a mesh made of getter material. Other contact mechanisms where pipes or containers are constructed of getter material may also be used to make contact between molten lithium and getter material. Essentially, any mechanism that effects contact between a getter material and molten lithium may be employed to ensure that getter materials react with and remove trace elements such as oxygen, nitrogen, and hydrogen from molten lithium. The reaction products of the getter materials with oxygen, nitrogen, and/or hydrogen materials can be removed, leaving purified lithium with a reduced density of lithium-based crystalline defects in lithium metal foils made therefrom.
In a secondary lithium battery cell, even just one defect at the surface of a lithium foil anode can lead to formation of a lithium shunt in the separator electrolyte that can cause a short circuit path as a cell cycles. It is known that lithium shunts that can lead to shorting may burn off or self-heal instead due to the large amount of current that can pass through such narrow shunts. When such a burn-off process occurs, shunts are less likely to lead to cell death. However, if a sufficient number of shunts are present at the same time and maintained, short circuit current is distributed among them instead of being concentrated on just one shunt, and the shunts are less likely to burn off or self-heal. Under such conditions a cell may not be able to recover, and it may fail due to poor coulombic efficiency and self-discharge. Thus, although some shunts can be tolerated without causing significant damage to a cell, it is still important to minimize the number of such defects that can lead to shunts that can form short circuit pathways.
Lithium Metal Foils with Ideal Crystalline Defect Densities
In an exemplary embodiment, a lithium metal secondary battery cell with a capacity of 10 Ah has a lithium foil surface area of 1.35 m2. One crystalline surface defect with a size of 20 or more can cause a short circuit path during cycling. For an idealized completely defect-free cell manufacturing yield of 99%, i.e., 99% of cells do not contain a single detectable crystalline surface defect that can cause a lithium shunt, the lithium metal foil used in the cells can have no more than I defect per 135 m2.
In another exemplary embodiment, a lithium metal secondary battery cell has a lithium foil thickness of 20 μm, corresponding to a lithium volume per cell of I 013 μm3 One crystalline surface defect with a size of 20 μm (approximate volume of 8000 μm3) or more can cause a short circuit path during cycling. For an idealized, completely defect-free manufacturing yield of 99%, i.e., 99% of cells do not contain a single detectable crystalline defect that can cause a lithium shunt, the lithium metal foil used in the cells can have no more than I defect with a size of 20 μm or more per 1.35×106 mm3.
Lithium Metal Foils with Pragmatic and Acceptable Crystalline Defect Densities
In an exemplary embodiment, a lithium metal secondary battery cell has a non-zero but acceptable self-discharge rate governed by a density of lithium shunts that have formed adjacent to crystalline defects. Typical self-discharge for lithium ion chemistries are in the range of 3-5% of cell capacity per month. With this same pragmatic boundary limit, lithium metal cells may have a certain shunt defect density which results in the same self-discharge rate (5% per month). Given a 10 Ah cell with a lithium metal anode and a LFP (lithium ferrous phosphate) cathode, over one month, a 5% self-discharge would occur with a total shunt resistance of approximately 4.2 kohms. Given that the shunts that may form in the separator electrolyte are made of lithium metal and are approximately the same cross sectional area as the 20 μm crystalline defects in the lithium foil (approximate volume of 8000 μm3 for a 20 μm thick separator), the total shunt resistance that would occur with a crystalline defect surface density in the lithium foil of about 1 per mm2 or a volumetric density of 100 per mm3 may be acceptable from a self-discharge and cell efficiency perspective. Such an allowable crystalline defect density is a limit that is easier to achieve and offers a pragmatic alternative to an ideal crystalline defect density limit, which is very difficult to achieve. Nevertheless, such a pragmatic limit is still much lower (by orders of magnitude) than what is currently available in any commercially-available lithium foil. The purification processes discussed herein have produced lithium foil with crystalline defect densities below this pragmatic limit.
In another embodiment of the invention, the lithium metal material described herein is used as an anode in a battery cell. With reference to
A polymer electrolyte may also include electrolyte salt(s) that help to provide ionic conductivity. Any of the polymer electrolytes described herein may be liquid or solid, depending on molecular weight. Examples of useful Li salts include, but are not limited to, LiPF6, LiBF4, LiN(CF3SQ2)2, Li(CF3SQ2)3C, LiN(SO2CF2CF3)2, LiB(C2Q4)2, Li2B12FxH12-x, Li2B12F12, LiTFSI, LiFSI, and mixtures thereof. Examples of solid polymer electrolytes include, but are not limited to, block copolymers that contain ionically-conductive blocks and structural blocks that make up ionically-conductive phases and structural phases, respectively. The ionically-conductive phase may contain one or more linear polymers such as polyethers, polyamines, polyimides, polyamides, poly alkyl carbonates, polynitriles, perfluoro polyethers, fluorocarbon polymers substituted with high dielectric constant groups such as nitriles, carbonates, and sulfones, and combinations thereof. In one arrangement, the ionically-conductive phase contains one or more phosphorous-based polyester electrolytes, as disclosed herein. The linear polymers can also be used in combination as graft copolymers with polysiloxanes, polyalkoxysiloxanes, polyphosphazines, polyolefins, and/or polydienes to form the conductive phase. The structural phase can be made of polymers such as polystyrene, hydrogenated polystyrene, polymethacrylate, poly(methy1 methacrylate), polyviny1pyridine, polyviny1cyclohexane, polyimide, polyamide, polypropylene, polyolefins, poly(t-butyl vinyl ether), poly(cyclohexyl methacrylate), poly(cyclohexyl vinyl ether), poly(t-butyl vinyl ether), polyethylene, poly(phenylene oxide), poly(2,6-dimethyl-1,4-phenylene oxide), poly(phenylene sulfide), poly(phenylene sulfide sulfone), poly(phenylene sulfide ketone), poly(phenylene sulfide amide), polysulfone, fluorocarbons, such as polyvinylidene fluoride, or copolymers that contain styrene, methacrylate, or vinylpyridine. It is especially useful if the structural phase is rigid and is in a glassy or crystalline state.
Suitable cathode active materials include, but are not limited to, LFP (lithium iron phosphate), LMP (lithium metal phosphate in which the metal can be Mn, Co, or Ni), V2Os (divanadium pentoxide), NCA (lithium nickel cobalt aluminum oxide), NCM (lithium nickel cobalt manganese oxide), high energy NCM (HE-NCM-magnesium-rich lithium nickel cobalt manganese oxide), lithium manganese spinel, lithium nickel manganese spinel, and combinations thereof. Suitable electronically-conductive additives include, but are not limited to, carbon black, graphite, vapor-grown carbon fiber, graphene, carbon nanotubes, and combinations thereof. A binder can be used to hold together the cathode active material particles and the electronically conductive additive. Suitable binders include, but are not limited to, PVDF (polyvinylidene difluoride), PVDF-HFP poly (vinylidene fluoride-co-hexafluoropropylene), PAN (polyacrylonitrile), PAA (polyacrylic acid), PEO (polyethylene oxide), CMC (carboxymethyl cellulose), and SBR (styrene-butadiene rubber).
Any of the polymer electrolytes described herein may be liquid or solid, depending on molecular weight.
This invention has been described herein in considerable detail to provide those skilled in the art with information relevant to apply the novel principles and to construct and use such specialized components as are required. However, it is to be understood that the invention can be carried out by different equipment, materials and devices, and that various modifications, both as to the equipment and operating procedures, can be accomplished without departing from the scope of the invention itself
This application is a division of U.S. application Ser. No. 16/294,896, filed Mar. 6, 2019, which claims the benefit of U.S. Provisional Patent Application 62/640,025, filed Mar. 8, 2018, the disclosures of which are incorporated in their entirety by reference herein.
Number | Date | Country | |
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62640025 | Mar 2018 | US |
Number | Date | Country | |
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Parent | 16294896 | Mar 2019 | US |
Child | 17378297 | US |