The field of the disclosure relates generally to the formation of secondary batteries, and more specifically, to a cell formation system for lithium based secondary batteries.
In rocking-chair battery cells, both the positive electrode and the negative electrode of a secondary battery comprise materials into which a carrier ion, such as lithium, inserts and extracts. As the battery is discharged, carrier ions are extracted from the negative electrode and inserted into the positive electrode. As the battery is charged, the carrier ion is extracted from the positive electrode and inserted into the negative electrode.
Silicon has become a promising candidate to replace carbonaceous materials as the anode because of its high specific capacity. For instance, graphite anodes formed from LiC6 may have a specific capacity of about 370 milli-amp hours per gram (mAh/g), while crystalline silicon anodes formed from Li15S14 may have a specific capacity of about 3600 mAh/g, a nearly 10-fold increase over graphite anodes. However, the use of silicon anodes has been limited, due to the large volumetric changes (e.g., 300%) in silicon when Li carrier ions are inserted into silicon anodes. This volumetric increase along with the cracking and pulverization associated with the charge and discharge cycles has limited the use of silicon anodes in practice. In addition, the use of silicon anodes has been limited due to its poor initial columbic efficiency (ICE), which leads to a capacity loss during the initial formation of secondary batteries that utilize silicon anodes.
After a lithium based secondary battery is assembled, the assembled battery is typically subjected to a formation process. During the formation process the battery is slowly charged and discharged one or more times. At least some known formation processes include a pre-lithiation process to add lithium to the battery. These formation processes are typically performed by large centralized systems. Such systems include a central control center that is connected to all of the batteries that are to undergo the formation process. The central control center directly controls the charging, discharging, and (where applicable) pre-lithiation of all of the batteries to which it is connected. In order to be capable of controlling the formation processes and distributing electrical power to a large number of batteries, the central control centers are relatively large and expensive systems using a significant amount of power, occupying a significant amount of space, and utilizing a large amount of wire to connect to all of the batteries undergoing formation.
One aspect of the present disclosure is a method of pre-lithiating a lithium based secondary battery, the lithium based secondary battery comprising a population of unit cells, an electrode busbar, and a counter-electrode busbar, wherein each unit cell of the population of unit cells comprises an electrode structure, a separator structure, and a counter-electrode structure, the electrode structure of each member of the unit cell population comprises an electrode current collector and an electrode active material layer, the counter-electrode structure of each member of the unit cell population comprises a counter-electrode current collector and a counter-electrode active material layer, and an auxiliary electrode containing lithium metal is connected to the population of unit cells. The method includes: (i) charging the lithium based secondary battery using a charging circuit connected to the electrode busbar and the counter-electrode busbar; (ii) stopping charging the lithium based secondary battery using the charging circuit when the battery voltage reaches a first voltage; (iii) controlling a current sink connected to the electrode busbar and the auxiliary electrode to conduct a current from the electrode busbar through the auxiliary electrode to diffuse lithium from the auxiliary electrode to the electrode active material layers of the lithium based secondary battery; (iv) stopping controlling the current sink connected to the electrode busbar and the auxiliary electrode to conduct the current from the electrode busbar through the auxiliary electrode when the battery voltage reaches a second voltage lower than the first voltage; and (v) repeating steps (i)-(iv).
Another aspect of this disclosure is a pre-lithiation and charging module for charging and pre-lithiating a lithium based secondary battery using an auxiliary electrode containing lithium metal. The lithium based secondary battery includes a population of unit cells, an electrode busbar, and a counter-electrode busbar, wherein each unit cell of the population of unit cells comprises an electrode structure, a separator structure, and a counter-electrode structure, the electrode structure of each member of the unit cell population comprises an electrode current collector and an electrode active material layer, the counter-electrode structure of each member of the unit cell population comprises a counter-electrode current collector and a counter-electrode active material layer, and the auxiliary electrode is connected to the population of unit cells. The pre-lithiation module includes: a current sink; a charging circuit; a module controller connected to the current sink and the charging circuit. The pre-lithiation module controller includes a processor and a memory; a battery connector connected to the charging circuit and the current sink, the battery connector configured for electrical connection to the electrode busbar and the counter-electrode busbar of the lithium based secondary battery; and a pre-lithiation connector for electrical connection of the current sink to the auxiliary electrode. The memory of the module controller stores instructions that program the module controller to, when the lithium based secondary battery is connected to the battery connector and the pre-lithiation connector is connected to the auxiliary electrode: (i) charge the lithium based secondary battery using the charging circuit; (ii) stop charging the lithium based secondary battery using the charging circuit when the battery voltage reaches a first voltage; (iii) control the current sink to conduct a current from the electrode busbar through the auxiliary electrode to diffuse lithium from the auxiliary electrode to the electrode active material layers of the lithium based secondary battery; (iv) stop controlling the current sink to conduct the current from the electrode busbar through the auxiliary electrode when the battery voltage reaches a second voltage lower than the first voltage; and (v) repeat steps (i)-(iv).
Various refinements exist of the features noted in relation to the above-mentioned aspects. Further features may also be incorporated in the above-mentioned aspects. These refinements and additional features may exist individually or in any combination. For instance, various features discussed below in relation to any of the illustrated embodiments may be incorporated into any of the above-described aspects, alone or in any combination.
Corresponding reference numerals used throughout the drawings indicate corresponding parts.
“A,” “an,” and “the” (i.e., singular forms) as used herein refer to plural referents unless the context clearly dictates otherwise. For example, in one instance, reference to “an electrode” includes both a single electrode and a plurality of similar electrodes.
“About” and “approximately” as used herein refers to plus or minus 10%, 5%, or 1% of the value stated. For example, in one instance, about 250 micrometers (μm) would include 225 μm to 275 μm. By way of further example, in one instance, about 1,000 μm would include 900 μm to 1,100 μm. Unless otherwise indicated, all numbers expressing quantities (e.g., measurements, and the like) and so forth used in the specification and claims are to be understood as being modified in all instances by the term “about.” Accordingly, unless indicated to the contrary, the numerical parameters set forth in the following specification and attached claims are approximations. Each numerical parameter should at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques.
“Anode” as used herein in the context of a secondary battery refers to the negative electrode in the secondary battery.
“Anode material” or “Anodically active material” as used herein means material suitable for use as the negative electrode of a secondary battery.
“Cathode” as used herein in the context of a secondary battery refers to the positive electrode in the secondary battery.
“Cathode material” or “Cathodically active material” as used herein means material suitable for use as the positive electrode of a secondary battery.
“Conversion chemistry active material” or “Conversion chemistry material” refers to a material that undergoes a chemical reaction during the charging and discharging cycles of a secondary battery.
“Counter-electrode” as used herein may refer to the negative or positive electrode (anode or cathode), opposite of the Electrode, of a secondary battery unless the context clearly indicates otherwise.
“Counter-electrode current collector” as used herein may refer to the negative or positive (anode or cathode) current collector, opposite of the Electrode current connector, of a secondary battery unless the context clearly indicates otherwise.
“Counter-electrode material” as used herein may refer to anode material or cathode material, opposite of the Electrode material, unless the context clearly indicates otherwise.
“Counter-electrode structure” as used herein may refer to an anode structure (e.g., negative electrode structure) or a cathode structure (e.g., positive electrode structure), opposite of the Electrode structure, adapted for use in a battery unless the context clearly indicates otherwise.
“Cycle” as used herein in the context of cycling of a secondary battery between charged and discharged states refers to charging and/or discharging a battery to move the battery in a cycle from a first state that is either a charged or discharged state, to a second state that is the opposite of the first state (i.e., a charged state if the first state was discharged, or a discharged state if the first state was charged), and then moving the battery back to the first state to complete the cycle. For example, a single cycle of the secondary battery between charged and discharged states can include, as in a charge cycle, charging the battery from a discharged state to a charged state, and then discharging back to the discharged state, to complete the cycle. The single cycle can also include, as in a discharge cycle, discharging the battery from the charged state to the discharged state, and then charging back to a charged state, to complete the cycle.
“Electrochemically active material” as used herein means anodically active or cathodically active material.
“Electrode” as used herein may refer to the negative or positive electrode (anode or cathode) of a secondary battery unless the context clearly indicates otherwise.
“Electrode current collector” as used herein may refer to the negative or positive (anode or cathode) current collector of a secondary battery unless the context clearly indicates otherwise.
“Electrode material” as used herein may refer to anode material or cathode material unless the context clearly indicates otherwise.
“Electrode structure” as used herein may refer to an anode structure (e.g., negative electrode structure) or a cathode structure (e.g., positive electrode structure) adapted for use in a battery unless the context clearly indicates otherwise.
“Capacity” or “C” as used herein refers to an amount of electric charge that a battery (or a sub-portion of a battery comprising one or more pairs of electrode structures and counter-electrode structures that form a bilayer) can deliver at a pre-defined voltage unless the context clearly indicates otherwise.
“Electrolyte” as used herein refers to a non-metallic liquid, gel, or solid material in which current is carried by the movement of ions adapted for use in a battery unless the context clearly indicates otherwise.
“Charged state” as used herein in the context of the state of a secondary battery refers to a state where the secondary battery is charged to at least 75% of its rated capacity unless the context clearly indicates otherwise. For example, the battery may be charged to at least 80% of its rated capacity, at least 90% of its rated capacity, and even at least 95% of its rated capacity, such as 100% of its rated capacity.
“Discharge capacity” as used herein in connection with a negative electrode means the quantity of carrier ions available for extraction from the negative electrode and insertion into the positive electrode during a discharge operation of the battery between a predetermined set of cell end of charge and end of discharge voltage limits unless the context clearly indicates otherwise.
“Discharged state” as used herein in the context of the state of a secondary battery refers to a state where the secondary battery is discharged to less than 25% of its rated capacity unless the context clearly indicates otherwise. For example, the battery may be discharged to less than 20% of its rated capacity, such as less than 10% of its rated capacity, and even less than 5% of its rated capacity, such as 0% of its rated capacity.
“Reversible coulombic capacity” as used herein in connection with an electrode (i.e., a positive electrode, a negative electrode or an auxiliary electrode) means the total capacity of the electrode for carrier ions available for reversible exchange with a counter-electrode.
“Longitudinal axis,” “transverse axis,” and “vertical axis,” as used herein refer to mutually perpendicular axes (i.e., each are orthogonal to one another). For example, the “longitudinal axis,” “transverse axis,” and the “vertical axis” as used herein are akin to a Cartesian coordinate system used to define three-dimensional aspects or orientations. As such, the descriptions of elements of the disclosed subject matter herein are not limited to the particular axis or axes used to describe three-dimensional orientations of the elements. Alternatively stated, the axes may be interchangeable when referring to three-dimensional aspects of the disclosed subject matter.
“Composite material” or “Composite” as used herein refers to a material which comprises two or more constituent materials unless the context clearly indicates otherwise.
“Void fraction” or “Porosity” or “Void volume fraction” as used herein refers to a measurement of the voids (i.e., empty) spaces in a material, and is a fraction of the volume of voids over the total volume of the material, between 0 and 1, or as a percentage between 0% and 100%.
“Polymer” as used herein may refer to a substance or material consisting of repeating subunits of macromolecules unless the context clearly indicates otherwise.
“Microstructure” as used herein may refer to the structure of a surface of a material revealed by an optical microscope above about 25× magnification unless the context clearly indicates otherwise.
“Microporous” as used herein may refer to a material containing pores with diameters less than about 2 nanometers unless the context clearly indicates otherwise.
“Macroporous” as used herein may refer to a material containing pores with diameters greater than about 50 nanometers unless the context clearly indicates otherwise.
“Nanoscale” or “Nanoscopic scale” as used herein may refer to structures with a length scale in the range of about 1 nanometer to about 100 nanometers.
“Pre-lithiation” or “pre-lithiate” as used herein may refer to the addition of lithium to the active lithium content of a lithium based secondary battery as part of the formation process prior to battery operation to compensate for the loss of active lithium. “Pre-lithiation” or “pre-lithiate” may also be referred to herein as a “buffer process.”
“Separator,” “Separator layer,” or “Separator structure” as used herein may refer to electrically insulating but ionically permeable separator material that is adapted to electrically isolate an electrode structure and an adjacent counter-electrode structure.
“Unit cell” as used herein may refer to a subassembly of a secondary battery that includes an electrode structure, a counter-electrode structure, and a separator between the electrode structure and the counter-electrode structure.
Some embodiments of the present disclosure may provide benefits such as mitigation or improvement of the poor ICE associated with silicon-based anodes in secondary batteries utilizing an auxiliary anode electrochemically coupled with the secondary battery that provides additional carrier ion during and/or subsequent to initial battery formation. The use of an auxiliary anode mitigates the initial loss of carrier ions in the secondary battery during initial formation, thereby providing a technical benefit of, for example, increasing the capacity of the secondary battery after formation. Further, the introduction of additional carrier ions after battery formation mitigates the cycle-based decrease in carrier ions that are typically lost through secondary reactions, thereby providing a technical benefit of decreasing the cycle-by-cycle capacity loss in a secondary battery. Further still, the introduction of additional carrier ions after battery formation improves the cycling performance of the secondary battery by maintaining the anode of the secondary battery at a lower potential voltage at discharge, as the anode includes additional carrier ions. In some embodiments, the auxiliary anode is removed from the secondary battery after formation, thereby providing a technical benefit of increasing the energy density of the battery.
As illustrated in
Each of the unit cells 102 includes at least one the anodically active material layer 104 and at least one cathodically active material layer 106. The anodically active material layer 104 and the cathodically active material layer 106 of each unit cell 102 are electrically isolated by a separator layer 108, which may also be referred to as a separator 108. It should be appreciated that in suitable embodiments of the present disclosure, any number of the unit cells 102 may be used, such as from 1 to 200 or more of the unit cells 102 in the secondary battery 100.
For each of the unit cells 102, in some embodiments, the separator layer 108 is an ionically permeable polymeric woven material suitable for use as a separator in a secondary battery. In an embodiment, the separator layer 108 is coated with ceramic particles on one or both sides.
Referring to
In this embodiment, the first busbar 110 is electrically coupled with a first electrical terminal 124 of the secondary battery 100, which is electrically conductive. When the first busbar 110 comprises an anode busbar for the secondary battery 100, the first electrical terminal 124 comprises a negative terminal for the secondary battery. Further in this embodiment, the second busbar 112 is electrically coupled with a second electrical terminal 125 of the secondary battery 100, which is electrically conductive. When the second busbar 112 comprises a cathode busbar for the secondary battery 100, the second electrical terminal 125 comprises a positive terminal for the secondary battery.
In one embodiment, a casing 116, which may be referred to as a constraint, may be applied over one or both of the X-Y surfaces of the electrode assembly 150. In the embodiment shown in
In some embodiments, the casing 116 comprises a sheet having a thickness in the range of about 10 to about 100 micrometers. In one embodiment, the casing 116 comprises a stainless-steel sheet (e.g., SS316) having a thickness of about 30 μm. In another embodiment, the casing 116 comprises an aluminum sheet (e.g., 7075-T6) having a thickness of about 40 μm. In another embodiment, the casing 116 comprises a zirconia sheet (e.g., Coorstek YZTP) having a thickness of about 30 μm. In another embodiment, the casing 116 comprises an E Glass UD/Epoxy 0 deg sheet having a thickness of about 75 μm. In another embodiment, the casing 116 comprises 12 μm carbon fibers at >50% packing density.
The casing 116 defines a first major surface 126 and a second major surface 127 that opposes the first major surface 126. The major surfaces 126, 127 of the casing 116 may be substantially planar is some embodiments.
With reference to
An anode current collector 202 of the multilayer stack 200 is shown in the center of the portion of the multilayer stack 200 shown in
In the example embodiment, each of the anodically active material layers 104 is a layer of anodically active material on at least one major surface of an anode current collector 202. Each of the cathodically active material layers 106 is a layer of cathodically active material on at least one major surface of a cathode current collector 204. In other embodiments, one or more of the anodically active material layers 104 and corresponding anode current collector 202 may be a single layer of suitable material. Additionally and/or alternatively, one or more of the cathodically active material layers 106 and corresponding cathode current collector 204 may be a single layer of suitable material.
The relative placement of the anode current collector layer 202, the anodically active material layer 104, the separator 108, the cathodically active material layer 106, and the cathode current collector layer 204 in the portion of the multilayer stack 200 shown in
The multilayer stack 200 includes stacked groups of the anode current collector layer 202, the anodically active material layer 104, the separator 108, the cathodically active material layer 106, and the cathode current collector layer 204. The stacked groups of the multilayer stack 200 may also be referred to as “unit cells,” such as the unit cells 102 in
In
A voltage difference V exists between adjacent cathode structures 206 and anode structures 207, with the adjacent structures considered a bilayer in some embodiments. Each bilayer has a capacity C determined by the makeup and configuration of the cathode structures 206 and the anode structures 207. In this embodiment, each bilayer produces a voltage difference of about 4.35 volts. In other embodiments, each bilayer has a voltage difference of about 0.5 volts, about 1.0 volts, about 1.5 volts, about 2.0 volts, about 2.5 volts, about 3.0 volts, about 3.5 volts, about 4.0 volts, 4.5 volts, about 5.0 volts, between 4 and 5 volts, or any other suitable voltage. During cycling between a charged state and a discharged state, the voltage may vary, for example, between about 2.5 volts and about 4.35 volts. The capacity C of a bilayer in this embodiment is about 3.5 milliampere-hour (mAh). In other embodiments, the capacity C of a bilayer is about 2 mAh, less than 5 mAh, or any other suitable capacity. In some embodiments, the capacity C of a bilayer may be up to about 10 mAh.
The cathode current collector 204 may comprise aluminum, nickel, cobalt, titanium, and tungsten, or alloys thereof, or any other material suitable for use as a cathode current collector layer. In general, the cathode current collector 204 will have an electrical conductivity of at least about 103 Siemens/cm. For example, in one such embodiment, the cathode current collector 204 will have a conductivity of at least about 104 Siemens/cm. By way of further example, in one such embodiment, the cathode current collector 204 will have a conductivity of at least about 105 Siemens/cm. In general, the cathode current collector 204, may comprise a metal such as aluminum, carbon, chromium, gold, nickel, NiP, palladium, platinum, rhodium, ruthenium, an alloy of silicon and nickel, titanium, or a combination thereof (see “Current collectors for positive electrodes of lithium-based batteries” by A. H. Whitehead and M. Schreiber, Journal of the Electrochemical Society, 152(11) A2105-A2113 (2005)). By way of further example, in one embodiment, the cathode current collector 204 comprises gold or an alloy thereof such as gold silicide. By way of further example, in one embodiment, the cathode current collector 204 comprises nickel or an alloy thereof such as nickel silicide.
The cathodically active material layer 106 may be an intercalation-type chemistry active material, a conversion chemistry active material, or a combination thereof.
Exemplary conversion chemistry materials useful in the present disclosure include, but are not limited to, S (or Li2S in the lithiated state), LiF, Fe, Cu, Ni, FeF2, FeOdF3.2d, FeF3, CoF3, CoF2, CuF2, NiF2, where 0≤d≤0.5, and the like.
Exemplary cathodically active material layers 106 also include any of a wide range of intercalation-type cathodically active materials. For example, for a lithium-ion battery, the cathodically active material may comprise a cathodically active material selected from transition metal oxides, transition metal sulfides, transition metal nitrides, lithium-transition metal oxides, lithium-transition metal sulfides, and lithium-transition metal nitrides may be selectively used. The transition metal elements of these transition metal oxides, transition metal sulfides, and transition metal nitrides can include metal elements having a d-shell or f-shell. Specific examples of such metal element are Sc, Y, lanthanoids, actinoids, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, Fe, Ru, Os, Co, Rh, Ir, Ni, Pb, Pt, Cu, Ag, and Au. Additional cathodically active materials include lithium cobalt oxide (LiCoO2), LiNi0.5Mn1.5O4, Li(NixCoyAlz)O2, lithium metal phosphate (e.g., lithium iron phosphate, LiFePO4), Li2MnO4, V2O5, molybdenum oxysulfides, phosphates, silicates, vanadates, sulfur, sulfur compounds, oxygen (air), lithium nickel manganese cobalt oxide (Li(NixMnyCoz)O2), and combinations thereof.
In general, the cathodically active material layers 106 will have a thickness of at least about 20 μm. For example, in one embodiment, the cathodically active material layers 106 will have a thickness of at least about 40 μm. By way of further example, in one such embodiment, the cathodically active material layers 106 will have a thickness of at least about 60 μm. By way of further example, in one such embodiment, the cathodically active material layers 106 will have a thickness of at least about 100 μm. Typically, the cathodically active material layers 106 will have a thickness of less than about 90 μm or less than about 70 μm.
The length LCE of the cathode structures 206 will vary depending upon the secondary battery 100 and its intended use. In general, however, each cathode structure 206 will typically have a length LCE in the range of about 5 millimeters (mm) to about 500 mm. For example, in one such embodiment, each cathode structure 206 has a length LCE of about 10 mm to about 250 mm. By way of further example, in one such embodiment each cathode structure 206 has a length LCE of about 25 mm to about 100 mm. According to one embodiment, the cathode structures 206 include one or more first electrode members having a first length, and one or more second electrode members having a second length that is different than the first length. In yet another embodiment, the different lengths for the one or more first electrode members and one or more second electrode members may be selected to accommodate a predetermined shape for an electrode assembly (e.g., the electrode assembly 150 of
The width WCE of the cathode structures 206 will also vary depending upon the secondary battery 100 and its intended use. In general, however, the cathode structures 206 will typically have a width WCE within the range of about 0.01 mm to 2.5 mm. For example, in one embodiment, the width WCE of each cathode structure 206 will be in the range of about 0.025 mm to about 2 mm. By way of further example, in one embodiment, the width WCE of each cathode structure 206 will be in the range of about 0.05 mm to about 1 mm. According to one embodiment, the cathode structures 206 include one or more first electrode members having a first width, and one or more second electrode members having a second width that is different than the first width. In yet another embodiment, the different widths for the one or more first electrode members and one or more second electrode members may be selected to accommodate a predetermined shape for the secondary battery 100, such as an assembly having a different widths along one or more of the longitudinal and/or transverse axis, and/or to provide predetermined performance characteristics for the secondary battery.
The height HCE of the cathode structures 206 will also vary depending upon the secondary battery 100 and its intended use. In general, however, the cathode structures 206 will typically have a height HCE within the range of about 0.05 mm to about 25 mm. For example, in one embodiment, the height HCE of each cathode structure 206 will be in the range of about 0.05 mm to about 5 mm. By way of further example, in one embodiment, the height HCE of each cathode structure 206 will be in the range of about 0.1 mm to about 1 mm. According to one embodiment, the cathode structures 206 include one or more first cathode members having a first height, and one or more second cathode members having a second height that is different than the first height. In yet another embodiment, the different heights for the one or more first cathode members and one or more second cathode members may be selected to accommodate a predetermined shape for the secondary battery 100, such as a shape having a different heights along one or more of the longitudinal and/or transverse axis, and/or to provide predetermined performance characteristics for the secondary battery.
In general, each cathode structure 206 has a length LCE that is substantially greater than its width WCE and substantially greater than its height HCE. For example, in one embodiment, the ratio of LCE to each of WCE and HCE is at least 5:1, respectively (that is, the ratio of LCE to WCE is at least 5:1, respectively and the ratio of LCE to HCE is at least 5:1, respectively), for each cathode structure 206. By way of further example, in one embodiment the ratio of LCE to each of WCE and HCE is at least 10:1 for each cathode structure 206. By way of further example, in one embodiment, the ratio of LCE to each of WCE and HCE is at least 15:1 for each cathode structure 206. By way of further example, in one embodiment, the ratio of LCE to each of WCE and HCE is at least 20:1 for each cathode structure 206.
In one embodiment, the ratio of the height HCE to the width WCE of the cathode structures 206 is at least 0.4:1, respectively. For example, in one embodiment, the ratio of HCE to WCE will be at least 2:1, respectively, for each cathode structure 206. By way of further example, in one embodiment the ratio of HCE to WCE will be at least 10:1, respectively, for each cathode structure 206. By way of further example, in one embodiment the ratio of HCE to WCE will be at least 20:1, respectively, for each cathode structure 206. Typically, however, the ratio of HCE to WCE will generally be less than 1,000:1, respectively, for each cathode structure 206. For example, in one embodiment the ratio of HCE to WCE will be less than 500:1, respectively, for each cathode structure 206. By way of further example, in one embodiment the ratio of HCE to WCE will be less than 100:1, respectively. By way of further example, in one embodiment the ratio of HCE to WCE will be less than 10:1, respectively. By way of further example, in one embodiment the ratio of HCE to WCE will be in the range of about 2:1 to about 100:1, respectively, for each cathode structure 206.
Referring again to
In general, the anodically active material layers 104 in the multilayer stack 200 may be selected from the group consisting of: (a) silicon (Si), germanium (Ge), tin (Sn), lead (Pb), antimony (Sb), bismuth (Bi), zinc (Zn), aluminum (Al), titanium (Ti), nickel (Ni), cobalt (Co), and cadmium (Cd); (b) alloys or intermetallic compounds of Si, Ge, Sn, Pb, Sb, Bi, Zn, Al, Ti, Ni, Co, or Cd with other elements; (c) oxides, carbides, nitrides, sulfides, phosphides, selenides, and tellurides of Si, Ge, Sn, Pb, Sb, Bi, Zn, Al, Ti, Fe, Ni, Co, V, or Cd, and their mixtures, composites, or lithium-containing composites; (d) salts and hydroxides of Sn; (e) lithium titanate, lithium manganate, lithium aluminate, lithium-containing titanium oxide, lithium transition metal oxide, ZnCo2O4; (f) particles of graphite and carbon; (g) lithium metal; and (h) combinations thereof.
Exemplary anodically active material layers 104 include carbon materials such as graphite and soft or hard carbons, or graphene (e.g., single-walled or multi-walled carbon nanotubes), or any of a range of metals, semi-metals, alloys, oxides, nitrides and compounds capable of intercalating lithium or forming an alloy with lithium. Specific examples of the metals or semi-metals capable of constituting the anode material include graphite, tin, lead, magnesium, aluminum, boron, gallium, silicon, Si/C composites, Si/graphite blends, silicon oxide (SiOx), porous Si, intermetallic Si alloys, indium, zirconium, germanium, bismuth, cadmium, antimony, silver, zinc, arsenic, hafnium, yttrium, lithium, sodium, graphite, carbon, lithium titanate, palladium, and mixtures thereof. In one exemplary embodiment, the anodically active material comprises aluminum, tin, or silicon, or an oxide thereof, a nitride thereof, a fluoride thereof, or other alloy thereof. In another exemplary embodiment, the anodically active material layers 104 comprise silicon or an alloy or oxide thereof.
In one embodiment, the anodically active material layers 104 are microstructured to provide a significant void volume fraction to accommodate volume expansion and contraction as lithium ions (or other carrier ions) are incorporated into or leave the anodically active material layers 104 during charging and discharging processes for the secondary battery 100. In general, the void volume fraction of (each of) the anodically active material layer 104 is at least 0.1. Typically, however, the void volume fraction of (each of) the anodically active material layer 104 is not greater than 0.8. For example, in one embodiment, the void volume fraction of (each of) the anodically active material layer 104 is about 0.15 to about 0.75. By way of the further example, in one embodiment, the void volume fraction of (each of) the anodically active material layer 104 is about 0.2 to about 0.7. By way of the further example, in one embodiment, the void volume fraction of (each of) the anodically active material layer 104 is about 0.25 to about 0.6.
Depending upon the composition of the microstructured anodically active material layers 104 and the method of their formation, the microstructured anodically active material layers may comprise macroporous, microporous, or mesoporous material layers or a combination thereof, such as a combination of microporous and mesoporous, or a combination of mesoporous and macroporous. Microporous material is typically characterized by a pore dimension of less than 10 nanometer (nm), a wall dimension of less than 10 nm, a pore depth of 1 μm to 50 μm, and a pore morphology that is generally characterized by a “spongy” and irregular appearance, walls that are not smooth, and branched pores. Mesoporous material is typically characterized by a pore dimension of 10 nm to 50 nm, a wall dimension of 10 nm to 50 nm, a pore depth of 1 μm to 100 μm, and a pore morphology that is generally characterized by branched pores that are somewhat well defined or dendritic pores. Macroporous material is typically characterized by a pore dimension of greater than 50 nm, a wall dimension of greater than 50 nm, a pore depth of 1 μm to 500 μm, and a pore morphology that may be varied, straight, branched, or dendritic, and smooth or rough-walled. Additionally, the void volume may comprise open or closed voids, or a combination thereof. In one embodiment, the void volume comprises open voids, that is, the anodically active material layers 104 contain voids having openings at the lateral surface of the anodically active material layers through which lithium ions (or other carrier ions) can enter or leave. For example, lithium ions may enter the anodically active material layers 104 through the void openings after leaving the cathodically active material layers 106. In another embodiment, the void volume comprises closed voids, that is, the anodically active material layers 104 contain voids that are enclosed. In general, open voids can provide greater interfacial surface area for the carrier ions whereas closed voids tend to be less susceptible to SEI formation, while each provides room for the expansion of anodically active material layers 104 upon the entry of carrier ions. In certain embodiments, therefore, it is preferred that the anodically active material layers comprise a combination of open and closed voids.
In one embodiment, the anodically active material layers 104 comprise porous aluminum, tin or silicon or an alloy, an oxide, or a nitride thereof. Porous silicon layers may be formed, for example, by anodization, by etching (e.g., by depositing precious metals such as gold, platinum, silver or gold/palladium on the surface of single crystal silicon and etching the surface with a mixture of hydrofluoric acid and hydrogen peroxide), or by other methods known in the art such as patterned chemical etching. Additionally, the porous anodically active material layers 104 will generally have a porosity fraction of at least about 0.1, but less than 0.8 and have a thickness of about 1 μm to about 100 μm. For example, in one embodiment, the anodically active material layers 104 comprise porous silicon, have a thickness of about 5 μm to about 100 μm, and have a porosity fraction of about 0.15 to about 0.75. By way of further example, in one embodiment, the anodically active material layers 104 comprise porous silicon, have a thickness of about 10 μm to about 80 μm, and have a porosity fraction of about 0.15 to about 0.7. By way of further example, in one such embodiment, the anodically active material layers 104 comprise porous silicon, have a thickness of about 20 μm to about 50 μm, and have a porosity fraction of about 0.25 to about 0.6. By way of further example, in one embodiment, the anodically active material layers 104 comprise a porous silicon alloy (such as nickel silicide), have a thickness of about 5 μm to about 100 μm, and have a porosity fraction of about 0.15 to about 0.75.
In another embodiment, the anodically active material layers 104 comprise fibers of aluminum, tin, or silicon, or an alloy thereof. Individual fibers may have a diameter (thickness dimension) of about 5 nm to about 10,000 nm and a length generally corresponding to the thickness of the anodically active material layers 104. Fibers (nanowires) of silicon may be formed, for example, by chemical vapor deposition or other techniques known in the art such as vapor liquid solid (VLS) growth and solid liquid solid (SLS) growth. Additionally, the anodically active material layers 104 will generally have a porosity fraction of at least about 0.1, but less than 0.8 and have a thickness of about 1 μm to about 200 μm. For example, in one embodiment, the anodically active material layers 104 comprise silicon nanowires, have a thickness of about 5 μm to about 100 μm, and a porosity fraction of about 0.15 to about 0.75. By way of further example, in one embodiment, the anodically active material layers 104 comprise silicon nanowires, have a thickness of about 10 μm to about 80 μm, and a porosity fraction of about 0.15 to about 0.7. By way of further example, in one such embodiment, the anodically active material layers 104 comprise silicon nanowires, have a thickness of about 20 μm to about 50 μm, and a porosity fraction of about 0.25 to about 0.6. By way of further example, in one embodiment, the anodically active material layers 104 comprise nanowires of a silicon alloy (such as nickel silicide), have a thickness of about 5 μm to about 100 μm, and a porosity fraction of about 0.15 to about 0.75.
In yet other embodiments, the anodically active material layers 104 are coated with a particulate lithium material selected from the group consisting of stabilized lithium metal particles, e.g., lithium carbonate-stabilized lithium metal powder, lithium silicate stabilized lithium metal powder, or other source of stabilized lithium metal powder or ink. The particulate lithium material may be applied on the anodically active material layers 104 by spraying, loading, or otherwise disposing the lithium particulate material onto the anodically active material layers at a loading amount of about 0.05 mg/cm2 to 5 mg/cm2, e.g., about 0.1 mg/cm2 to 4 mg/cm2, or even about 0.5 mg/cm2 to 3 mg/cm2. The average particle size (D50) of the lithium particulate material may be 5 μm to 200 μm, e.g., about 10 μm to 100 μm, 20 μm to 80 μm, or even about 30 μm to 50 μm. The average particle size (D50) may be defined as a particle size corresponding to 50% in a cumulative volume-based particle size distribution curve. The average particle size (D50) may be measured, for example, using a laser diffraction method.
In one embodiment, the anode current collector 202 has an electrical conductance that is substantially greater than the electrical conductance of its associated the anodically active material layers 104. For example, in one embodiment the ratio of the electrical conductance of the anode current collector 202 to the electrical conductance of the anodically active material layers 104 is at least 100:1 when there is an applied current to store energy in the secondary battery 100 or an applied load to discharge the secondary battery. By way of further example, in some embodiments the ratio of the electrical conductance of the anode current collector 202 to the electrical conductance of the anodically active material layers 104 is at least 500:1 when there is an applied current to store energy in the secondary battery 100 or an applied load to discharge the secondary battery. By way of further example, in some embodiments the ratio of the electrical conductance of the anode current collector 202 to the electrical conductance of the anodically active material layers 104 is at least 1000:1 when there is an applied current to store energy in the secondary battery 100 or an applied load to discharge the secondary battery. By way of further example, in some embodiments the ratio of the electrical conductance of the anode current collector 202 to the electrical conductance of the anodically active material layers 104 is at least 5000:1 when there is an applied current to store energy in the secondary battery 100 or an applied load to discharge the secondary battery. By way of further example, in some embodiments, the ratio of the electrical conductance of the anode current collector 202 to the electrical conductance of the anodically active material layers 104 is at least 10,000:1 when there is an applied current to store energy in the secondary battery 100 or an applied load to discharge the secondary battery.
The length LE of the anode structures 207 will vary depending upon the secondary battery 100 and its intended use. In general, however, the anode structures 207 will typically have a length LE in the range of about 5 millimeters (mm) to about 500 mm. For example, in one such embodiment, the anode structures 207 have a length LE of about 10 mm to about 250 mm. By way of further example, in one such embodiment, the anode structures 207 have a length LE of about 25 mm to about 100 mm. According to one embodiment, the anode structures 207 include one or more first electrode members having a first length, and one or more second electrode members having a second length that is different than the first length. In yet another embodiment, the different lengths for the one or more first electrode members and the one or more second electrode members may be selected to accommodate a predetermined shape for the secondary battery 100, such as a shape having a different lengths along one or more of the longitudinal and/or transverse axis, and/or to provide predetermined performance characteristics for the secondary battery 100.
The width WE of the anode structures 207 will also vary depending upon the secondary battery 100 and its intended use. In general, however, each anode structure 207 will typically have a width WE within the range of about 0.01 mm to 2.5 mm. For example, in one embodiment, the width WE of each anode structure 207 will be in the range of about 0.025 mm to about 2 mm. By way of further example, in one embodiment, the width WE of each anode structure 207 will be in the range of about 0.05 mm to about 1 mm. According to one embodiment, the anode structures 207 include one or more first electrode members having a first width, and one or more second electrode members having a second width that is different than the first width. In yet another embodiment, the different widths for the one or more first electrode members and one or more second electrode members may be selected to accommodate a predetermined shape for the secondary battery 100, such as a shape having a different widths along one or more of the longitudinal and/or transverse axis, and/or to provide predetermined performance characteristics for the secondary battery 100.
The height HE of the anode structures 207 will also vary depending upon the secondary battery 100 and its intended use. In general, however, the anode structures 207 will typically have a height HE within the range of about 0.05 mm to about 25 mm. For example, in one embodiment, the height HE of each anode structure 207 will be in the range of about 0.05 mm to about 5 mm. By way of further example, in one embodiment, the height HE of each anode structure 207 will be in the range of about 0.1 mm to about 1 mm. According to one embodiment, the anode structures 207 include one or more first electrode members having a first height, and one or more second electrode members having a second height that is different than the first height. In yet another embodiment, the different heights for the one or more first electrode members and one or more second electrode members may be selected to accommodate a predetermined shape for the secondary battery 100, such as a shape having a different heights along one or more of the longitudinal and/or transverse axis, and/or to provide predetermined performance characteristics for the secondary battery.
In general, each anode structure 207 has a length LE that is substantially greater than each of its width WE and its height HE. For example, in one embodiment, the ratio of LE to each of WE and HE is at least 5:1, respectively (that is, the ratio of LE to WE is at least 5:1, respectively and the ratio of LE to HE is at least 5:1, respectively), for each anode structure 207. By way of further example, in one embodiment the ratio of LE to each of WE and HE is at least 10:1. By way of further example, in one embodiment, the ratio of LE to each of WE and HE is at least 15:1. By way of further example, in one embodiment, the ratio of LE to each of WE and HE is at least 20:1, for each anode structure 207.
In one embodiment, the ratio of the height HE to the width WE of the anode structures 207 is at least 0.4:1, respectively. For example, in one embodiment, the ratio of HE to WE will be at least 2:1, respectively, for each anode structure 207. By way of further example, in one embodiment the ratio of HE to WE will be at least 10:1, respectively. By way of further example, in one embodiment the ratio of HE to WE will be at least 20:1, respectively. Typically, however, the ratio of HE to WE will generally be less than 1,000:1, respectively. For example, in one embodiment the ratio of HE to WE will be less than 500:1, respectively. By way of further example, in one embodiment the ratio of HE to WE will be less than 100:1, respectively. By way of further example, in one embodiment the ratio of HE to WE will be less than 10:1, respectively. By way of further example, in one embodiment the ratio of HE to WE will be in the range of about 2:1 to about 100:1, respectively, for each anode structure 207.
Referring again to
In general, the separator layers 108 will each have a thickness of at least about 4 μm. For example, in one embodiment, the separator layers 108 will have a thickness of at least about 8 μm. By way of further example, in one such embodiment the separator layers 108 will have a thickness of at least about 12 μm. By way of further example, in one such embodiment the separator layers 108 will have a thickness of at least about 15 μm. In some embodiments, the separator layers 108 will have a thickness of up to 25 μm, up to 50 μm, or any other suitable thickness. Typically, however, the separator layers 108 will have a thickness of less than about 12 μm or less than about 10 μm.
In general, the material of the separator layers 108 may be selected from a wide range of material having the capacity to conduct carrier ions between the anodically active material layers 104 and the cathodically active material layers 106 of the multilayer stack 200. For example, the separator layers 108 may comprise a microporous separator material that may be permeated with a liquid, non-aqueous electrolyte. Alternatively, the separator layers 108 may comprise a gel or solid electrolyte capable of conducting carrier ions between the anodically active material layers 104 and the cathodically active material layers 106 of the multilayer stack 200.
In one embodiment, the separator layers 108 may comprise a polymer-based electrolyte. Exemplary polymer electrolytes include PEO-based polymer electrolytes and polymer-ceramic composite electrolytes.
In another embodiment, the separator layers 108 may comprise an oxide-based electrolyte. Exemplary oxide-based electrolytes include lithium lanthanum titanate (Li0.34La0.56TiO3), Al-doped lithium lanthanum zirconate (Li6.24La3Zr2Al0.24O11.98), Ta-doped lithium lanthanum zirconate (Li6.4La3Zr1.4Ta0.6O12), and lithium aluminum titanium phosphate (Li1.4Al0.4Ti1.6(PO4)3).
In another embodiment, the separator layers 108 may comprise a solid electrolyte. Exemplary solid electrolytes include sulfide-based electrolytes such as lithium tin phosphorus sulfide (Li10SnP2S12), lithium phosphorus sulfide (β-Li3PS4), and lithium phosphorus sulfur chloride iodide (Li6PS5Cl0.9I0.1).
In some embodiments, the separator layers 108 may comprise a solid-state lithium ion conducting ceramic, such as a lithium-stuffed garnet.
In one embodiment, the separator layers 108 comprise a microporous separator material comprising a particulate material and a binder, with the microporous separator material having a porosity (void fraction) of at least about 20 vol. %. The pores of the microporous separator material will have a diameter of at least 50 Å and will typically fall within the range of about 250 Å to about 2,500 Å. The microporous separator material will typically have a porosity of less than about 75%. In one embodiment, the microporous separator material has a porosity (void fraction) of at least about 25 vol %. In one embodiment, the microporous separator material will have a porosity of about 35-55%.
The binder for the microporous separator material may be selected from a wide range of inorganic or polymeric materials. For example, in one embodiment, the binder is an organic material selected from the group consisting of silicates, phosphates, aluminates, aluminosilicates, and hydroxides such as magnesium hydroxide, calcium hydroxide, etc. For example, in one embodiment, the binder is a fluoropolymer derived from monomers containing vinylidene fluoride, hexafluoropropylene, tetrafluoropropene, and the like. In another embodiment, the binder is a polyolefin such as polyethylene, polypropylene, or polybutene, having any of a range of varying molecular weights and densities. In another embodiment, the binder is selected from the group consisting of ethylene-diene-propene terpolymer, polystyrene, polymethyl methacrylate, polyethylene glycol, polyvinyl acetate, polyvinyl butyral, polyacetal, and polyethyleneglycol diacrylate. In another embodiment, the binder is selected from the group consisting of methyl cellulose, carboxymethyl cellulose, styrene rubber, butadiene rubber, styrene-butadiene rubber, isoprene rubber, polyacrylamide, polyvinyl ether, polyacrylic acid, polymethacrylic acid, and polyethylene oxide. In another embodiment, the binder is selected from the group consisting of acrylates, styrenes, epoxies, and silicones. In another embodiment, the binder is a copolymer or blend of two or more of the aforementioned polymers.
The particulate material comprised by the microporous separator material may also be selected from a wide range of materials. In general, such materials have a relatively low electronic and ionic conductivity at operating temperatures and do not corrode under the operating voltages of the battery electrode or current collector contacting the microporous separator material. For example, in one embodiment, the particulate material has a conductivity for carrier ions (e.g., lithium) of less than 1×10−4 S/cm. By way of further example, in one embodiment, the particulate material has a conductivity for carrier ions of less than 1×10−5 S/cm. By way of further example, in one embodiment, the particulate material has a conductivity for carrier ions of less than 1×10−6 Siemens/cm (S/cm). Exemplary particulate materials include particulate polyethylene, polypropylene, a TiO2-polymer composite, silica aerogel, fumed silica, silica gel, silica hydrogel, silica xerogel, silica sol, colloidal silica, alumina, titania, magnesia, kaolin, talc, diatomaceous earth, calcium silicate, aluminum silicate, calcium carbonate, magnesium carbonate, or a combination thereof. For example, in one embodiment, the particulate material comprises a particulate oxide or nitride such as TiO2, SiO2, Al2O3, GeO2, B2O3, Bi2O3, BaO, ZnO, ZrO2, BN, Si3N4, and Ge3N4. See, for example, P. Arora and J. Zhang, “Battery Separators” Chemical Reviews 2004, 104, 4419-4462). In one embodiment, the particulate material will have an average particle size of about 20 nm to 2 μm, more typically 200 nm to 1.5 μm. In one embodiment, the particulate material will have an average particle size of about 500 nm to 1 μm.
In an alternative embodiment, the particulate material comprised by the microporous separator material may be bound by techniques such as sintering, binding, curing, etc. while maintaining the void fraction desired for electrolyte ingress to provide the ionic conductivity for the functioning of the battery.
In the secondary battery 100 (see
When a secondary battery is assembled, the amount of carrier ions available for cycling between the anode and the cathode is often initially provided in the cathode, because cathodically active materials, such as lithium cobalt oxide, are relatively stable in ambient air (e.g., they resist oxidation) compared to lithiated anode materials, such as lithiated graphite. When a secondary battery is charged for the first time, the carrier ions are extracted from the cathode and introduced into the anode. As a result, the anode potential is lowered significantly (toward the potential of the carrier ions), and the cathode potential is increased (to become even more positive). These changes in potential may give rise to parasitic reactions on both the cathode and the anode, but sometimes more severely on the anode. For example, a decomposition product comprising lithium (or other carrier ions) and electrolyte components, known as solid electrolyte interphase (SEI), may readily form on the surfaces of carbon anodes. These surfaces or covering layers are carrier ion conductors, which establish an ionic connection between the anode and the electrolyte and prevent the reactions from proceeding any further.
Although formation of the SEI layer is desired for the stability of a half-cell system comprising the anode and the electrolyte, a portion of the carrier ions introduced into the cells via the cathode is irreversibly bound and thus removed from cyclic operation, i.e., from the capacity available to the user. As a result, during the initial discharge, fewer carrier ions are returned to the cathode from the anode than was initially provided by the cathode during the initial charging operation, leading to irreversible capacity loss. During each subsequent charge and discharge cycle, the capacity losses resulting from mechanical and/or electrical degradation to the anode and/or the cathode tend to be much less per cycle, but even the relatively small carrier ion losses per cycle contribute significantly to reductions in energy density and cycle life as the battery ages. In addition, chemical and electrochemical degradation may also occur on the electrodes and cause capacity losses. To compensate for the formation of SEI (or another carrier ion-consuming mechanism such as mechanical and/or electrical degradation of the negative electrode), additional or supplementary carrier ions may be provided from an auxiliary electrode after formation of the battery.
In general, the positive electrode 208 of the secondary battery 100 (e.g., the collective population of the cathode structures 206 in the secondary battery 100) preferably has a reversible coulombic capacity that is matched to the discharge capacity of the negative electrode 209 (e.g., the collective population of the anode structures 207 in the secondary battery 100). Stated differently, the positive electrode 208 of the secondary battery 100 is sized to have a reversible coulombic capacity that corresponds to the discharge capacity of the negative electrode 209 which, in turn, is a function of the negative electrode 209 end of discharge voltage.
In some embodiments, the negative electrode 209 of the secondary battery 100 (e.g., the collective population of the anode structures 207 in the secondary battery 100) is designed to have a reversible coulombic capacity that exceeds the reversible coulombic capacity of the positive electrode 208. For example, in one embodiment a ratio of the reversible coulombic capacity of the negative electrode 209 to the reversible coulombic capacity of the positive electrode 208 is at least 1.2:1, respectively. By way of further example, in one embodiment a ratio of the reversible coulombic capacity of the negative electrode 209 to the reversible coulombic capacity of the positive electrode 208 is at least 1.3:1, respectively. By way of further example, in one embodiment a ratio of the reversible coulombic capacity of the negative electrode 209 to the reversible coulombic capacity of the positive electrode 208 is at least 2:1, respectively. By way of further example, in one embodiment a ratio of the reversible coulombic capacity of the negative electrode 209 to the reversible coulombic capacity of the positive electrode 208 is at least 3:1, respectively. By way of further example, a ratio of the reversible coulombic capacity of the negative electrode 209 to the reversible coulombic capacity of the positive electrode 208 is at least 4:1, respectively. By way of further example, a ratio of the reversible coulombic capacity of the negative electrode 209 to the reversible coulombic capacity of the positive electrode 208 is at least 5:1, respectively. Advantageously, the excess coulombic capacity of the negative electrode 209 provides a source of anodically active material to allow the secondary battery 100 to reversibly operate within a specified voltage that inhibits formation of crystalline phases (incorporating carrier ions) on the negative electrode 209 that reduce cycle-life of the negative electrode 209 as result of cycling.
As previously noted, the formation of SEI during the initial charge/discharge cycle reduces the amount of carrier ions available for reversible cycling. Mechanical and/or electrical degradation of the negative electrode 209 during cycling of the secondary battery 100 may further reduce the amount of carrier ions available for reversible cycling. To compensate for the formation of SEI (or another carrier ion-consuming mechanism such as mechanical and/or electrical degradation of the negative electrode), therefore, additional or supplementary carrier ions may be provided from an auxiliary electrode after formation of the secondary battery 100. In the embodiments of the present disclosure, the auxiliary electrode is used to electrochemically transfer additional carrier ions to the positive electrode 208 and/or the negative electrode 209 of the secondary battery 100 during and/or after formation. In one embodiment, the auxiliary electrode is removed after transferring the additional carrier ions to the secondary battery 100 in order to improve the energy density of the secondary battery in its final form.
Referring to
The auxiliary electrode 502 partially surrounds the secondary battery 100 in the buffer system 500, and contains a source of carrier ions to replenish the lost energy capacity of the secondary battery 100 after formation (i.e., to compensate for the loss of carrier ions upon the formation of SEI and other carrier ion losses in the first charge and/or discharge cycle of the secondary battery 100). In embodiments, the auxiliary electrode 502 may comprise a foil of the carrier ions in metallic form (e.g., a foil of lithium, magnesium, or aluminum), or any of the previously mentioned materials used for the cathodically active material layers 106 and/or the anodically active material layers 104 (see
Referring to
The separator 702 may comprise any of the materials previously described with respect to the separator layer 108 of the secondary battery 100. The separator 702 may be permeated with an electrolyte that serves as a medium to conduct carrier ions from the carrier ion supply layers 706 to the positive electrode 208 of the secondary battery 100 and/or the negative electrode 209 of the secondary battery. The electrolyte may comprise any of the materials previously described with respect to the secondary battery 100.
The separator 702 in this embodiment includes a first surface 802 and a second surface 803 that opposes the first surface 802. The surfaces 802, 803 of the separator 702 form major surfaces for the separator 702 and are disposed in the X-Y plane in
In one embodiment, the width 804 of the separator 702 is about 34 mm. In other embodiments, the width 804 of the separator is about 30 mm, about 35 mm, or another suitable value. In some embodiments, the width 804 of the separator 702 lies in a range of values of about 10 mm to about 200 mm, or some other suitable range that allows the separator to function as described herein.
The separator 702, in one embodiment, has a length 808 that extends in a direction of the X-axis. In an embodiment, the length 808 of the separator 702 is about 72 mm. In other embodiments, the length 808 of the separator 702 is about 65 mm, about 70 mm, about 75 mm, or some other suitable value that allows the separator to function as described herein. In some embodiments, the length 808 of the separator 702 lies in a range of values of about 30 mm to about 200 mm, or some other suitable range of values that allows the separator to function as described herein.
In one embodiment, the separator 702 has a thickness 810 that extends in the direction of the Z-axis. Generally, the thickness 810 is a distance from the first surface 802 of the separator 702 to (and including) the second surface 803 of the separator. In one embodiment, the thickness 810 of the separator 702 is about 0.025 mm. In other embodiments, the thickness 810 of the separator 702 is about 0.015 mm, about 0.02 mm, about 0.03 mm, about 0.035 mm, or some other suitable value. In some embodiments, the thickness 810 of the separator 702 lies in a range of values of about 0.01 mm to about 1.0 mm, or some other suitable range of values that allows the separator to function as described herein.
The conductive layer 704 is electrically conductive, and may comprise a metal, a metalized film, an insulating base material with a conductive material applied thereto, or some other type of electrically conductive material. In some embodiments, the conductive layer 704 comprises copper. In other embodiments, the conductive layer 704 comprises aluminum or another metal. In this embodiment, the conductive layer 704 is electrically coupled with the conductive tab 508-2, which is also electrically conductive. The conductive tab 508-2 has a first end 812 disposed proximate to the conductive layer 704 and a second end 813 disposed distal to the conductive layer 704 that opposes the first end 812. The first end 812 of the conductive tab 508-2 is electrically coupled to the conductive layer 704. In some embodiments, the first end 812 of the conductive tab 508-2 is spot-welded to the conductive layer 704. In other embodiments, the first end 812 of the conductive tab 508-2 is soldered to the conductive layer 704. Generally, the conductive tab 508-2 may be affixed at the first end 812 to the conductive layer 704 using any suitable means that ensure a mechanical connection and an electrical connection to the conductive layer. The conductive tab 508-2 may comprise any type of electrically conductive material as desired. In one embodiment, the conductive tab 508-2 comprises a metal. In these embodiments, the conductive tab 508-2 may comprise nickel, copper, aluminum, or other suitable metals or metal alloys that allows the conductive tab 508-2 to function as described herein.
The conductive layer 704 in this embodiment includes a first surface 814 and a second surface 815 that opposes the first surface 814. The surfaces 814, 815 of the conductive layer 704 form major surfaces for the conductive layer and are disposed in the X-Y plane in
In some embodiments, the width 816 of the conductive layer 704 lies in a range of values of about 5 mm to about 100 mm, or some other suitable range of values that allows the conductive layer to function as described herein. The first surface 814 of the conductive layer 704 in this embodiment is segmented into a first region 818-1, disposed proximate to a first end 820 of the conductive layer 704, a second region 818-2, disposed proximate to a second end 821 of the conductive layer 704, and a third region 818-3 disposed between the first region 818-1 and the second region 818-2.
The conductive layer 704 has a length 822 that extends in a direction of the X-axis. In one embodiment, the length 822 of the conductive layer 704 is about 70 mm. In other embodiments, the length 822 of the conductive layer 704 is about 60 mm, about 65 mm, about 75 mm, or some other suitable value that allows the conductive layer 704 to function as described herein. In some embodiments, the length 822 of the conductive layer 704 lies in a range of values of about 30 mm to about 200 mm, or some other suitable range of values that allows the conductive layer to function as described herein.
The conductive layer 704 has a thickness 824 that extends in a direction of the Z-axis. Generally, the thickness 824 is a distance from the first surface 814 of the conductive layer 704 to (and including) the second surface 815 of the conductive layer 704. In one embodiment, the thickness 824 of the conductive layer 704 is about 0.1 mm. In other embodiments, the thickness 824 of the conductive layer 704 is about 0.005 mm, about 0.15 mm, or about 0.2 mm. In some embodiments, the thickness 824 of the conductive layer 704 lies in a range of values of about 0.01 mm to about 1.0 mm, or any other suitable range for the thickness that allows the conductive layer to function as described herein.
The carrier ion supply layers 706, which comprise a population of carrier ion supply layers in an embodiment, comprise any carrier ion containing material previously described that may be utilized to supply carrier ions to the positive electrode 208 and/or the negative electrode 209 of the secondary battery 100. The carrier ion supply layers 706 may comprise one or more sources of lithium ions, sodium ions, potassium ions, calcium ions, magnesium ions, and aluminum ions. In this embodiment, the carrier ion supply layers 706 are disposed within the first region 818-1 and the second region 818-2 of the conductive layer 704. In some embodiments, the carrier ion supply layers 706 are also disposed in the third region 818-3 of the conductive layer 704.
The carrier ion supply layers 706 in this embodiment include a first surface 826 and a second surface 827 that opposes the first surface 826. The surfaces 826, 827 of the carrier ion supply layers 706 form major surfaces for the carrier ion supply layers and are disposed in the X-Y plane in
The carrier ion supply layers 706, in one embodiment, have a length 830 that extends in a direction of the X-axis. In an embodiment, the length 830 of the carrier ion supply layers 706 are about 23 mm. In other embodiments, the length 830 of the carrier ion supply layers 706 are about 15 mm, about 20 mm, about 25 mm, or some other suitable length that allows the carrier ion supply layers to function as described herein. In some embodiments, the length 830 of the carrier ion supply layers 706 lie in a range of values of about 10 mm to about 100 mm, or some other suitable range of values that allow the carrier ion supply layers to function as described herein.
The carrier ion supply layers 706 each have a thickness 832 that extends in a direction of the Z-axis. Generally, the thickness 832 is a distance between the first surface 826 of the carrier ion supply layers 706 and the second surface 827 of the carrier ion supply layers. In one embodiment, the thickness 832 of the carrier ion supply layers 706 are about 0.13 mm. In other embodiments, the thickness 832 of the carrier ion supply layers 706 are about 0.005 mm, about 0.15 mm, or about 0.2 mm. In some embodiments, the thickness 832 of the carrier ion supply layers 706 lie in a range of values of about 0.01 mm to about 1.0 mm, or any other suitable range of values for the thickness that allows the carrier ion supply layers to function as described herein.
In this embodiment, the carrier ion supply layers 706 are separated from each other by a distance 834, corresponding to the third region 818-3. In one embodiment, the distance 834 is about 23 mm. In other embodiments, the distance 834 is about 15 mm, about 20 mm, about 25 mm, or about 30 mm. In some embodiments, the distance 834 lies in a range of values of about 10 mm to about 50 mm, or any other suitable range of values that allows the carrier ion supply layers 706 to function as described herein.
In one embodiment, the carrier ion supply layers 706 are sized to be capable of providing at least 15% of the reversible coulombic capacity of the positive electrode 208 of the secondary battery 100. For example, in one such embodiment, the carrier ion supply layers 706 are sized such that they contain sufficient carrier ions (e.g., lithium, magnesium, or aluminum ions) to provide at least 30% of the reversible coulombic capacity of the positive electrode 208 of the secondary battery 100. By way of further example, in one such embodiment, the carrier ion supply layers 706 are sized such that they contain sufficient carrier ions to provide at least 100% of the reversible coulombic capacity of the positive electrode 208 of the secondary battery 100. By way of further example, in one such embodiment, the carrier ion supply layers 706 are sized such that they contain sufficient carrier ions to provide at least 200% of the reversible coulombic capacity of the positive electrode 208 of the secondary battery 100. By way of further example, in one such embodiment, the carrier ion supply layers 706 are sized such that they contain sufficient carrier ions to provide at least 300% of the reversible coulombic capacity of the positive electrode 208 of the secondary battery 100. By way of further example, in one such embodiment, the carrier ion supply layers 706 are sized such that they contain sufficient carrier ions to provide about 100% to about 200% of the reversible coulombic capacity of the positive electrode 208 of the secondary battery 100.
During an assembly process for the auxiliary electrode 502, the separator 702 may be cut from stock material or prefabricated to achieve the width 804 and the length 808 as shown in
In other embodiments, the conductive layer 704 is prefabricated to include the carrier ion supply layers 706 arranged in the orientation depicted in
To continue the fabrication process of the auxiliary electrode 502, in one embodiment, the second portion 806 of the separator 702 is folded in the direction of an arrow 902 towards the left (about an axis parallel to the X-axis) in
In one embodiment, the separator 702 is bonded to itself along at least a portion of an outer perimeter 1002 of the separator using a hot melt process, a welding process, a bonding process, etc. In
In response to fabricating the auxiliary electrode 502, performing a fabrication process for the buffer system 500 (see
With the auxiliary electrode 502 oriented within the pouch 514 as depicted in
With the secondary battery 100 loaded onto the second region 818-2 of the auxiliary electrode 502 within the pouch 514, the auxiliary electrode 502 is folded in the direction of an arrow 1302 in order to position the first side 1004 of the first region 818-1 of the auxiliary electrode 502 in contact with the second major surface 127 of the secondary battery 100, the result of which is depicted in
With the secondary battery 100 sandwiched by the auxiliary electrode 502 within the pouch 514 as illustrated in
With the secondary battery 100 and the carrier ion supply layers 706 of the auxiliary electrode 502 (not visible in
Either prior to inserting the secondary battery 100 into the buffer system 500, or after, the secondary battery 100 is charged (e.g., via the electrical terminals 124, 125) by transferring carrier ions from the cathode structures 206 of the secondary battery to the anode structures 207 of the secondary battery. Charging may be discontinued when the positive electrode 208 of the secondary battery 100 reaches its the end-of-charge design voltage. During the initial charging cycle, SEI may form on the surfaces of the anode structures 207 of the secondary battery 100. To compensate for the loss of carrier ions to SEI, and to further provide additional carrier ions to mitigate the long term secondary reactions during cycling where carrier ions are lost due to side reactions, the positive electrode 208 and/or the negative electrode 209 of the secondary battery 100 may be replenished by applying a voltage across the auxiliary electrode 502 and the cathode structures 206 and/or the anode structures 207 (e.g., via the conductive tab 508-1 of the auxiliary electrode 502 and one of the electrical terminals 124, 125) to drive carrier ions from the carrier ion supply layers 706 of the auxiliary electrode 502 to the cathode structures 206 and/or the anode structures 207 of the secondary battery 100. Once the transfer of carrier ions from the auxiliary electrode 502 to the secondary battery 100 is complete, the negative electrode 209 of the secondary battery is again charged, this time with carrier ions transferred from the cathode structures 206 of the secondary battery 100 to the anode structures 207 of the secondary battery.
In one embodiment, the amount of carrier ions transferred from the auxiliary electrode 502 to the secondary battery 100 during the buffer process is about 50% of the reversable columbic capacity of the positive electrode 208 of the secondary battery. In other embodiments, the amount of carrier ions transferred from the auxiliary electrode 502 to the secondary battery 100 during the buffer process is about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 90%, about 95%, or about 100% of the reversable columbic capacity of the positive electrode 208 of the secondary battery. In some embodiments, the amount of carrier ions transferred from the auxiliary electrode 502 to the secondary battery 100 lies in a range of values of about 1% to about 100% of the reversable columbic capacity of the positive electrode 208 of the secondary battery. In one particular embodiment, the negative electrode 209 of the secondary battery 100 has about 170% of the reversable columbic capacity of the positive electrode 208 of the secondary battery stored as carrier ions when the secondary battery is charged, and about 70% of the reversable columbic capacity of the positive electrode 208 of the secondary battery stored as carrier ions when the secondary battery is discharged. An excess of carrier ions at the negative electrode 209 of the secondary battery 100 provided during the buffer process provides a technical benefit of mitigating the loss of carrier ions at the secondary battery due to SEI at initial formation. Further, an excess of carrier ions at the negative electrode 209 of the secondary battery 100 provided during the buffer process provides a technical benefit of mitigating the loss of carrier ions at the secondary battery due to side reactions that deplete carrier ions in the secondary battery as the secondary battery is cycled during use, which reduces the capacity loss of the secondary battery over time.
In some embodiments, transferring carrier ions from the auxiliary electrode 502 to the secondary battery 100 may occur concurrently with an initial formation of the secondary battery (e.g., during the first charge of the secondary battery), and/or during a subsequent charge of the secondary battery after initial formation. In these embodiments, carrier ions are transferred from the positive electrode 208 of the secondary battery 100 to the negative electrode 209 of the secondary battery. Concurrently with or based on a temporal delay or a temporal pattern, carrier ions are transferred from the auxiliary electrode 502 to the positive electrode 208 and/or the negative electrode 209 of the secondary battery 100.
In yet another embodiment, the positive electrode 208 may be replenished with carrier ions by simultaneously transferring carrier ions from the auxiliary electrode 502 to the positive electrode 208 of the secondary battery 100, while also transferring carrier ions from the positive electrode of the secondary battery to the negative electrode 209 of the secondary battery. Referring to
In one embodiment, without being limited by any particular theory, the carrier ions are transferred from the auxiliary electrode 502 to the positive electrode 208 of the secondary battery 100 as a part of the replenishment of the negative electrode 209 of the secondary battery (as opposed to transferring from the auxiliary electrode directly to the negative electrode of the secondary battery), because the positive electrode may be capable of more uniformly accepting carrier ions across the surface thereof, thus allowing the carrier ions to more uniformly participate in the transfer thereof between the positive electrode and the negative electrode of the secondary battery.
After the buffer process is performed on the secondary battery 100 utilizing the buffer system 500, the auxiliary electrode 502 may be removed from the buffer system in order to improve the energy density of the secondary battery 100 in its final form. For example, after the buffer process, the carrier ion supply layers 706 (see
In this embodiment, the secondary battery 100 (see
The auxiliary electrode 502 (see
The auxiliary subassembly 516 is installed in the enclosure 504, where the electrical terminals 124, 125 of the secondary battery 100 and the electrically conductive tab 508 of the auxiliary electrode 502 electrically extend from the perimeter 506 of enclosure 504 (see step 1804, and
Carrier ions are transferred from the positive electrode 208 of the secondary battery 100 to the negative electrode 209 of the secondary battery to at least partially charge the secondary battery by applying a potential voltage across the electrical terminals 124, 125 (see step 1806). Charging may be discontinued when the positive electrode 208 of the secondary battery 100 reaches its the end-of-charge design voltage. During the initial charging cycle, SEI may form on the internal structural surfaces of the negative electrode 209 of the secondary battery 100.
To compensate for the loss of carrier ions to SEI, and to further provide additional carrier ions to mitigate the long term secondary reactions during cycling where carrier ions are lost due to side reactions, carrier ions are transferred from the carrier ion supply layers 706 of the auxiliary electrode 502 to the positive electrode 208 and/or the negative electrode 209 of the secondary battery 100 by applying a potential voltage across the electrically conductive tab 508 of the auxiliary electrode 502 and one or more of the electrical terminals 124, 125 of the secondary battery (see step 1808,
In one embodiment, the amount of carrier ions transferred from the auxiliary electrode 502 to the secondary battery 100 is about 50% of the reversable columbic capacity of the positive electrode 208 of the secondary battery. In other embodiments, the amount of carrier ions transferred from the auxiliary electrode 502 to the secondary battery 100 is about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 90%, about 95%, or about 100% of the reversable columbic capacity of the positive electrode 208 of the secondary battery. In some embodiments, the amount of carrier ions transferred from the auxiliary electrode 502 to the secondary battery 100 lies in a range of values of about 1% to about 100% of the reversable columbic capacity of the positive electrode 208 of the secondary battery. In one particular embodiment, the negative electrode 209 of the secondary battery 100 has about 170% of the reversable columbic capacity of the positive electrode 208 of the secondary battery stored as carrier ions when the secondary battery is charged, and about 70% of the reversable columbic capacity of the positive electrode 208 of the secondary battery stored as carrier ions when the secondary battery is discharged. An excess of carrier ions at the negative electrode 209 of the secondary battery 100 provided during the buffer process provides a technical benefit of mitigating the loss of carrier ions at the secondary battery due to SEI at initial formation. Further, an excess of carrier ions at the negative electrode 209 of the secondary battery 100 provided during the buffer process provides a technical benefit of mitigating the loss of carrier ions at the secondary battery due to side reactions that deplete carrier ions in the secondary battery as the secondary battery is cycled during use, which reduces the capacity loss of the secondary battery over time.
In some embodiments, transferring carrier ions from the auxiliary electrode 502 to the secondary battery 100 may occur concurrently with an initial formation of the secondary battery (e.g., during the first charge of the secondary battery), and/or during a subsequent charge of the secondary battery after initial formation. In these embodiments, carrier ions are transferred from the positive electrode 208 of the secondary battery 100 to the negative electrode 209 of the secondary battery. Concurrently with or based on a temporal delay or a temporal pattern, carrier ions are transferred from the auxiliary electrode 502 to the positive electrode 208 and/or the negative electrode 209 of the secondary battery 100.
Carrier ions are again transferred from the positive electrode 208 of the secondary battery 100 to the negative electrode 209 of the secondary battery to charge the secondary battery by applying a potential voltage across the electrical terminals 124, 125 of the secondary battery until the negative electrode 209 has greater than 100% of the positive electrode 208 coulombic capacity stored as the carrier ions (see step 1810).
In yet another embodiment, the positive electrode 208 may be replenished with carrier ions by simultaneously transferring carrier ions from the auxiliary electrode 502 to the positive electrode 208 of the secondary battery 100, while also transferring carrier ions from the positive electrode 208 of the secondary battery to the negative electrode 209 of the secondary battery. Referring to
In one embodiment, without being limited by any particular theory, the carrier ions are transferred from the auxiliary electrode 502 to the positive electrode 208 of the secondary battery 100 as a part of the replenishment of the negative electrode 209 of the secondary battery (as opposed to transferring from the auxiliary electrode 502 directly to the negative electrode of the secondary battery), because the positive electrode may be capable of more uniformly accepting carrier ions across the surface thereof, thus allowing the carrier ions to more uniformly participate in the transfer thereof between the positive electrode and the negative electrode of the secondary battery.
In some embodiments of the method 1800, the enclosure 504 is opened (see step 1902 of
Although installing the auxiliary subassembly 516 in the enclosure 504 as previously described with respect to step 1804 detailed above, one particular embodiment comprises installing the auxiliary subassembly 516 on the first enclosure layer 510 (see step 2002 of
The enclosure layers 510, 511 may be sealed along the sealing line 1602 (see
In embodiments where the first enclosure layer 510 includes the pouch 514, installing the auxiliary subassembly 516 within the enclosure 504 initially comprises placing the auxiliary subassembly 516 within the pouch 514 (see step 2102 of
In some embodiments, one or more steps of the formation process performed on the secondary battery 100 discussed above may be performed using a battery tray and a formation base removably attachable to the battery tray.
The battery tray 2202 includes battery slots 2212 and a first assembly connector 2213. Each battery slot 2212 is configured (e.g., sized and shaped) to receive and retain a secondary battery 100. In the example embodiment, each battery slot 2212 is configured to receive only one secondary battery 100, but in other embodiments, each battery slot may be configured to receive more than one battery. In one example embodiment, the battery tray 2202 includes one hundred and twenty battery slots 2212 arranged in three rows of forty battery slots. Other embodiments include more or fewer battery slots 2212 arranged in more or fewer rows. Openings are defined in a bottom of the battery tray 2202 at locations corresponding to the battery slots 2212 to allow the first terminal 124, the second terminal 125, and the conductive tab 508-1 to extend through the bottom of the battery tray when a secondary battery 100 is positioned in a battery slot 2212.
The formation base 2204 is sized and shaped similar to the battery tray 2202, and is configured for removable attachment to the battery tray. The formation base 2204 includes connector groups 2214, pre-lithiation modules 2216, and a second assembly connector 2218. Each connector group 2214 is configured for making electrical connection to the conductive tab 508-1, and one of the first terminal 124 and the second terminal 125 of a different secondary battery 100 when the battery tray 2202 with the secondary battery loaded therein is attached to the formation base. The one of the first terminal 124 and the second terminal 125 of a different secondary battery 100 to which the connector group 2214 connects is the cathodic terminal. In other embodiments, each connector group 2214 is configured for making electrical connection to the conductive tab 508-1, the first terminal 124, and the second terminal 125 of a different secondary battery 100 when the battery tray 2202 with the secondary battery loaded therein is attached to the formation base 2204.
Each pre-lithiation module 2216 is electrically connected to a different one of the connector groups 2214, and is configured to diffuse lithium to the electrode active materials of the secondary battery 100 connected to the connector group 2214 to which the pre-lithiation module 2216 is electrically connected. In other embodiments, each pre-lithiation module 2216 is electrically connected to more than one of the connector groups 2214, and is configured to diffuse lithium to the electrode active materials of the secondary batteries 100 connected to the more than one connector group 2214 to which the pre-lithiation module 2216 is electrically connected. In an example embodiment, the pre-lithiation modules 2216 are current sink-based pre-lithiation modules as described below. In another example, the pre-lithiation modules 2216 are switched capacitor circuits. In another example, the pre-lithiation modules 2216 include a resistor to be electrically connected between the conductive tab 508-1, and one of the first terminal 124 and the second terminal 125, and a circuit which interrupts the connection when the voltage drops to 1.5V (indicating the completion of the buffer process). Other embodiments include any other suitable pre-lithiation module. In some embodiments, each pre-lithiation module 2216 is separate from each other pre-lithiation module 2216, while in other embodiments, two or more pre-lithiation modules 2216 are integrated in a common circuit or mounted on a common support (such as rigid circuit board, a flexible circuit board, or other suitable support).
The second assembly connector 2218 is configured to matingly engage with the first assembly connector 2213 to mechanically connect the battery tray 2202 to the formation base 2204. In one example embodiment, the first assembly connector 2213 is a rectangular opening through the bottom of the battery tray 2202, and the second assembly connector 2218 is a rotatable t-shaped connector extending from the formation base 2204. In a first orientation, the second assembly connector 2218 may pass through the rectangular opening of the first assembly connector 2213 to allow the battery tray 2202 to be placed into position on the formation base 2204. When the second assembly connector 2218 is rotated to a second position (e.g., ninety degrees from the first position), the second assembly connector 2218 cannot pass through the rectangular opening of the first assembly connector 2213. Thus, after the battery tray 2202 is placed into position on the formation base 2204, the second assembly connector 2218 is rotated to the second position to lock the battery tray 2202 and the formation base 2204 together into the formation assembly 2209. Other embodiments may use other connection systems as the first and second assembly connectors 2213, 2218.
The loading station 2206, the charging station 2208, and the formation station 2210 are stations for loading batteries 100 into the battery tray 2202, charging batteries in the battery tray, and buffering batteries in the formation assembly 2209, respectively. At the loading station 2206, secondary batteries 100 are typically loaded into the battery tray 2202 by a robotic loader (not shown). In other embodiments, secondary batteries 100 are loaded into the battery tray 2202 by a human operator. The charging station 2208 is configured to receive the battery tray 2202 loaded with secondary batteries 100, and to store the loaded battery tray and charge the batteries 100 in the battery tray. The formation station 2210 is configured to receive the formation assembly 2209 including the battery tray 2202 loaded with charged secondary batteries 100, and to store the formation assembly while lithium is diffused to the electrode active materials of the secondary batteries in the battery tray by the pre-lithiation modules 2216. Some embodiments also include a mounting station (not shown) at which the battery tray 2202 is mounted to the formation base 2204. The battery tray 2202 and the formation assembly 2209 may travel between the loading station 2206, the charging station 2208, the formation station 2210, and the mounting station on a conveyer belt or any other suitable conveyance system.
The charging station 2208 includes a rack or shelving system to store the battery tray 2202, as well as electrical connections for providing power to the battery tray to charge the secondary batteries 100 in the battery tray. In some embodiments, the charging station includes charging circuitry to control the charging of the secondary batteries 100, while in other embodiments, the charging circuitry is included in the battery tray 2202 or the formation base 2204. In some embodiments, the charging station 2208 also includes communications connections to allow one or more remote computing devices to control and/or monitor charging of secondary batteries 100 at the charging station 2208.
The formation station 2210 includes a rack or shelving system to store the formation assembly 2209, as well as electrical connections for providing power for the formation process. In some embodiments, the formation station 2210 also includes communications connections to allow one or more remote computing devices to control and/or monitor the formation process at the formation station 2210.
In
One example method of cell formation using the cell formation system 2200 will be described below. It should be understood that the cell formation system 2200 may be used for other methods of cell formation as well.
First, a population of lithium based secondary batteries 100 are loaded into the battery tray 2202. Each battery 100 is loaded into a different battery slot 2212 with the conductive tab 508-1, the first terminal 124, and the second terminal 125 extending through the base 2302 of the battery tray to a position accessible from a bottom side of the base of the battery tray. The battery tray 2202 is then transported to the charging station 2208, where the lithium based secondary batteries 100 in the battery tray are charged. The battery tray 2202 is removed from the charging station 2208 and the formation base 2204 is attached to the battery tray from the bottom side of the base 2302 of the battery tray to form the formation assembly 2209. The formation assembly 2209 is transported to the formation station 2210, and the lithium based secondary batteries 100 in the formation assembly 2209 are pre-lithiated using the pre-lithiation modules 2216. The formation base 2204 is removed from the battery tray 2202 after pre-lithiation is complete. One or more additional processes may be performed on the lithium based secondary batteries 100 in the battery tray 2202. The formation base 2204 is returned for re-use while the additional processes are performed. Thus, an additional population of lithium based secondary batteries 100 may be loaded into an additional battery tray 2202, and the process above may be repeated with the additional battery tray 2202 and the formation base 2204.
In some embodiments, the formation process is performed by a distributed formation system (which may include the cell formation system 2200), in which each secondary battery 100 is connected to a separate formation cluster that performs the formation process for the secondary battery 100 to which it is connected. In embodiments using the cell formation system 2200, the separate formation cluster for each secondary battery 100 may be included in the formation base 2204. In such embodiments, charging and discharging may occur with the formation base 2204 attached to the battery tray, or may occur in the battery tray without the formation base 2204 attached (e.g., the charging module and discharging modules may be in the battery tray and the pre-lithiation module may be in the formation base).
The formation clusters 3002 are communicatively coupled to the central controller 3004 by a network 3006. The network 3006 may be a wired or a wireless network of any type suitable for communication between the formation clusters 3002 and the central controller 3004. For example, the network 3006 may be an inter-integrated circuit (I2C) network, a controller area network (CAN), a local area network (LAN), a wide area network (WAN), or the like. Although shown connected to the same network 3006 in
Each formation cluster 3002 is connected to a power source 3008, such as an electrical grid, a generator, a photovoltaic system, a battery, or the like. The formation clusters 3002 use electrical power from the power source 3008 to power the formation cluster and to perform the formation process. Although illustrated connected to the same power source 3008 in
Groups of formation clusters 3002 are supported by a housing 3010. The housing 3010 may be an enclosure, such as a cabinet, or an open support, such as a rack. Although two formation clusters 3002 are shown in one housing 3010, and a single formation cluster 3002 is shown in another housing for simplicity, in practice each housing 3010 will typically support a larger number of formation clusters, such as 10, 25, 50, 100, 250, or a 1000 formation clusters. Notably, the central controller 3004 is separate from (and may be remotely located from) the housings 3010 and their formation clusters 3002. Moreover, the housings 3010 may be located in different locations from each other, so long as they are located somewhere with access to the power source 3008 and the network 3006. Further, each housing 3010 may support a different number of formation clusters 3002.
The battery connector 3100 connects the formation cluster 3002 to the secondary battery 100. The battery connector 3100 may be any connector suitable for connection to the secondary battery 100, including a connector configured to mate with a similar connector on the battery, a clamping connector (such as an alligator clip), a wire soldered or welded to the secondary battery and the formation cluster 3002, and the like. The battery connector 3100 is configured to connect to the anode and the cathode of the secondary battery 100. In some embodiments, the battery connector 3100 also electrically connects the formation cluster 3002 to the auxiliary electrode 502. In other embodiments, the formation cluster 3002 includes a separate connector, referred to as a pre-lithiation connector, that electrically connects the formation cluster 3002 to the auxiliary electrode 502. In some embodiments, the formation cluster 3002 includes more than one battery connector 3100, with each battery connector connected to a separate one of the modules of the formation cluster (e.g., the charging module 3102, the pre-lithiation module 3104, and the discharging module 3106).
The charging module 3102 is connected to the battery connector 3100 and is configured to charge the secondary battery 100 connected to the battery connector 3100. The pre-lithiation module 3104 is connected to the battery connector 3100 and configured to diffuse lithium carrier ions to the electrode active material layers (e.g., the cathodically active material layers 106 and/or the anodically active material layers 104) of the secondary battery 100. The discharging module 3106 is connected to the battery connector 3100 and is configured to discharge the secondary battery 100.
The communication interface 3108 connects the formation cluster 3002 to the central controller 3004. The communication interface 3108 may be any wired or wireless communications interface that permits the controller 3110 to communicate with the central controller 3004 directly or via a network. Wireless communication interfaces 3108 may include a radio frequency (RF) transceiver, a Bluetooth® adapter, a Wi-Fi transceiver, a ZigBee® transceiver, an infrared (IR) transceiver, and/or any other device and communication protocol for wireless communication. (Bluetooth is a registered trademark of Bluetooth Special Interest Group of Kirkland, Washington; ZigBee is a registered trademark of the ZigBee Alliance of San Ramon, California.) Wired communication interfaces 3108 may use any suitable wired communication protocol for direct communication including, without limitation, USB, RS232, I2C, SPI, analog, and proprietary I/O protocols. In some embodiments, the wired communication interface 3108 includes a wired network adapter allowing the controller 3110 to be coupled to a network, such as the Internet, a local area network (LAN), a wide area network (WAN), a mesh network, and/or any other network to communicate with remote devices and systems via the network.
The formation cluster controller 3110 controls the operation of the formation cluster 3002 to operate as described herein. The formation cluster controller 3110 includes a processor 3116 and a memory 3118. The processor 3116 is any programmable system including a microcontroller, microcomputer, microprocessor, reduced instruction set circuit (RISC), application specific integrated circuit (ASIC), programmable logic circuit (PLC), and any other circuit or processor capable of executing the functions described herein. The memory 3118 stores computer-readable instructions executable by the processor 3116 for control of the formation cluster 3002 as described herein. The memory 3118 may be any suitable type of memory including, but not limited to, random access memory (RAM) such as dynamic RAM (DRAM) or static RAM (SRAM), read-only memory (ROM), erasable programmable read-only memory (EPROM), electrically erasable programmable read-only memory (EEPROM), and non-volatile RAM (NVRAM). In some embodiments, the processor 3116 and the memory 3118 are both embodied in a microcontroller, while in other embodiments the processor 3116 and the memory 3118 are separate components.
In the example embodiment, the formation cluster controller 3110 is programmed (by instruction stored in the memory 3118) to directly control each of the modules 3102, 3104, and 3106. That is, the formation cluster controller 3110 is programmed to control the charging module to charge the secondary battery 100, to control the pre-lithiation module 3104 to pre-lithiate (also referred to as buffering) the secondary battery 100, and to control the discharging module 3106 to discharge the secondary battery 100. The formation cluster controller 3110 is also programmed to control the overall formation process, such as when to use each of the modules 3102, 3104, and 3106.
In other embodiments one or more of the modules 3102, 3104, and 3106 includes its own module controller (having a processor and memory). In such embodiments, the formation cluster controller 3110 controls the overall formation process, but the module controllers control the specific tasks of their modules. For example, the formation cluster controller 3110 may instruct the charging module 3102 to charge the secondary battery 100, and the module controller in the charging module will then control the charging module to charge the secondary battery 100 according to instructions stored in the memory of the charging module's module controller.
In further embodiments, the formation cluster 3002 does not include the formation cluster controller 3110. Rather, each of the modules 3102, 3104, and 3106 includes its own module controller. In such embodiments, the central controller 3004 controls the overall formation process and sends instructions to the module controllers through the communication interface 3108. In such embodiments, the multiple module controllers in the formation cluster 3002 may be considered as a distributed formation cluster controller 3110.
Various levels of interaction and control may be performed by the central controller 3004 and the formation cluster controller 3110 in different embodiments. For example, in some embodiments, the central controller 3004 merely sends instructions to the formation cluster 3002 to begin the formation process. Then, in response to the instructions, the formation cluster controller 3110 controls the modules 3102, 3104, 3106 to perform the formation process. Alternatively, in response to the instructions, the formation cluster controller 3110, may instruct the modules 3102, 3104, 3106 to perform their respective functions at the appropriate times. In other embodiments, the central controller 3004 sends instructions to the formation clusters 3002 to perform an individual portion of the formation process (e.g., “charge the battery now”), and the formation cluster controller 3110 or the module controllers perform the task commanded by the central controller. In some embodiments, the central controller 3004 may send instructions to the formation clusters 3002 for how to perform one or more of the formation tasks, including sending control algorithms. In some embodiments, the formation cluster controller 3110 or the module controller may store instructions for multiple ways of performing the same task (e.g., a fast charge, a slow charge, a charge with a rest period, and the like), and the central controller's instructions may instruct the formation cluster 3002 which method to use.
In some embodiments, the central controller 3004 may program or update the programming of the formation cluster controller 3110 or the module controllers. For example, the central controller 3004 may send control algorithms to the formation cluster 3002, and the formation cluster controller 3110 and/or the module controllers may store the control algorithms in their respective memories. In other embodiments, the central controller may send a modification of a control algorithm already stored in the formation cluster, such as a change to a variable, a change in timing, or the like. The formation cluster controller 3110 or the controller modules then store the modification in memory for use in the formation process.
The formation cluster controller 3110 also transmits information back to the central controller 3004 in some embodiments. The information sent to the central controller 3004 may include confirmation that instructions were received, confirmation that a commanded process has begun, status of the operations being performed, data collected from the sensor 3114, or any other suitable information.
The power connection 3112 connects the formation cluster 3002 to the power source 3008. The power connection 3112 may be any connector suitable for connection to the power source 3008, including a plug configured for insertion into a mating socket of the power source, a wire soldered or welded to the power source, a clamping connector for clamping onto a terminal or wire of the power source, or the like. The PSU 3113 converts and/or distributes power from the power source to the rest of the formation cluster 3002 for use in the formation process. The PSU 3113 may be an AC/DC power converter, a DC/DC power converter, an inverter, or any other unit for suitable for converting and/or distributing power to the formation cluster. Some embodiments do not include a PSU, and utilize power from the power source 3008 directly.
The sensor 3114 is any sensor capable of monitoring a variable of interest to the formation process. For example, the sensor 3114 may be a voltage sensor for monitoring the voltage of the secondary battery 100, an ambient temperature sensor for monitoring the temperature around the formation cluster 3002, a temperature sensor for monitoring the temperature of the battery secondary or a component of the formation cluster, a current sensor for monitoring current flowing into, out of, or through the secondary, etc. Some embodiments include more than one sensor 3114, including combinations of the sensors described above. Moreover, some sensors 3114 may perform more than one of the above-described monitoring tasks.
The modular and distributed nature of the cell formation system 3000 allows for the system to be easily expanded or contracted as desired. Unlike traditional centralized systems that are configured for formation of a set number of batteries at one time, the system 3000 may be expanded to any number of batteries simply by adding more formation clusters 3002 (including increasing the number of batteries by as few as one additional battery). With a traditional centralized system, increases to the number of batteries to be formed would require acquisition of an additional system and an increase by some set number of batteries (determined by the size and configuration of the centralized system acquired). Further, centralized systems typically require running significant additional wiring for each additional battery in order to provide controlled power and communication to the additional batteries. In contrast, the cell formation system 3000 merely requires connecting additional formation clusters 3002 to a power source and an already existing communication network. The formation clusters 3002 in the system 3000 need not all be the same, so long as the central controller 3004 knows the configuration of each formation cluster 3002. Moreover, the formation clusters 3002 in the system 3000 may be used to form different batteries, either at different times or at the same time, so long as the central controller 3004 or the formation cluster controller 3110 knows what secondary battery 100 is connected to the formation cluster 3002.
The current sink 3200 is controlled by the pre-lithiation module controller 3202 to selectively conduct current between the auxiliary electrode 502 and one of the electrodes (e.g., one of the positive electrode 208 and the negative electrode 209) of the secondary battery 100 to diffuse lithium from the auxiliary electrode to the electrode active material layers (e.g., the cathodically active material layers 106 or the anodically active material layers 104) of the secondary battery 100. In an example embodiment, the current sink 3200 is a linear current regulator. In other embodiments, any other suitable controllable current sink may be used as the current sink 3200.
The pre-lithiation module controller 3202 controls operation of the pre-lithiation module 3104 pre-lithiate the secondary battery 100 by selectively conducting current through the auxiliary electrode 502 to diffuse lithium to the electrode active material layers of the secondary battery. The pre-lithiation module controller 3202 includes a processor 3210 and a memory 3212. The memory 3212 stores instructions that, when executed by the processor 3210 cause the processor to perform the pre-lithiation as described herein. The processor 3210 is any programmable system including a microcontroller, microcomputer, microprocessor, reduced instruction set circuit (RISC), application specific integrated circuit (ASIC), programmable logic circuit (PLC), field-programmable gate array (FPGA), and any other circuit or processor capable of executing the functions described herein. The memory 3212 may be any suitable type of memory including, but not limited to, random access memory (RAM) such as dynamic RAM (DRAM) or static RAM (SRAM), read-only memory (ROM), erasable programmable read-only memory (EPROM), electrically erasable programmable read-only memory (EEPROM), and non-volatile RAM (NVRAM). In some embodiments, the processor 3210 and the memory 3212 are both embodied in a microcontroller, while in other embodiments the processor and the memory are separate components.
The battery connector 3204 connects the pre-lithiation module 3104 to the secondary battery 100. The battery connector 3204 may be the battery connector 3100 or may be a separate battery connector connected only to the pre-lithiation module 3104. The battery connector 3204 may be any connector suitable for connection to the secondary battery 100, including a connector configured to mate with a similar connector on the secondary battery, a clamping connector (such as an alligator clip), a wire soldered or welded to the secondary battery and the pre-lithiation module 3104, and the like. The battery connector 3204 is configured to connect to the anode (e.g., the negative electrode 209) and the cathode (e.g., the positive electrode 208) of the secondary battery 100.
The pre-lithiation connector 3206 connects the pre-lithiation module 3104 to the auxiliary electrode 502 of the secondary battery 100. The pre-lithiation connector 3204 may be any connector suitable for connection to the secondary battery 100, including a connector configured to mate with a similar connector on the battery, a clamping connector (such as an alligator clip), a wire soldered or welded to the secondary battery and the pre-lithiation module 3104, and the like. In some embodiments, the pre-lithiation connector 3206 is part of the battery connector 3100.
The sensors 3207 include sensors to monitor the pre-lithiation of the secondary battery 100 by the pre-lithiation module 3104. In the example embodiment, the sensors 3207 include voltage sensors to monitor voltages of the secondary battery 100 and the auxiliary electrode 502, as will be described in more detail below. The sensors 3207 may include temperature sensors for monitoring the ambient temperature around the secondary battery 100 and/or the temperature of the secondary battery, current sensors for monitoring current flowing through the secondary battery, or any other suitable sensors for monitoring the secondary battery or the pre-lithiation process. The sensors 3207 may include or may be connected to the pre-lithiation module controller 3202 through one or more other components, such as amplifiers, analog to digital converters (ADCs), filters, signal processors, or the like.
The communication interface 3208 connects the pre-lithiation module 3104 to the central controller 3004. The communication interface 3208 may be the communication interface 3108 or may be a separate communication interface. The communication interface 3208 may allow the pre-lithiation module 3104 to communicate directly with the central controller 3004, or it may allow the pre-lithiation module 3104 to communicate indirectly with the central controller, such as via the formation cluster controller 3110. The communication interface 3208 may be any wired or wireless communications interface that permits the controller 3202 to communicate with the communication central controller 3004 directly or via a network. Wireless communication interfaces 3208 may include a radio frequency (RF) transceiver, a Bluetooth® adapter, a Wi-Fi transceiver, a ZigBee® transceiver, an infrared (IR) transceiver, and/or any other device and communication protocol for wireless communication. (Bluetooth is a registered trademark of Bluetooth Special Interest Group of Kirkland, Washington; ZigBee is a registered trademark of the ZigBee Alliance of San Ramon, California). Wired communication interfaces 3208 may use any suitable wired communication protocol for direct communication including, without limitation, USB, RS232, I2C, SPI, analog, and proprietary I/O protocols. In some embodiments, the wired communication interface 3108 includes a wired network adapter allowing the controller 3202 to be coupled to a network, such as the Internet, a local area network (LAN), a wide area network (WAN), a mesh network, and/or any other network to communicate with remote devices and systems via the network.
The pre-lithiation module controller 3202 controls the current sink 3200 to pre-lithiate the secondary battery 100 according to a control algorithm stored in its memory 3212. Specifically, the pre-lithiation module controller 3202 adjusts the amplitude of the current through the current sink 3200 according to the control algorithm.
In a first embodiment, the control algorithm is a pulsed control algorithm. The pre-lithiation module controller 3202 drives the current sink 3200 to conduct a current between the cathode of the secondary battery 100 and the auxiliary electrode 502 for a first predetermined time. After the predetermined time, the pre-lithiation module controller 3202 turns off the current sink 3200 for a second predetermined time. In the example embodiment, the first and second predetermined times are the same length of time, resulting in a fifty percent duty cycle for the pulsed current provided by the current sink 3200. In other embodiments, the first and second predetermined times are not equal. In some embodiments, the first and second predetermined times are both about 15 seconds. In other embodiments, the first and second predetermined times may be longer or shorter than 15 seconds. In some embodiments, the first and second predetermined times are selectable/configurable by an operator. While the current sink 3200 is off, the pre-lithiation module controller 3202 samples the cathode to auxiliary electrode voltage (the first voltage) and the cathode to anode voltage (the second voltage) using the sensors 3207. The pre-lithiation module controller 3202 compares the first and second voltage and adjusts the amplitude of the current provided by the current sink 3200 (if needed) to attempt to minimize the different between the two voltages. The pre-lithiation module controller 3202 then begins to drive the current sink 3200 again and the process repeats. In the example embodiment, the process repeats until the first voltage decreases below a predetermined voltage threshold. In other embodiments, the process repeats for a predetermined length of time, a predetermined number of cycles, or until the current drops to a minimum level and stays there for a predetermined length of time.
In another example, the control algorithm does not pulse the current between the cathode of the secondary battery 100 and the auxiliary electrode 502 and attempts to maintain the voltage from the auxiliary electrode 502 to the anode of the secondary battery 100 at a small negative value. In this example, the pre-lithiation module controller 3202 drives the current sink 3200 to conduct a current between the cathode of the secondary battery 100 and the auxiliary electrode 502. While current is being conducted, the pre-lithiation module controller 3202 samples the cathode to auxiliary electrode voltage (the first voltage) and the cathode to anode voltage (the second voltage) using the sensors 3207.
The pre-lithiation module controller 3202 compares the first and second voltage and adjusts the amplitude of the current provided by the current sink 3200 (if needed) to maintain the voltage from the auxiliary electrode 502 to the anode of the secondary battery 100 at a small negative value. The small negative voltage may be predetermined. In an example embodiment, the small negative value is about negative ten millivolts. In other embodiments, the small negative voltage may be about negative ten millivolts, about negative nine millivolts, about negative eight millivolts, about negative seven millivolts, about negative six millivolts, about negative five millivolts, about negative four millivolts, about negative three millivolts, about negative two millivolts, or about negative one millivolts. The predetermined negative voltage may, in some embodiments, be greater than about negative ten millivolts. In some embodiments, the pre-lithiation module controller 3002 may selectively adjust the amplitude of the current provided by the current sink 3200 to maintain the voltage from the auxiliary electrode 502 to the anode of the secondary battery 100 at a voltage between zero volts and the predetermined negative voltage. In other embodiments, any other suitable negative voltage value may be used. By preventing this voltage from becoming positive, the possibility of lithium from the auxiliary electrode 502 unintentionally plating other components in the secondary battery 100 (such as casing/constraint 116) may be avoided.
The speed of the pre-lithiation process may be increased by decreasing (relative to the embodiment above) the voltage difference between the auxiliary electrode 502 and the anode of the secondary battery 100 to zero volts or a smaller negative value. The small negative value between the auxiliary electrode and the anode in the above examples is used (rather than 0 volts) in part as an offset to accommodate component tolerances and offsets, drift, and temperature based fluctuations (generally referred to sometimes as measurement error) affecting the pre-lithiation circuitry, such as pre-lithiation module 3202, that could result in a positive voltage from the auxiliary electrode to the anode of no offset were used. At least some of the following examples are operable to determine the measurement error and compensate for it in the control of the pre-lithiation process, thereby allowing pre-lithiation to be controlled with a smaller negative voltage (or a zero voltage) difference between the auxiliary electrode 502 and the anode of the secondary battery 100.
One example method of pre-lithiating a lithium based secondary battery (e.g., the secondary battery 100) with such a decreased voltage difference includes connecting a current sink (e.g., the current sink 3200) to an electrode (e.g., the positive electrode 208) and a source of lithium carrier ions (e.g., the auxiliary electrode 502) and controlling the current sink to conduct a current from the electrode through the auxiliary electrode to diffuse lithium from the auxiliary electrode to electrode active material layers of the lithium based secondary battery. The method includes periodically detecting a voltage between the auxiliary electrode and a counter-electrode (e.g., the negative electrode 208) periodically determining an adjustment to the voltage. The current sink is then controlled to control an amplitude of the current from the electrode through the auxiliary electrode to cause a sum of the voltage and the adjustment to be about zero volts. The connections to the electrode and counter-electrode by be by connection directly or indirectly to the current collectors (e.g., the anode current collectors 202 and cathode current collectors 204) or to the respective busbars (e.g., the first and second busbars 110, 112).
A detection circuit 3700 is an example sensor 3207 configured to monitor a voltage between the auxiliary electrode 502 and the anode (e.g., the negative electrode 209) of the secondary battery 100. In some embodiments, a second sensor 3207 may additionally monitor the voltage between the voltage between the cathode (e.g., the positive electrode 208) of the secondary battery 100 and the auxiliary electrode 502 of the secondary battery 100. The connection to the anode and/or cathode of the secondary battery 100 may be a connection directly or indirectly to the current collectors (e.g., the anode current collectors 202 and cathode current collectors 204) or to the respective busbars (e.g., the first and second busbars 110, 112).
The detection circuit 3700 includes an amplifier 3702 and a switch circuit 3704. The detection circuit uses an analog to digital converter (ADC) 3706, which may be a part of the detection circuit or may be a part of the pre-litionation module separate from the detection circuit. The amplifier may be an op-amp or any other amplifier suitable for providing an amplified voltage signal from an input voltage appropriate to a secondary battery. The example amplifier includes a first input 3708 and a second input 3710. The first input 3708 is coupled to the auxiliary electrode through the switch circuit. The second input 3710 is coupled to the anode of the secondary battery 100 through the switch circuit. In embodiments in which the amplifier is an op-amp, the first input is an inverting input of the amplifier, and the second input is the non-inverting input of the amplifier.
The switch circuit 3704 includes a pair of first switches 3712 and a second switch 3714. The switch circuit is controlled by the pre-lithiation module controller 3202. The first switches are switched together (e.g., both on/closed or both off/open). The second switch is generally switched opposite of the first switches. That is, when the first switches are closed, the second switch is open. When transitioning which of the first switches and the second switch are opened/closed, there will be an overlap when all switches in the switch circuit are open in some embodiments to avoid the possibility of all three switches being closed at the same time. Thus, for example, when the first switches are closed, the second switch is open, and it is determined to open the first switches and close the second switch, the first switches are opened first, and the second switch is only closed after the first switches are opened. The first switches selectively couple the first input 3708 to the auxiliary electrode 502 and the second input 3710 to the anode of the secondary battery. When the first switches are closed/on, the first input 3708 is electrically connected to the auxiliary electrode 502 and the second input 3710 is electrically connected to the anode of the secondary battery 100, and when the first switches are open/off, the first input 3708 is electrically disconnected from the auxiliary electrode 502 and the second input 3710 is electrically disconnected from the anode of the secondary battery 100. The second switch connects the first input to the second input. When the second switch is closed, the first input and the second input are electrically connected, and when the second switch is open, the first input and the second input are electrically disconnected.
In the first operational state (
When pre-lithiating the secondary battery 100 using the embodiments of the pre-lithiation module shown in
In another example, the control algorithm does not pulse the current between the cathode of the secondary battery 100 and the auxiliary electrode 502 and attempts to maintain a sum of the voltage offset and the voltage from the auxiliary electrode 502 to the anode of the secondary battery 100 close to zero or a small negative value. In this example, the pre-lithiation module controller 3202 drives the current sink 3200 to conduct a current between the cathode of the secondary battery 100 and the auxiliary electrode 502. While current is being conducted, the pre-lithiation module controller 3202 samples the auxiliary electrode to anode voltage using the detection module 3704 with in a first operational state (
In the example control algorithms described above, the pre-lithiation module controller 3202 adjusts the amplitude of the current provided by the current sink 3200 (if needed) to maintain the voltage from the auxiliary electrode 502 to the anode of the secondary battery 100 at about zero or at or below a very small negative value. The very small negative voltage may be predetermined. In an example embodiment, the very small negative value is less than about negative ten millivolts. In other embodiments, the very small negative voltage may be about or less than about negative nine millivolts, negative eight millivolts, negative seven millivolts, negative six millivolts, negative five millivolts, negative four millivolts, negative three millivolts, negative two millivolts, or negative one millivolts. In some embodiments, the pre-lithiation module controller 3002 may selectively adjust the amplitude of the current provided by the current sink 3200 to maintain the voltage from the auxiliary electrode 502 to the anode of the secondary battery 100 at a voltage between zero volts and the predetermined negative voltage. In other embodiments, any other suitable negative voltage value may be used. By preventing this voltage from becoming positive, the possibility of lithium from the auxiliary electrode 502 unintentionally plating other components in the secondary battery 100 (such as casing/constraint 116) may be avoided.
Temperature may affect the pre-lithiation process using any of the control algorithms described herein. An increased temperature may result in an increased current being able to be applied from the cathode of the secondary battery 100 to the auxiliary electrode 502. Thus, by operating at a higher temperature, more current may be conducted, which may result in pre-lithiation being completed more quickly. The gain may be greatest early in the pre-lithiation process and may decrease later in the process. Accordingly, in some embodiments, the pre-lithiation process is performed at higher temperatures early in the process in order to accelerate the pre-lithiation. In some embodiments, the gain relationship may be about 1 mA/1C in the early pre-lithiation process.
Some embodiments of the present disclosure achieve additional efficiencies during cell formation by combining two or more steps of the formation process into a combined step.
At 3902, the lithium based secondary battery 100 is charged using a charging circuit connected to the electrode busbar and the counter-electrode busbar of the secondary battery. In some embodiments, the secondary battery is charged at the same charge rate every time charging is performed. In other embodiments, the secondary battery is charged at a first charge rate the first-time charging is performed and charged at a second charge rate higher than the first charge rate each subsequent time that charging is performed on the same secondary battery. The charge rate(s) may be any suitable charge rates for the particular capacity and composition of the battery being charged. The charge rate is typically defined relative to the capacity (C) of the secondary battery. In some example embodiments, the charge rate that is always used or that is used for the first charge rate is C/20, and the charge rate used for the second charge rate is C/8. In some embodiments, using only a single charge rate, the charge rate is C/8. In other embodiments, a C/20 charge rate is always used.
Charging of the lithium based secondary battery 100 is stopped 3904 when the battery voltage reaches a first voltage between the electrode and the counter-electrode. The first voltage is the maximum voltage at which pre-lithiation is desired to be performed for a particular secondary battery. In some example embodiments, the first voltage is 3.65V. In other embodiments, the first voltage is 3.6V, 3.7V, 3.55V, or any other suitable voltage. In some embodiments, the first voltage is defined as predetermined percentage of or a predetermined voltage below the maximum voltage of the secondary battery 100. In general, and without being limited to any particular theory, a first voltage that is too high may slow down pre-lithiation by reducing the open circuit voltage between the auxiliary electrode and the counter-electrode, while too low of a first voltage my slow down pre-lithiation because the impedance in the secondary battery may rise as the voltage decreases and the electrode being full of lithium and not wanting to accept more lithium.
In the example embodiment, the method continues immediately to pre-lithiation of the secondary battery 100 at 3906. Specifically, after stopping the charging, a current sink connected to the electrode busbar and an auxiliary electrode is controlled to conduct a current from the electrode busbar through the auxiliary electrode to diffuse lithium from the auxiliary electrode to the electrode active material layers of the lithium based secondary battery. The specific pre-lithiation control scheme may be any suitable control algorithm, including any of the pre-lithiation control techniques described above. In some embodiments, the method 3900 includes a dwell time between stopping charging at 3904 and controlling the current sink at 3906. During the dwell time, the secondary battery 100 is not actively charged or pre-lithiated. The dwell time may be any suitable length of time, such as 1 second, 2 seconds, 5 seconds, 15 seconds, 30 seconds, 45 seconds, 60 seconds, 75 seconds, 90 seconds, 105 seconds, 120 seconds, 135 seconds, 150 seconds. In some embodiments, the dwell time is less than 150 seconds, less than 120 seconds, less than 90 seconds, less than 60 seconds, less than 30 seconds, or less than 15 seconds. In other embodiments, the dwell time is not predetermined and is based on another variable, such as a temperature, a voltage, a current, or the like.
Controlling the current sink to pre-lithiate the secondary battery 100 is stopped 3908 when the battery voltage reaches a second voltage between the electrode and the counter-electrode. The second voltage is lower than the first voltage. The second voltage is generally the minimum voltage at which pre-lithiation is desired to be performed for a particular secondary battery to achieve the desired pre-lithiation speed and stability. In some example embodiments, the second voltage is 3.55V. In other embodiments, the second voltage is about 3.5V, 3.3V, 3.1V, 2.9V 2.7V, 2.5V, 2.3V, 2.1V, 1.9V or any other suitable voltage. In general, and without being limited to any particular theory, allowing the pre-lithiation to continue to a lower second voltage appears to result in a shorter time to complete the pre-lithiation process than if a higher second voltage is used.
In the example embodiment, after controlling the current sink is stopped at 3908, the method 3900 immediately returns to 3902 and charges the secondary battery 100 back up to the first voltage and the charging/pre-lithiation cycle starts over again. As noted above, in some embodiments, the charging on the second or later time charging is performed at a different rate than the first time that the secondary battery is charged.
In some embodiments, the method 3900 includes a dwell time between stopping pre-lithiation at 3908 and returning to charging at 3902. During the dwell time, the secondary battery 100 is not actively charged or pre-lithiated. The dwell time may be any suitable length of time, such as 1 second, 2 seconds, 5 seconds, 15 seconds, 30 seconds, 45 seconds, 60 seconds, 75 seconds, 90 seconds, 105 seconds, 120 seconds, 135 seconds, 150 seconds. In some embodiments, the dwell time is less than 150 seconds, less than 120 seconds, less than 90 seconds, less than 60 seconds, less than 30 seconds, or less than 15 seconds. In other embodiments, the dwell time is not predetermined and is based on another variable, such as a temperature, a voltage, a current, or the like.
The method 3902 continues until the pre-lithiation is completed according to the particular pre-lithiation control algorithm being used. Thus, in some embodiments, the steps 3902-3908 of the method 3900 are repeated until a current through the auxiliary electrode drops below a threshold current.
Some other embodiments perform charging and pre-lithiation at the same time, rather than alternating in the manner of the method 3900. An example method 4000 for simultaneous charging and pre-lithiation is shown in
At 4002, the lithium based secondary battery 100 is charged for a predetermined time using a charging circuit connected to the electrode busbar and the counter-electrode busbar of the secondary battery. The charge rate(s) may be any suitable charge rates for the particular capacity and composition of the battery being charged. The charge rate is typically defined relative to the capacity (C) of the secondary battery. In the example embodiment, the charge rate is C/20. In some other embodiments, the charge rate is C/8. Still other embodiments may use any other suitable charge rate. The predetermined time in the example embodiment is two hours. Other embodiments may charge the secondary battery for a longer or shorter predetermined time. In other embodiments, the length of this initial charge is determined by the voltage difference between the electrode and the counter-electrode of the secondary battery, rather than a length of time. That is, the initial charging of the battery lasts until the voltage difference between the electrode and the counter-electrode of the secondary battery reaches a threshold value, such as 3.65V, 3.6V, 3.7V, 3.55V, some percentage of fully charged voltage, or the like.
The method 4000 begins pre-lithiation and continues charging of the secondary battery 100 at 4004. Specifically, after the predetermined time elapses, a current sink connected to the electrode busbar and an auxiliary electrode is controlled to conduct a current from the electrode busbar through the auxiliary electrode to diffuse lithium from the auxiliary electrode to the electrode active material layers of the lithium based secondary battery. The specific pre-lithiation control scheme may be any suitable control algorithm, including any of the pre-lithiation control techniques described above. In the example embodiment, the secondary battery is charged at a second charge rate in 4004 different from the charge rate during charging in 4002. The second charge rate in the example embodiment is C/8. In other embodiments, the second rate is any other suitable charge rate. In still other embodiments, a second charge rate is not used, and the secondary battery 100 is charged at the same rate during charging in 4002 and charging and pre-lithiating in 4004.
In some embodiments, the charging of the secondary battery is stopped during the pre-lithiation at 4004 when/if the voltage difference between the electrode and the counter-electrode of the secondary battery reaches a first threshold value, and restarted if/when the voltage difference between the electrode and the counter-electrode of the secondary battery drops to a second threshold value lower than the first threshold value. In an example embodiment, the first threshold value is 4.0V and the second threshold value is 3.6V. Other embodiments may use any other suitable higher or lower voltages as the first threshold and the second threshold.
Controlling the current sink to pre-lithiate the secondary battery 100 and charging the secondary battery is stopped 4006 when pre-lithiation is complete according to the particular pre-lithiation control algorithm being used. Thus, in some embodiments, the simultaneous charging and pre-lithiation of the method 4000 until a current through the auxiliary electrode drops below a threshold current, such as 250 microamps. In some other embodiments, the charging of the secondary battery continues, if necessary, after pre-lithiation is completed until the voltage difference between the electrode and the counter-electrode of the secondary battery reaches a third threshold value greater than the first and second threshold values. In such embodiments, the method 4000 may include holding the voltage difference between the electrode and the counter-electrode of the secondary battery at the third threshold value after stopping the pre-lithiation.
Embodiments of the present disclosure utilize auxiliary electrodes to transfer or buffer carrier ions to a secondary battery during or subsequent to, initial formation of the secondary battery. Transferring carrier ions to the secondary battery (also referred to as pre-lithiating or buffering) mitigates carrier ion losses during formation due to, for example, SEI, thereby providing a technical benefit of improving the capacity of the secondary battery. Further, transferring carrier ions to the secondary battery provides the negative electrode of the secondary battery additional carrier ions beyond the coulombic capacity of the positive electrode of the secondary battery, thereby providing a reservoir of addition carrier ions over the cycle life of the secondary battery, further mitigating carrier ion loss during cycling due to side reactions which remove the carrier ions from availability during cycling. The result of the additional carrier ions at the negative electrode provides a further technical benefit of reducing the amount of capacity loss in the secondary battery from one discharge-charge cycle to the next, thereby improving the overall capacity of the secondary battery during its cycle life.
The following embodiments are provided to illustrate various aspects of the present disclosure. The following embodiments are not intended to be limiting and therefore, the present disclosure further supports other aspects and/or embodiments not specifically provided below.
This written description uses examples to disclose the invention, including the best mode, and also to enable any person skilled in the art to practice the invention, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the invention is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims if they have structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal languages of the claims.
This application claims benefit of U.S. Provisional Patent Application Ser. No. 63/584,714, filed on Sep. 22, 2023, which is hereby incorporated by reference herein in its entirety.
Number | Date | Country | |
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63584714 | Sep 2023 | US |