Battery packs including electrochemical cells, associated components, and arrangements thereof are generally described.
Batteries typically include cells that undergo electrochemical reactions to produce electric current. Heat may be produced during cycling of the cell, which may affect the performance of the battery. Applying a force to at least a portion of an electrochemical cell (e.g., during cycling of the cell) can improve the performance of the electrochemical cell. Certain embodiments of the present disclosure are directed to inventive articles, systems, and methods relating to the handling of compressive force and heat transfer in batteries.
Battery packs including electrochemical cells, associated components, and arrangements thereof are generally described. In some aspects, battery packs with housings that undergo relatively little expansion and contraction even in cases where electrochemical cells in the battery pack undergo a relatively high degree of expansion and contraction during charging and discharging are provided. Battery packs configured to apply relatively high magnitudes and uniform force to electrochemical cells in the battery pack, while in some cases having high energy densities and a relatively low pack burden, are also provided. In certain aspects, arrangements of electrochemical cells and associated components are generally described. In some aspects, thermally conductive solid articles that can be used for aligning components of the battery pack are described. In some aspects, thermally insulating and compressible components for battery packs are generally described. In some instances, the battery pack includes multiple battery modules at least partially enclosed by the same housing. The subject matter of the present invention involves, in some cases, interrelated products, alternative solutions to a particular problem, and/or a plurality of different uses of one or more systems and/or articles.
In one aspect, battery packs are provided. In some embodiments, a battery pack comprises a first battery comprising a first electrochemical cell and a first pair of terminals electronically coupled to the first electrochemical cell; a second battery comprising a second electrochemical cell and a second pair of terminals electronically coupled to the second electrochemical cell; and a housing at least partially enclosing the first battery and the second battery; wherein the housing is configured to apply, during at least one period of time during charge and/or discharge of the first electrochemical cell and/or the second electrochemical cell, an anisotropic force with a component normal to a first electrode surface of the first electrochemical cell and/or a second electrode surface of the second electrochemical cell defining a pressure of at least 3 kgf/cm2. In some embodiments, the first electrode surface of the first electrochemical cell is a first electrode active surface and/or the second electrode surface of the second electrochemical cell is a second electrode active surface.
In some embodiments, a battery pack comprises a stack comprising a first electrochemical cell and a second electrochemical cell; and a housing at least partially enclosing the stack, the housing comprising a solid plate covering at least a portion of an end of the stack; wherein: the housing is configured to apply, via the solid plate and tension in a solid housing component coupled to the solid plate, during at least one period of time during charge and/or discharge of the first electrochemical cell and/or the second electrochemical cell, an anisotropic force with a component normal to a first electrode surface of the first electrochemical cell and/or a second electrode surface of the second electrochemical cell defining a pressure of at least 3 kgf/cm2, and the solid housing component is coupled to the solid plate at least partially via coupling of an insert to a housing stop portion adjacent to an exterior surface of the solid plate, the insert comprising: a body that passes through the solid housing component and enters a complementary recess of the housing stop portion adjacent to a first side of the solid housing component, and a head adjacent to a second side of the solid housing component opposite the first side. In some embodiments, the first electrode surface of the first electrochemical cell is a first electrode active surface and/or the second electrode surface of the second electrochemical cell is a second electrode active surface.
In some embodiments, a battery pack comprises a stack of electrochemical cells comprising a first electrochemical cell and a second electrochemical cell; a first battery comprising a first battery module comprising: a first subset of the electrochemical cells, the first subset including the first electrochemical cell, and a first pair of terminals electronically coupled to the first electrochemical cell; a second battery comprising a second battery module comprising: a second, different, subset of the electrochemical cells, the second subset including the second electrochemical cell, and a second pair of terminals electronically coupled to the second electrochemical cell; a housing at least partially enclosing the stack, the housing comprising a solid plate comprising carbon fiber covering at least a portion of an end of the stack; a substrate to which a tab of the first electrochemical cell and/or the second electrochemical cell can be connected; and an electrically conductive interconnect on the substrate connected to at least one tab of the first electrochemical cell and/or the second electrochemical cell; wherein: the first battery and the second battery can be charged and/or discharged independently; the first battery is configured to be part of a circuit having a first voltage, and the second battery is configured to be part of a circuit having a second, different voltage; the housing is configured to apply, via the solid plate and tension in a solid housing component coupled to the solid plate, during at least one period of time during charge and/or discharge of the first electrochemical cell and/or the second electrochemical cell, an anisotropic force with a component normal to a first electrode surface of the first electrochemical cell and/or a second electrode surface of the second electrochemical cell defining a pressure of at least 3 kgf/cm2; the solid housing component comprises carbon fiber and is coupled to the solid plate at least partially via coupling of an insert to a housing stop portion adjacent to an exterior surface of the solid plate, the insert comprising: a body that passes through the solid housing component and enters a complementary recess of the housing stop portion adjacent to a first side of the solid housing component, and a head adjacent to a second side of the solid housing component opposite the first side; and at least one electrochemical cell of the battery pack comprises lithium metal and/or a lithium alloy as an electrode active material during at least a portion of a charging and/or discharging process of the at least one electrochemical cell. In some embodiments, the first electrode surface of the first electrochemical cell is a first electrode active surface and/or the second electrode surface of the second electrochemical cell is a second electrode active surface. In some embodiments, the electronically conductive interconnect comprises: a first material portion connected to a first tab of the first electrochemical cell, and a second material portion connected to a second tab of the second electrochemical cell. In some embodiments, the first material portion and the second material portion are made of different metals and/or metal alloys.
Other advantages and novel features of the present invention will become apparent from the following detailed description of various non-limiting embodiments of the invention when considered in conjunction with the accompanying figures. In cases where the present specification and a document incorporated by reference include conflicting and/or inconsistent disclosure, the present specification shall control.
Non-limiting embodiments of the present invention will be described by way of example with reference to the accompanying figures, which are schematic and are not intended to be drawn to scale. In the figures, each identical or nearly identical component illustrated is typically represented by a single numeral. For purposes of clarity, not every component is labeled in every figure, nor is every component of each embodiment of the invention shown where illustration is not necessary to allow those of ordinary skill in the art to understand the invention. In the figures:
Battery packs including electrochemical cells, associated components, and arrangements thereof are generally described. In some aspects, battery packs with housings that undergo relatively little expansion and contraction even in cases where electrochemical cells in the battery pack undergo a relatively high degree of expansion and contraction during charging and discharging are provided. Battery packs configured to apply relatively high magnitudes and uniform force to electrochemical cells in the battery pack, while in some cases having high energy densities and a relatively low pack burden, are also provided. In certain aspects, arrangements of electrochemical cells and associated components are generally described. In some aspects, thermally conductive solid articles that can be used for aligning components of the battery pack are described. In some aspects, thermally insulating and compressible components for battery packs are generally described. In some instances, the battery pack includes multiple battery modules at least partially enclosed by the same housing. The present disclosure describes multiple inventive aspects relating to battery pack components and arrangements thereof, application of force to multiple electrochemical cells in battery packs, and thermal management. These inventive aspects can, alone or in combination, lead to the manufacture of battery packs with unexpected properties such as unexpectedly high energy densities and durability.
In some cases, it may be beneficial to apply force to electrochemical cells in a battery pack. For example, in some cases applying an anisotropic force with a component normal to at least one electrode surface of the electrochemical cells can improve performance during charging and/or discharging by reducing problems such as dendrite formation and surface roughening of the electrode while improving current density. One such example is the case where at least one of the electrochemical cells of the battery pack comprises lithium metal or a lithium metal alloy as an electrode active material. Lithium metal may undergo dendrite growth, for example, which can in certain cases lead to failure of the electrochemical cell and safety hazards. Application of relatively high magnitudes of anisotropic force to electrodes comprising lithium metal may mitigate lithium dendrite formation and other deleterious phenomena. However, it has been realized in the context of the present disclosure that numerous challenges may emerge when applying force within battery packs comprising multiple electrochemical cells (e.g., comprising lithium and/or lithium alloy as an electrode active material). For example, application of a relatively uniform force such that each of the electrochemical cells experiences a relatively similar pressure distribution can be important for performance and durability, and managing pressure on multiple cells must be accomplished simultaneously. Further, certain types of electrochemical cells may undergo relatively large dimensional changes during cycling. As one example, an electrode comprising lithium and/or lithium metal alloy may expand significantly due to lithium deposition during charging and contract significantly upon lithium ion release during discharging. Such dimensional changes of the electrochemical cells may lead to uneven pressure distributions and problematic battery pack dimensional changes.
The present disclosure provides methods, articles, and devices that can, in some cases, be used to mitigate such dimensional changes of the overall battery pack (e.g., the housing) even in situations where electrochemical cells may expand and contract. For example, relatively high magnitudes of force (e.g., defining a pressure of greater than or equal to 3 kgf/cm2 and up to 25 kgf/cm2) may be applied. For example, it has been realized that relatively high magnitudes of force may be applied relatively uniformly using certain housing components (e.g., solid plates) having relatively high stiffness while being lightweight (e.g., certain types of carbon fiber having certain weaves, fiber orientation, and/or thicknesses). Further, certain articles in the battery pack may compensate for dimensional changes of the electrochemical cells (e.g., thermally insulating compressible solid article portions such as microcellular elastomeric foams). It has been discovered that certain types of components can have suitable mechanical properties for use in battery packs under compressive force (e.g., relatively low compression set, relatively high resilience) while being thermally insulating. Some such thermally insulating compressible solid article portions may then be capable of serving multiple roles: compensating for dimensional changes in electrochemical cells and mitigating heat transfer between electrochemical cells. It has also been discovered that aligning components (e.g., electrochemical active regions of the electrochemical cells) of the battery pack can lead to improved performance and durability (e.g., by increasing the uniformity of the pressure distribution experienced by the electrochemical active regions). Certain aspects of the present disclosure are related to thermally conductive solid article portions that can be used to align electrochemical active regions of the battery pack while also performing other functions, such as facilitating heat transfer away from the electrochemical cells (e.g., laterally). The use of articles capable of alignment and thermal transfer may reduce the number of components needed for the battery pack, which may reduce complexity, pack burden, and/or costs. Certain aspects also relate to unconventional arrangements of components that can simultaneously mitigate multiple potentially deleterious phenomena associated with battery packs comprising multiple electrochemical cells, while using relatively few components, which may allow for relatively high energy densities while also allowing for good durability. For example, certain arrangements of electrochemical cells, thermally conductive solid article portions, and thermally insulating compressible solid article portions may promote unexpectedly efficient heat transfer away from the electrochemical cells while also facilitating compensation for applied forces and cell breathing and facilitating relatively uniform pressure distributions (e.g., within ±2.5 kgf/cm2 or within ±2 kgf/cm2 across an electrochemical active region).
In one aspect, battery packs are generally described. The battery pack may include, in some embodiments, one or more rechargeable electrochemical cells. In some embodiments, the battery pack comprises one or more rechargeable lithium-ion electrochemical cells. In this disclosure, a battery pack refers to any collection of multiple electrochemical cells. In some embodiments, the multiple electrochemical cells of the battery pack are each at least partially enclosed by a housing of the battery pack, as described in more detail below. The multiple electrochemical cells of the battery pack may be electronically coupled in series and/or parallel. For example, in some embodiments, the electrochemical cells of the battery pack are electronically coupled in series and/or parallel to form a single battery having a single pair of terminals (a positive terminal and a negative terminal). In some embodiments, the battery pack comprises multiple battery modules each comprising multiple electrochemical cells. The multiple electrochemical cells within each battery module of the battery pack may be electronically coupled in series and/or parallel within that battery module. In some embodiments, the multiple electronically coupled electrochemical cells of each battery module can form an electronically independent circuit. In some embodiments, the battery pack has multiple pairs of terminals. For example, in some embodiments, each battery module of the battery pack has a pair of terminals (a positive terminal and a negative terminal) electronically coupled to the electrochemical cells of that battery module. In some embodiments, the multiple battery modules of the battery pack are at least partially enclosed by a same housing.
In some embodiments, electrochemical cells in the battery pack (e.g., the first electrochemical cell, the second electrochemical cell) comprise at least one anode.
In some embodiments, electrochemical cells in the battery pack (e.g., the first electrochemical cell, the second electrochemical cell) comprise at least one cathode. For example, referring again to
As used herein, “cathode” refers to the electrode in which an electrode active material is oxidized during charging and reduced during discharging, and “anode” refers to the electrode in which an electrode active material is reduced during charging and oxidized during discharging.
In some embodiments, electrochemical cells in the battery pack (e.g., the first electrochemical cell, the second electrochemical cell) comprise a separator between the anode and the cathode.
It should be understood that while in some embodiments the first electrochemical cell and the second electrochemical cell have the same types of components (e.g., same anode active material, same cathode active material, same type of separator), in other embodiments the first electrochemical cell has one or more different components than the second electrochemical cell (e.g., a different anode active material, a different cathode active material, a different type of separator). In some embodiments, the first electrochemical cell and the second electrochemical cell are identical in composition and/or dimensions.
In some embodiments, the battery pack comprises a housing. The housing may at least partially enclose other components of the battery pack. For example, the housing may at least partially enclose the first electrochemical cell and the second electrochemical cell.
Some embodiments are related to applying, during at least one period of time during charge and/or discharge of the electrochemical cells (e.g., first electrochemical cell, second electrochemical cell), an anisotropic force with a component normal to an electrode active surface of at least one electrochemical cell of the battery pack. As used herein, the term “electrode active surface” is used to describe a surface of an electrode that can be in physical contact with an electrolyte when the article is part of an electrochemical cell, and at which electrochemical reactions may take place. The electrolyte can comprise any of a variety of materials that permit transport of ions or other non-electron electrochemically active reactants between the electrode and a counter-electrode. As one example, in embodiments in which the electrode comprises a lithium metal foil, the external surface of the lithium metal foil would be an active surface of the electrode. As mentioned above, application of such a force may reduce potentially deleterious phenomena associated with certain types of electrochemical cells (e.g., cells comprising lithium metal as an electrode active material) and improve utilization. For example, in some cases, applying an anisotropic force with a component normal to an active surface of an electrode of the electrochemical device can reduce problems (such as surface roughening of the electrode and dendrite formation) while improving current density. Application of such forces to multiple electrochemical cells of a battery pack may present certain challenges, including uniformity of pressure distribution for each electrochemical cell, which can be important for both performance and durability. Certain aspects described herein may, in some cases, address and overcome such challenges.
In some embodiments, the housing of the battery pack is configured to apply, during at least one period of time during charge and/or discharge of the first electrochemical cell and/or the second electrochemical cell, an anisotropic force having a relatively high magnitude component normal to electrode active surfaces of at least one (or all) of the electrochemical cells in the battery pack. For example, in some embodiments where the battery pack comprises a first electrochemical cell having a first electrode active surface and a second electrochemical cell having a second electrode active surface, the housing of the battery pack is configured to apply, during at least one period of time during charge and/or discharge of the first electrochemical cell and/or the second electrochemical cell, an anisotropic force having a relatively high magnitude component normal to the first electrode active surface and the second electrode active surface. The housing may be configured to apply such a force in a variety of ways. For example, in some embodiments, the housing comprises two solid articles (e.g., a first solid plate and a second solid plate as shown in
Some embodiments comprise applying an anisotropic force with a component normal to a first electrode active surface of the first electrochemical cell and/or a second electrode active surface of the second electrochemical cell defining a pressure of at least 3 kgf/cm2, at least 5 kgf/cm2, at least 8 kgf/cm2, at least 10 kgf/cm2, at least 12 kgf/cm2, at least 20 kgf/cm2, at least 25 kgf/cm2, or more. In some such cases, the housing is configured to apply such anisotropic forces. While high magnitudes of anisotropic force with a component normal to an electrode active surface can improve performance, too high of a magnitude of force may cause problems such as damage to certain components of the battery pack (e.g., the thermally insulating compressible solid article portion described below). It has been unexpectedly observed, however, that there are ranges of magnitudes of anisotropic force that can be applied that can, in some cases, achieve desirable performance of the battery pack while avoiding such damage. For example, some embodiments comprise applying (e.g., via the housing) during at least one period of time during charge and/or discharge of the first electrochemical cell and/or the second electrochemical cell, an anisotropic force with a component normal to a first electrode active surface of the first electrochemical cell and/or a second electrode active surface of the second electrochemical cell defining a pressure of less than or equal to 40 kgf/cm2, less than or equal to 35 kgf/cm2, less than or equal to 30 kgf/cm2, less than or equal to 25 kgf/cm2, less than or equal to 20 kgf/cm2, less than or equal to 15 kgf/cm2, less than or equal to 12 kgf/cm2, or less. Combinations of these ranges (e.g., at least 3 kgf/cm2 and less than or equal to 25 kgf/cm2, at least 3 kgf/cm2 and less than or equal to 15 kgf/cm2, at least 10 kgf/cm2 and less than or equal to 40 kgf/cm2, or at least 12 kgf/cm2 and less than or equal to 30 kgf/cm2) are possible. In some embodiments, an anisotropic force with a component normal to a first electrode surface of the first electrochemical cell and/or a second electrode surface of the second electrochemical cell defining a pressure in one of the aforementioned ranges is applied. In some embodiments, an anisotropic force with a component normal to a surface of an electrode of the first electrochemical cell and/or a surface of an electrode of the second electrochemical cell defining a pressure in one of the aforementioned ranges is applied, where the surface of the electrode of the first electrochemical cell and/or the second electrochemical cell comprises metallic lithium (e.g., lithium metal and/or a metal alloy comprising lithium). In some embodiments, an anisotropic force with a component normal to a surface of an electrode of the first electrochemical cell and/or a surface of an electrode of the second electrochemical cell defining a pressure in one of the aforementioned ranges is applied, where the surface of the electrode of the first electrochemical cell and/or the second electrochemical cell is facing an electrode of the first electrochemical cell or the second electrochemical cell having an opposite polarity (e.g., the anisotropic force has a component normal to a surface of an anode facing a cathode of the cell, or the anisotropic force has a component normal to a surface of a cathode facing an anode of the cell). In some embodiments where the first electrochemical cell and the second electrochemical cell are part of a stack of cells, an anisotropic force with a component normal to a lateral surface of the stack (corresponding to an end of the stack rather than a side of the stack) defining a pressure in one of the aforementioned ranges is applied. In some embodiments where the first electrochemical cell and the second electrochemical cell are part of a stack of cells, an anisotropic force with a component parallel to the direction in which the cells are stacked defining a pressure in one of the aforementioned ranges is applied. For example, in
Some embodiments comprise applying a first anisotropic force with a component normal to a first electrode active surface of the first electrochemical cell and/or a second electrode active surface of the second electrochemical cell defining a pressure having a first magnitude of at least 3 kgf/cm2 and then also during a charge and/or discharge of the battery pack, applying a second anisotropic force with a component normal to a first electrode active surface of the first electrochemical cell and/or a second electrode active surface of the second electrochemical cell defining a pressure having a second magnitude that is at least 5 kgf/cm2, at least 8 kgf/cm2, at least 10 kgf/cm2, at least 12 kgf/cm2, at least 15 kgf/cm2, or higher and less than or equal to 40 kgf/cm2, less than or equal to 30 kgf/cm2, less than or equal to 25 kgf/cm2, less than or equal to 20 kgf/cm2, less than or equal to 15 kgf/cm2, less than or equal to 12 kgf/cm2, or less. For example, some embodiments comprise applying a first anisotropic force with a component normal to a first electrode active surface of the first electrochemical cell and/or a second electrode active surface of the second electrochemical cell defining a pressure having a first magnitude of at least 3 kgf/cm2 and then also during a charge and/or discharge of the battery pack, applying a second anisotropic force with a component normal to a first electrode active surface of the first electrochemical cell and/or a second electrode active surface of the second electrochemical cell defining a pressure having a second magnitude that is greater than or equal to 12 kgf/cm2 and less than or equal to 25 kgf/cm2. In some embodiments, the second magnitude of pressure is greater than the first magnitude by a factor of at least 1.2, at least 1.5, at least 2, at least 2.5, and/or up to 3, or up to 4, or higher. The second magnitude may be higher than the first magnitude, for example, in some embodiments where the first magnitude of force is applied via the housing (e.g., a rigid housing) and during a charging and/or discharge process, expansion of one or more components of the battery pack (e.g., one or more electrochemical cells) causes the force experienced by the electrochemical cells to increase. In some embodiments, the first magnitude occurs when the electrochemical cells are at a state of charge (SOC) of less than or equal to 10%, less than or equal to 5%, less than or equal to 2%, less than or equal to 1%, or 0%. In some embodiments, the second magnitude occurs when the electrochemical cells are at a state of charge of greater than or equal to 50%, greater than or equal to 75%, greater than or equal to 90%, greater than or equal to 95%, greater than or equal to 99%, or 100%. Combinations of these ranges are possible. For example, in some embodiments, the first magnitude occurs when the electrochemical cells are at a state of charge of less than or equal to 10% and the second magnitude (e.g., that defines a pressure that is greater than that of the first magnitude by a factor of at least 1.2 and up to 4) occurs when the electrochemical cells are at a state of charge of greater than or equal to 50%. In one exemplary embodiment, the magnitude of anisotropic force defines a pressure of 3 kgf/cm2 at a 0% SOC and 25 kgf/cm2 at a 100% SOC. In another exemplary embodiment, the magnitude of anisotropic force defines a pressure of 5 kgf/cm2 at a 0% SOC and 15 kgf/cm2 at a 100% SOC. In another exemplary embodiment, the magnitude of anisotropic force defines a pressure of 12 kgf/cm2 at a 0% SOC and 30 kgf/cm2 at a 100% SOC. In some embodiments, an anisotropic force with a component normal to a first electrode surface of the first electrochemical cell and/or a second electrode surface the second electrochemical cell defining a pressure in one of the aforementioned ranges is applied. In some embodiments, an anisotropic force with a component normal to a surface of an electrode of the first electrochemical cell and/or a surface of an electrode of the second electrochemical cell defining a pressure in one of the aforementioned ranges is applied, where the surface of electrode of the first electrochemical cell and/or the second electrochemical cell comprises metallic lithium (e.g., lithium metal and/or a metal alloy comprising lithium). In some embodiments, an anisotropic force with a component normal to a surface of an electrode of the first electrochemical cell and/or a surface of an electrode of the second electrochemical cell defining a pressure in one of the aforementioned ranges is applied, where the surface of the electrode of the first electrochemical cell and/or the second electrochemical cell is facing an electrode of the first electrochemical cell or the second electrochemical cell having an opposite polarity (e.g., the anisotropic force has a component normal to a surface of an anode facing a cathode of the cell, or the anisotropic force has a component normal to a surface of a cathode facing an anode of the cell). In some embodiments where the first electrochemical cell and the second electrochemical cell are part of a stack of cells, an anisotropic force with a component normal to a lateral surface of the stack (corresponding to an end of the stack rather than a side of the stack) defining a pressure in one of the aforementioned ranges is applied. In some embodiments where the first electrochemical cell and the second electrochemical cell are part of a stack of cells, an anisotropic force with a component parallel to the direction in which the cells are stacked defining a pressure in one of the aforementioned ranges is applied.
As mentioned above, in some embodiments, the battery pack comprises one or more solid plates. In some such cases, the housing is configured to apply the anisotropic force via a solid plate. The solid plates may be, for example, endplates configured to apply an anisotropic force to the electrochemical cells (e.g., first electrochemical cell, second electrochemical cell). For example, in
The solid plate may have any of a variety of shapes, depending on, for example, the configuration of the housing and the desired performance attributes of the battery. In some embodiments, the solid plate is shaped such that a mass of the solid plate is relatively low for a given overall set of lateral dimensions. In some embodiments, the solid plate has a lateral recess. For example, the solid plate may be shaped such that some (e.g., at least 25 vol %, at least 50 vol %, at least 75 vol %, at least 90 vol %, or more), but not all of an edge region of the solid plate is missing (e.g., lacks solid material). An edge region may be a volume of a solid plate within 20%, within 10%, within 5%, or less of an edge of the solid plate.
In some embodiments, the solid plate has a lateral cross-sectional shape where some (or all) corners of the shape are truncated.
The housing may comprise any suitable solid material. In some embodiments, a solid plate is or comprises a metal, metal alloy, composite material, or a combination thereof. In some cases, the metal that the solid plate is or comprises is a transition metal. For example, in some embodiments, the solid article is or comprises Ti, Cr, Mn, Fe, Co, Ni, Cu, or a combination thereof. In some embodiments, the solid plate is or comprises a non-transition metal. For example, in some embodiments, the solid article is or comprises Al, Zn, or combinations thereof. Exemplary metal alloys that the solid plate can be or comprise include alloys of aluminum, alloys of iron (e.g., stainless steel), or combinations thereof. Exemplary composite materials that the solid plate can be or comprise include, but are not limited to, reinforced polymeric, metallic, or ceramic materials (e.g., fiber-reinforced composite materials), carbon-containing composites, or combinations thereof.
In some embodiments, a solid plate (e.g., solid plate 201) of the housing comprises carbon fiber. Carbon fiber may be present in the solid plate in a relatively high amount (e.g., greater than or equal to 50 wt %, greater than or equal to 75 wt %, greater than or equal to 90 wt %, greater than or equal to 95 wt %, greater than or equal to 99 wt %, 100 wt %). Carbon fiber can, in some cases, afford relatively high stiffness and/or strength while having a relatively low mass (e.g., by having a relatively low mass density). It has been discovered, in the context of the present disclosure, that certain types of carbon fiber solid plates can allow for the application of relatively high magnitudes of anisotropic force to the electrochemical cells of the battery pack with relatively uniform distributions across multiple of the electrochemical cells without burdening the battery pack with too much mass. In some embodiments, the carbon fiber comprises unidirectional carbon fiber. In other words, in some embodiments, at least one layer (or all layers) of the carbon fiber material of the solid plate is unidirectional within the layer. While relatively thin and/or twill weave carbon fiber materials are known, it has been discovered herein that unidirectional carbon fiber laminates may afford relatively beneficial properties (e.g., high stiffness and/or strength, low deflection under load). In some embodiments, the housing comprises a solid plate comprising carbon fiber, the solid plate having a thickness of at least 5 mm, at least 8 mm, at least 10 mm, and/or up to 12 mm, up to 15 mm, up to 20 mm, or more.
In some embodiments, the solid plate comprises multiple layers of carbon fiber (e.g., unidirectional carbon fiber). In some such embodiments, the solid plate of the housing comprises a first layer comprising carbon fibers substantially parallel to a first direction in the plane of the first layer and a second layer comprising carbon fibers substantially parallel to a second direction in the plane of the second layer. In some embodiments, two lines in a plane can be substantially parallel if, for example, the maximum angle defined by the two lines is less than or equal to 10°, less than or equal to 5°, less than or equal to 2°, or less than or equal to 1°. The angle between the first direction and the second direction may be an angle θ. In embodiments in which such a layer orientation pattern is repeated, the pattern can be represented as “[0°/0].” In some embodiments, θ is greater than or equal to (i.e., more positive than) −90°, greater than or equal to −75°, greater than or equal to −60°, greater than or equal to −45°, greater than or equal to −30°, greater than or equal to −15°, or greater, and/or less than or equal to 90°, less than or equal to 75°, less than or equal to 60°, less than or equal to 45°, less than or equal to 30°, less than or equal to 15°, or less. Combinations of these ranges (e.g., θ greater than or equal to −90° and less than or equal to 90°) are possible. In some embodiments, θ has a non-zero value. In some embodiments, the solid plate comprises a third layer comprising carbon fibers substantially parallel to the first direction. In embodiments in which such a layer orientation pattern is repeated, the pattern can be represented as “[0°/θ/0° ].”
In some embodiments, the multiple layers of carbon fiber comprise, in order: a first layer comprising carbon fibers substantially parallel to a first direction in the plane of the first layer, a second layer comprising carbon fibers substantially parallel (e.g. within 10°, within 5°, within 2°, within 1° of parallel) to a second direction in the plane of the second layer, a third layer comprising carbon fibers substantially parallel to the first direction in the plane of the third layer, a fourth layer comprising carbon fibers substantially parallel (e.g. within 10°, within 5°, within 2°, within 1° of parallel) to a third direction in the fourth layer, and a fifth layer comprising carbon fibers substantially parallel to the first direction in the plane of the fifth layer. The angle between the first direction and the second direction may be an angle θ, and the angle between the first direction and the third direction may be an angle cp. In embodiments in which such a layer orientation pattern is repeated, the pattern can be represented as “[0°/θ/0°/φ/0° ].” It should be understood that when notation of this form is used, the direction of each layer may be within 10° (i.e., +/−10°) of the direction denoted by the angle value in the notation. For example, a layer orientation having repeating units in which the first layer is at 0°, the second layer is at θ, the third layer is at 5°, the fourth layer is at φ, and the fifth layer is at −10° would be considered to have a “[0°/θ/0°/φ/0° ]” layer orientation pattern because each layer is within 10° of the value indicated by the notation. Each of the individual layers may have a unidirectional weave. In some embodiments, θ is greater than or equal to (i.e., more positive than) −90°, greater than or equal to −75°, greater than or equal to −60°, greater than or equal to −45°, greater than or equal to −30°, greater than or equal to −15°, or greater, and/or less than or equal to 90°, less than or equal to 75°, less than or equal to 60°, less than or equal to 45°, less than or equal to 30°, less than or equal to 15°, or less. Combinations of these ranges (e.g., θ greater than or equal to −90° and less than or equal to 90°) are possible. In some embodiments, φ is greater than or equal to −90°, greater than or equal to −75°, greater than or equal to −60°, greater than or equal to −45°, greater than or equal to −30°, greater than or equal to −15°, or greater, and/or less than or equal to 90°, less than or equal to 75°, less than or equal to 60°, less than or equal to 45°, less than or equal to 30°, less than or equal to 15°, or less. Combinations of the ranges (e.g., φ greater than or equal to −90° and less than or equal to 90°) are possible. In some embodiments, φ has a nonzero value. In some embodiments, the value of φ is equal to the negative value of θ (e.g., θ equals 30° and φ equals −30°, or θ equals 60° and φ equals −60°).
The multiple layers of carbon fiber may include repeating units of the patterns of layer orientations described above (e.g., repeating units of [0°/θ], [0°/θ/0° ], [0°/θ/0°/φ/0° ], etc.). It has been observed that some patterns of unidirectional carbon fiber layers, with certain orientations (e.g., where θ equals 30° and φ equals −30°, denoted as “[0°/30°/0°/−30/0°]”) can afford properties that are beneficial in some scenarios. For example, it has been observed that solid articles such as solid plates having some such patterns of unidirectional carbon fiber layers demonstrate less deflection under applied load than otherwise identical solid articles such as solid plates lacking such patterns (e.g., solid plates in which the carbon fibers of each layer are all substantially parallel).
In some embodiments, the solid plate comprises carbon fiber having a relatively high modulus. For example, in some embodiments the solid plate comprises layers comprising carbon fiber, and one or more of the layers has a relatively high tensile modulus and a relatively high flexural modulus. In some embodiments, the solid plate comprises layers comprising carbon fiber, one or more of the layers having a tensile modulus of at least 120 GPa, at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa or greater, and a flexural modulus of at least 120 GPa at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa or greater at room temperature (25° C.). In some embodiments, the solid plate comprises layers comprising carbon fiber, one or more of the layers having a tensile modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa or less, and a flexural modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa or less at room temperature (25° C.). Combinations of the ranges (e.g., a tensile modulus of at least 120 GPa and less than or equal to 650 GPa and a flexural modulus of at least 120 GPa and less than or equal to 650 GPa) are possible. The tensile modulus of a layer can be measured using ASTM D3039, and the flexural modulus can be measured using ASTM D790. In certain instances, the solid plate has a relatively large number of layers satisfying the modulus ranges above. For example, in some embodiments, the solid plate comprises at least 1, at least 2, at least 3, at least 5, at least 10, at least 15, and/or up to 20, up to 25, up to 50, up to 60, up to 75, or more layers comprising carbon fiber having a tensile modulus of at least 120 GPa, at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa or greater, and a flexural modulus of at least 120 GPa at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa or greater at room temperature (25° C.). In some embodiments, the solid plate comprises at least 1, at least 2, at least 3, at least 5, at least 10, at least 15, and/or up to 20, up to 25, up to 50, up to 60, up to 75, or more layers comprising carbon fiber having a tensile modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa or less, and a flexural modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa or less at room temperature (25° C.).
The housing may comprise couplings that can be used to connect components of the housing and/or apply the anisotropic force. The housing may comprise, for example, couplings proximate to the ends of the housing (e.g., proximate to the ends of the solid plates).
Some embodiments may comprise at least partially charging and/or discharging electrochemical cells in a battery pack, such that the electrochemical cells undergo a cumulative expansion during the charging and/or discharging. The cumulative expansion of the electrochemical cells refers to the sum of the changes in thicknesses of the electrochemical cells themselves, not counting any other components of the battery pack (e.g., foams, sensors, plates, etc.). For example, referring to
It has been observed that the expansion of at least some electrochemical cells (e.g., some electrochemical cells comprising lithium metal and/or a lithium metal alloy as an anode active material) is equal to 0.055 mm/Ah multiplied by the capacity of the cell in Ah. For example, such a 20 Ah cell will expand 1.1 mm because (0.055 mm/Ah)×(20 Ah)=1.1 mm. As another example, a 6 Ah cell will expand 0.33 mm because (0.055 mm/Ah)×(6 Ah)=0.33 mm. From this expansion relationship, it can be determined that in some instances the cumulative expansion of the electrochemical cells in a battery pack will be equal to the number of cells in the stack multiplied by 0.055 mm/Ah multiplied by the capacity of the cell in Ah. For example, a battery pack having 12 electrochemical cells each having a 20 Ah capacity may have a cumulative expansion of 13.2 mm because 12×(0.055 mm/Ah)×(20 Ah)=13.2 mm. As another example, a battery pack having 48 electrochemical cells each having a 20 Ah capacity may have a cumulative expansion of 52.8 mm because 48×(0.055 mm/Ah)×(20 Ah)=52.8 mm.
In some embodiments, the electrochemical cells of the battery pack undergo a cumulative expansion during the charging and/or discharging of at least 10%, at least 15%, at least 20%, and/or up to 30% or more, while an expansion of the battery pack during the charging and/or discharging is less than or equal to 0.75%, less than or equal to 0.5%, less than or equal to 0.1%, and/or as low as 0.05%. In some embodiments, the electrochemical cells undergo a cumulative expansion during the charging and/or discharging, wherein a ratio of the cumulative expansion of the electrochemical cells to an expansion of the battery pack is greater than or equal to the total number of electrochemical cells in the battery pack. For example, a battery pack comprising 12 electrochemical cells may undergo a cumulative expansion of 13 mm, and the battery pack may undergo an expansion of 0.9 mm, and therefore the ratio of the cumulative expansion of the electrochemical cells to the expansion of the battery pack is 13 divided by 0.9=14.4, which is greater than the number of electrochemical cells in the battery pack (12). In some embodiments, the electrochemical cells undergo a cumulative expansion during the charging and/or discharging of greater than or equal to 0.3 mm, greater than or equal to 0.5 mm, greater than 1 mm, greater than or equal to 1.1, greater than or equal to 1.2 mm, greater than or equal to 1.5 mm, greater than or equal to 2 mm, greater than or equal to 5 mm, greater than or equal to 10 mm, greater than or equal to 12 mm, greater than or equal to 20 mm, greater than or equal to 30 mm, greater than or equal to 40 mm, greater than or equal to 50 mm, and/or up to 60 mm, up to 80 mm, up to 100 mm or more, and an expansion of the battery pack during the charging and/or discharging is less than or equal to 1 mm, less than or equal to 0.75 mm, less than or equal to 0.5 mm, and/or as low as 0.2 mm, as low as 0.1 mm, or less. It should be understood that in some embodiments, the cumulative expansion of the electrochemical cells may be in any of the above-mentioned ranges, while the battery pack does not expand at all. For example, in some embodiments, one or more components of the battery pack (e.g., a compressible component such as a thermally insulating compressible solid article portion) may absorb the expansion by compressing to an equal extent. In some embodiments, during the cumulative expansion of the electrochemical cells, each electrochemical cell expands by at least 1 mm. In some embodiments, the cumulative expansion of the electrochemical cells is at least 12 mm. In some embodiments, the cumulative expansion of the electrochemical cells is at least 24 mm. In some embodiments, the cumulative expansion of the electrochemical cells is at least 36 mm. In some embodiments, the cumulative expansion of the electrochemical cells is at least 52 mm.
In some embodiments, the battery pack has a relatively small volume. It has been discovered that certain aspects described herein, alone or in combination, such as the solid plates comprising carbon fiber, the thermally insulating compressible solid article portions, and the thermally conductive solid article portions, can allow for relatively high magnitudes of force and/or relatively high energy densities for the battery pack, even with a relatively small volume. In some embodiments, the battery pack has a volume of less than or equal to 15000 cm3, less than or equal to 13500 cm3, less than or equal to 12000 cm3, less than or equal to 10000 cm3, less than or equal to 8000 cm3, less than or equal to 6750 cm3, less than or equal to 6000 cm3, less than or equal to 5000 cm3, and/or as low as 4000 cm3, or lower. As described in more detail below, certain configurations of the housing may provide for an ability to enclose a relatively large amount of electrochemical cell volume and/or apply relatively high force while having a relatively small housing volume.
In some embodiments, the battery pack has a relatively high energy density, as described above. In some embodiments, the battery pack has a specific energy of greater than or equal to 250 Wh/kg. In some embodiments, the battery pack has a specific energy of greater than or equal to 280 Wh/kg, greater than or equal to 290 Wh/kg, greater than or equal to 300 Wh/kg, and/or up to 320 Wh/kg, up to 350 Wh/kg, or more. In some embodiments, the battery pack has a volumetric density of greater than or equal to 230 Wh/L, greater than or equal to 250 Wh/L, greater than or equal to 280 Wh/L, and/or up to 300 Wh/L, or higher.
The battery pack may, surprisingly, have a relatively high energy density and/or apply a relatively high magnitude of force while having a relatively low pack burden (defined as one minus the mass of the electrochemical cells of the battery pack divided by the total mass of the battery pack). Expressed as an equation, pack burden=1−(mass of the electrochemical cells/mass of the battery pack). In some embodiments, the battery pack has a pack burden of less than or equal to 50%, less than or equal to 45%, less than or equal to 40%, less than or equal to 35%, less than or equal to 30%, and/or as low as 25%, as low as 20%, or lower.
In some embodiments, the battery pack includes components configured such that the battery pack (or portions of the battery pack) has a relatively low volume for a given size of electrochemical cells, compared to other configurations. Having a relatively low housing volume while having relatively large electrochemical active regions of cells may afford relatively large volumetric energy densities. Relatively large volumetric energy densities may be advantageous in certain applications where limited space for battery packs is available, but where a large amount of stored energy may be desired, such as certain battery-powered vehicles. It has been realized that certain existing housings configured to apply anisotropic forces may have arrangements or operate under mechanisms that require relatively large spatial profiles. For example, housings configured to apply anisotropic forces to electrochemical cells via solid plates generally include fasteners spanning between solid plates. Tension in the fasteners may contribute some or all of the force applied to the cells within the housings. The battery pack in
In some embodiments, the battery pack comprises a stack comprising electrochemical cells (e.g., the first electrochemical cell, the second electrochemical cell). It should be understood that the stack may be a multicomponent stack comprising non-cell components such as thermally insulating compressible solid article portions, thermally conductive solid article portions, and/or sensors. The stack may be at least partially enclosed by a housing comprising a solid plate. The solid plate may cover at least a portion (e.g., at least 10%, at least 25%, at least 50%, at least 75%, at least 90%, at least 95%, or all) of an end of the stack. A portion of a surface (e.g., an end of a stack) of an object is considered covered by a second object in this context if there exists a line perpendicular to and extending out of the portion of the surface and away from a bulk of the object that intersects any of the second object. Those of ordinary skill in the art will appreciate that any stack of components (e.g., cells) includes two ends: the first end corresponds to the external surface of the first component (e.g., first cell) that faces away from the bulk of the stack, and the second end corresponds to the external surface of the last component (e.g., last cell) that faces away from the bulk of the stack. In the schematic cross-sectional illustration in
In some embodiments, the housing of the battery pack further comprises a solid housing component coupled to the solid plate. In some embodiments, the solid housing component is a discrete object separate from the solid plate rather than part of a unitary object with the solid plate (though in some embodiments the solid housing component and the solid plate are part of a unitary solid object). The solid housing component (e.g., discrete solid housing component) may contribute, at least in part, to application of anisotropic force by the housing (e.g., to an electrochemical cell in the stack). For example, in some embodiments, the housing is configured to apply, via the solid plate and tension in the solid housing component coupled to the solid plate, during at least one period of time during charge and/or discharge of the first electrochemical cell and/or the second electrochemical cell, an anisotropic force with a component normal to a first electrode active surface of the first electrochemical cell and/or a second electrode active surface of the second electrochemical cell. As noted above, the anisotropic force may define a pressure of at least 3 kgf/cm2, at least 5 kgf/cm2, at least 8 kgf/cm2, at least 10 kgf/cm2, at least 12 kgf/cm2, at least 20 kgf/cm2, and/or up to 25 kgf/cm2, up to 30 kgf/cm2, up to 35 kgf/cm2, up to 40 kgf/cm2, or more. The solid housing component (e.g., discrete solid housing component) may contribute to force application by being coupled to a first solid plate (covering at least a portion of a first end of the stack) and a second component of the housing covering at least a portion of a second end of the stack (e.g., a second solid plate or a part of a frame). For example, referring again to
The solid plate may have a largest lateral dimension that is relatively small with respect to an electrochemical active region of one or more of the electrochemical cells in the battery pack. Electrochemical active regions of electrochemical cells are described in more detail below in connection with
In some embodiments in which the stack comprises a first electrochemical cell comprising a first electrochemical active region and a second electrochemical cell comprising a second electrochemical active region, a ratio of the largest lateral dimension of the solid plate to the largest lateral dimension of the first electrochemical active region and/or a ratio of the largest lateral dimension of the solid plate to the largest lateral dimension of the second electrochemical active region is less than or equal to 1.5, less than or equal to 1.4, less than or equal to 1.3, less than or equal to 1.2, less than or equal to 1.1, less than or equal to 1.05, less than or equal to 1.02, less than or equal to 1.01, and/or as low as 1.005, as low as 1.001, or as low as 1.
The housing of the battery pack may have a largest lateral pressure-applying dimension. A lateral pressure-applying dimension refers to a dimension of the housing parallel with the lateral exterior surfaces of components of the stack and the solid plate that corresponds to components of the housing under tension such that they participate in the application of pressure to the electrochemical cells of the stack via the anisotropic force discussed above.
The housing may have a largest lateral pressure-applying dimension that is relatively small with respect to an electrochemical active region of one or more of the electrochemical cells in the battery pack. Having a relatively small lateral pressure-applying profile of the housing may stand in contrast to certain existing pressure-applying housings having larger lateral pressure-applying profiles (e.g., due to lateral space needed for load-applying fasteners to pass through one or more components of the housing such as a solid plate). Certain embodiments of this disclosure are directed to various techniques and configurations that can make housings having relatively small lateral pressure-applying profiles practical (e.g., via certain configurations of solid housing components). Small pressure-applying regions of housings (relative to the electrochemical cells) may afford overall battery packs having relatively small volumes, which can be advantageous in some applications.
In some embodiments in which the stack comprises a first electrochemical cell comprising a first electrochemical active region and a second electrochemical cell comprising a second electrochemical active region, a ratio of the largest lateral pressure-applying dimension to the largest lateral dimension of the first electrochemical active region and/or a ratio of the largest lateral pressure-applying dimension of the solid plate to the largest lateral dimension of the second electrochemical active region is less than or equal to 1.6, less than or equal to 1.5, less than or equal to 1.4, less than or equal to 1.3, less than or equal to 1.2, less than or equal to 1.1, less than or equal to 1.05, less than or equal to 1.02, less than or equal to 1.01, and/or as low as 1.005, as low as 1.001, or as low as 1. In some embodiments, at least 90%, at least 95%, at least 99%, or all of the first electrochemical active region of the first electrochemical cell and/or the second electrochemical active region of the second electrochemical cell is covered by a portion of the housing within the largest lateral pressure-applying dimension of the housing.
The solid housing component may couple (or contribute to coupling of) the solid plate covering at least a portion of a first end of the stack to a component of the housing covering at least a portion of second end of the stack. Such a coupling via the solid housing component (e.g., solid housing component 314) may contribute to the anisotropic force applied by the housing. In some embodiments, the solid housing component spans from the solid plate to the second end of the stack. For example, in
Solid housing components may join two or more parts of the housing via any of a variety of coupling techniques. The solid housing components may be part of the underlying structure of the housing. For example, in some embodiments, the housing comprises a frame at least partially enclosing the stack, and a solid housing component is a part of the frame (e.g., a side of the frame joining two ends of the frame).
In some embodiments, a housing has spaces lacking solid material (e.g., along a portion of a solid housing component). For example, in
The housing may have a single solid housing component, or the housing may comprise multiple solid housing components. In some embodiments, the housing comprises a first solid housing component along a first side of the stack and a second solid housing component on along a second (e.g., opposite) side of the stack. Housing 302 in
In some embodiments, no auxiliary fastener spanning from the solid plate toward the second end of the stack along a side of the stack is in tension during application of the anisotropic force. An auxiliary fastener in this context is a fastener that is not part of the underlying housing structure. For example, in
The solid housing component may be made of any of a variety of materials, depending on desired properties of the solid housing component and/or the overall battery pack. The solid housing component may be made of any of the materials described above for the solid plate. In some embodiments, the solid housing component comprises a metal (e.g., aluminum, titanium, etc.), metal alloy (e.g., stainless steel), composite, polymeric material (e.g., a rigid plastic), or combination thereof. For example, some (e.g., at least 50 wt %, at least 75 wt %, at least 90 wt %, at least 95 wt %, at least 99 wt %) or all of the solid housing component may be metal, metal alloy, polymeric material, composite, or a combination thereof. In some embodiments, the solid housing component comprises a composite material. Exemplary composite materials that the solid housing component can be or comprise include, but are not limited to, reinforced polymeric, metallic, or ceramic materials (e.g., fiber-reinforced composite materials), carbon-containing composites, or combinations thereof. For example, in some embodiments, the solid housing component comprises carbon fiber. As described above in the context of the solid plate, the solid housing component may comprise multiple layers of carbon fiber (e.g., unidirectional carbon fiber weaves, optionally with binder). In some embodiments, the solid housing component comprises multiple layers of carbon fiber (e.g., unidirectional carbon fiber) having any of the orientation patterns described above (e.g., a “[0°/90°/0° ]” pattern, a “[0°/30°/0°/−30/0°]” pattern, etc.). In some embodiments, the solid housing component comprises a woven fabric. For example, the solid housing component may comprise multiple layers of woven fabric (e.g., woven carbon fibers). In some embodiments, the solid housing component comprises multiple layers of material such as woven fabric (e.g., woven carbon fiber), with at least two adjacent layers having a same or different weave pattern. In some such embodiments, the at least two adjacent layers with the same or different weave pattern are rotated with respect to each other (e.g., at an angle greater than 0°, greater than or equal to 15°, greater than or equal to 30°, greater than or equal to 45°, greater than or equal to 60°, greater than or equal to 90°, greater than or equal to 180°, or more). It has been observed that carbon fiber composite solid housing components may afford sufficient strength and rigidity for contributing to application of anisotropic force to cells in the stack while being relatively light-weight, which may promote desirable specific energy densities for certain applications. In some embodiments where a housing comprises a solid plate and a solid housing component coupled to the solid plate, the solid plate and the solid housing component have the same composition. For example, both may be made of the same metal or metal alloy (e.g., aluminum), polymeric material, composite (e.g., carbon fiber composite), or combination thereof. However, in some embodiments the solid plate and the solid housing component are made of different compositions (e.g., different types of materials or the same materials in different relative amounts).
In some embodiments, the solid housing component comprises a material (e.g., a composite comprising carbon fiber) having a relatively high modulus. In some embodiments, the solid housing component has a relatively high tensile modulus and a relatively high flexural modulus. In some embodiments, some or all of the solid housing component has a tensile modulus of at least 1 GPa, at least 5 GPa, at least 10 GPa, at least 20 GPa, at least 50 GPa, at least 75 GPa, at least 100 GPa, 120 GPa, at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa and/or up to 550 GPa, up to 600 GPa, up to 650 GPa, or greater, and a flexural modulus of at least 120 GPa at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa and/or up to 550 GPa, up to 600 GPa, up to 650 GPa, or greater at room temperature (25° C.). For example, in some embodiments the solid housing component comprises layers comprising a material (e.g., a composite comprising carbon fiber), and one or more of the layers has a relatively high tensile modulus and a relatively high flexural modulus. In some embodiments, the solid housing component comprises layers comprising a material (e.g., a composite comprising carbon fiber), one or more of the layers having a tensile modulus of at least 120 GPa, at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa or greater, and a flexural modulus of at least 120 GPa at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa, or greater at room temperature (25° C.). In some embodiments, the solid housing component comprises layers comprising a material (e.g., a composite comprising carbon fiber), one or more of the layers having a tensile modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa, or less, and a flexural modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa, or less at room temperature (25° C.). Combinations of the ranges (e.g., a tensile modulus of at least 120 GPa and less than or equal to 650 GPa and a flexural modulus of at least 120 GPa and less than or equal to 650 GPa) are possible. In certain instances, the solid housing component has a relatively large number of layers satisfying the modulus ranges above. For example, in some embodiments, the solid housing component comprises at least 1, at least 2, at least 3, at least 5, at least 10, at least 15, and/or up to 20, up to 25, up to 50, up to 60, up to 75, or more layers comprising a material (e.g., a composite comprising carbon fiber) having a tensile modulus of at least 120 GPa, at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa or greater, and a flexural modulus of at least 120 GPa at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa or greater at room temperature (25° C.). In some embodiments, the solid housing component comprises at least 1, at least 2, at least 3, at least 5, at least 10, at least 15, and/or up to 20, up to 25, up to 50, up to 60, up to 75, or more layers comprising a material (e.g., a composite comprising carbon fiber) having a tensile modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa or less, and a flexural modulus of less than or equal to 650 GPa, less than or equal to 600 GPa, less than or equal to 550 GPa or less at room temperature (25° C.).
In some embodiments, a substantial portion of the housing comprises a material (e.g., a composite comprising carbon fiber) having a relatively high modulus. In some embodiments, a material having a flexural and/or tensile modulus of at least 120 GPa, at least 150 GPa, at least 200 GPa, at least 300 GPa, at least 500 GPa, and/or up to 550 GPa, up to 600 GPa, up to 650 GPa, or higher is present in the housing in an amount of at least 50 wt %, at least 75 wt %, at least 90 wt %, at least 95 wt %, or more. Some embodiments where the housing comprises a material having a relatively high modulus may be advantageous because they facilitate battery packs with a relatively small lateral profile, a relatively high volumetric energy density, and/or adequate resistance to deformation (e.g., upon application of force). In some embodiments where the housing comprises a solid plate and a solid housing component, each comprising a composite material having a relatively high modulus, such as a composite comprising carbon fiber, it can be beneficial to have some housing components with planarity parallel to a first plane and other housing components with planarity not parallel to that first plane. For example, in some embodiments it may be advantageous for a solid plate of the housing to have multiple layers of unidirectional carbon fiber having planarity parallel to a plane of the solid plate, as well as a solid housing component (e.g., a frame component spanning from the solid plate to a second end of the stack) having multiple layers of unidirectional carbon fiber with planarity nonparallel to (e.g., substantially perpendicular to) the plane of the solid plate.
While in some embodiments the solid housing component has a relatively high modulus, such a property is not necessary in all embodiments. In some embodiments, the solid housing component has a tensile strength sufficient to avoid observable deflection and/or failure when the housing applies the anisotropic force to the electrochemical cells. In some embodiments, the solid housing component has a tensile strength in at least one dimension of at least 10 MPa, at least 20 MPa, at least 50 MPa, at least 100 MPa, at least 200 MPa, at least 500 MPa, at least 1 GPa, at least 2 GPa, at least 5 GPa, and/or up to 10 GPa, up to 20 GPa, up to 50 GPa, up to 100 GPa, up to 120 GPa, or higher.
In some embodiments, components of the housing of the battery pack are reinforced by local increases in thickness and/or the attachment of mechanical doublers. In some embodiments, local increases in thickness and/or the attachment of mechanical doublers provide additional support for portions of the housing (e.g., solid housing components along a side of the stack) that are pressure-applying or are otherwise mechanically loaded under at least some configurations of the housing. In some embodiments, local increases in thickness and/or the attachment of mechanical doublers facilitate a reduction in the largest lateral pressure applying dimension of the housing and/or increase the gravimetric and/or volumetric energy density of the battery pack. A local increase in thickness or a mechanical doubler may have an area of less than 100%, less than or equal to 90%, less than or equal to 75%, less than or equal to 50%, less than or equal to 25%, less than or equal to 10%, less than or equal to 5%, or less of a corresponding solid housing component. Further, a thickness of the solid housing component at a local increase in thickness and/or a combined thickness of a solid housing component and a mechanical doubler may be greater than an average thickness of the solid housing component by a factor of greater than or equal to 1.05, greater than or equal to 1.1, greater than or equal to 1.25, greater than or equal to 1.5, greater than or equal to 2, and/or up to 3, up to 5, or greater.
The solid housing component may have any of a variety of lengths while maintaining rigidity. In some embodiments, such a rigidity even at relatively long lengths (unlike traditional auxiliary fasteners) affords an ability for the ratio of the distance between a solid plate and the second end of the stack to the largest lateral dimension of the housing to be relatively large if desired. In turn, such a large ratio may allow for a relatively large number (e.g., at least 6, at least 12, at least 18, at least 24, at least 30, at least 36, or more) of electrochemical cells to be included in the stack of the battery pack. Such an ability for relatively long housing components spanning the stack stands in contrast to traditional auxiliary fasteners such as rods or bolts with nuts. Tension in long fasteners may produce bending moments that result in deleterious deflection. Solid housing components (e.g., comprising composites comprising carbon fiber) may not appreciably deflect under such tension. In some embodiments, the ratio of the distance between a solid plate and the second end of the stack to the largest lateral dimension of the battery pack is less than or equal to 20, less than or equal to 10, less than or equal to 5, less than or equal to 2, less than or equal to 1.5, less than or equal to 1, less than or equal to 0.5, less than or equal to 0.2, less than or equal to 0.1, or less. In some embodiments, the ratio of the distance between a solid plate and the second end of the stack to the largest lateral dimension of the battery pack is greater than or equal to 0.01, greater than or equal to 0.1, greater than or equal to 0.5, greater than or equal 1, greater than or equal to 2, greater than or equal to 5, or greater. Combinations of the above ranges are possible: for instance, in some embodiments, the ratio of the distance between a solid plate and the second end of the stack to the largest lateral dimension of the battery pack is greater than or equal to 0.01 and less than or equal to 20.
In some embodiments, housings with any given ratio of the distance between a solid plate and the second end of the stack to the largest lateral dimension of the housing can be reconfigured to have a new ratio of the distance between the solid plate and the second end of the stack to largest lateral dimension of the battery pack by modifying and/or adjusting one or more solid housing components of the housing. For a given collection of geometries, a variety of solid housing components for spanning along a side of the stack of the battery pack can be interchanged to accommodate a variety of ratios of the distance between a solid plate and the second end of the stack to the largest lateral pressure-applying dimension, in some embodiments. In some embodiments, the ability to reconfigure the length of the housing without the adjustment of auxiliary fasteners can facilitate a reduction in the largest lateral pressure applying dimension of the battery pack. In some embodiments, the ability to reconfigure the length of the housing in such a way advantageously reduces the number of parts of the housing.
In some embodiments, the housing comprises a lateral base portion proximate to and/or along a lateral edge of the solid plate. In some embodiments, the lateral base portion is part of the solid plate. However, in some embodiments, the lateral base portion is part of a solid housing component coupled to the solid plate. In some embodiments, battery packs can be mounted to an external surface using fasteners (e.g., auxiliary fasteners). In some embodiments, the lateral base portion is configured for mounting the battery pack to an external surface. For battery packs that lack a lateral base portion, additional portions of the solid plate may be required to mount the battery pack to an external surface, and these may increase the lateral profile of the battery pack. Therefore, inclusion of a lateral base portion may be advantageous for reducing the maximum lateral pressure-applying dimension of the housing and/or increasing the battery pack's volumetric energy density. For example, battery pack 100 in
In some embodiments, a relatively large percentage of the stack of the battery pack is covered by the housing of the battery pack. This may, in some cases, be advantageous because it can afford substantial protection to the battery pack (e.g., from impact during handling and/or use). In some embodiments, the housing covers at least 30%, at least 50%, at least 70%, at least 90%, at least 95%, at least 99%, or 100% of an external surface area of the stack.
The solid housing component may couple to the solid plate of the housing in any of a variety of suitable ways. It has been realized that certain coupling techniques may establish coupling while maintaining relatively small lateral profiles for the housing. In some embodiments, mechanically interlocking features of the solid housing component and a lateral edge of the solid plate establish a joint. Any of a variety of suitable joints may be employed via the interlocking features. For example, any of a variety of woodworking joints may be suitable. It should be understood that woodworking joints refer to the geometries and balances of forces associated with the joints, and it is not required that any part of two components joined with a woodworking joint actually be made of wood. Examples of types of joints that may be established by interlocking features of the solid housing component and a lateral edge of the solid plate include, but are not limited to, box joints, dovetail joints, splice joints (e.g. tabled splice joints), and Knapp joints.
In some embodiments, a joint between the solid housing components and the solid plate of the housing is formed at least in part between a projection of the solid housing component (or solid plate) and a recess of the solid plate (or solid housing component). Some such embodiments may involve the solid housing comprising a projection, the solid plate comprising a recess, and the solid housing component and the solid plate being configured to form a joint at least in part via coupling of the projection and the recess. For example, referring to
In some embodiments, the solid housing component is coupled to the solid plate via coupling to a housing stop portion adjacent to an exterior surface of the solid plate. The housing stop portion may be directly adjacent to the exterior surface of the solid plate (a surface of the plate facing away from the stack). However, in some embodiments, the housing stop portion is indirectly adjacent to the exterior surface of the solid plate such that one or more intervening components (e.g., washers, layers of material, etc.) is between the housing stop portion and the exterior surface of the solid plate. The housing stop portion may be discrete from the solid housing component and/or the solid plate. The housing stop portion may be made of any of a variety of materials, such as a metal (e.g., aluminum or titanium), a metal alloy (e.g., stainless steel), a composite (e.g., carbon fiber), a polymeric material (e.g., a rigid plastic), or a combination thereof. The housing stop portion may have any of a variety of shapes depending on, for example, a desired deflection of the solid plate and/or pressure distribution within the battery pack. It has been realized that some shapes of housing stop portions (e.g., elongated bars, or rings (e.g., rectangular or non-rectangular rings) conforming to a perimeter of the solid plate) can distribute force (e.g., from tension in the solid housing component) across the face of the solid plate more uniformly than, for example, solid plates coupled via discrete auxiliary fasteners (e.g., bolts with nuts) in contact with relatively small areas of the solid plate.
The stop portion may have any of a variety of configurations.
In some embodiments, the solid housing component is coupled to the solid plate at least partially via coupling of an insert to a housing stop portion adjacent to an exterior surface of the solid plate. As mentioned above, in some embodiments, the stop portion is coupled to the solid housing component at least in part via an insert. The insert may have a shape complementary to a recess of the stop portion.
In some embodiments in which the solid housing component is coupled to the solid plate at least partially via coupling of an insert to a housing stop portion adjacent (e.g., directly adjacent) to an exterior surface of the solid plate, the housing stop portion is also adjacent (e.g., directly adjacent) to at least one other surface of the solid plate. The other surface may be, for example, a lateral edge surface. As one example, in some embodiments, the housing stop portion is in the form of a bracket. The bracket may couple to an edge of the solid plate that is proximal to the solid housing component to which the solid plate is coupled. As a result, the bracket may be adjacent to both the exterior surface of the solid plate (with respect to the housing) and the lateral edge surface of the solid plate proximal to the solid housing component.
In some embodiments where the housing stop portion comprises recesses complementary to the inserts, the recesses are located on a region of the housing stop portion adjacent to the lateral edge surface of the solid plate.
For some embodiments in which the housing stop portion is adjacent to multiple sides of the solid plate (e.g., as in
Referring to
The solid housing component may be coupled to the housing stop portion via any of a variety of suitable techniques. For example, the solid housing component may be coupled to the housing stop portion via a weld, a fastener, an adhesive, or a combination thereof. As mentioned above, the coupling of the housing stop portion to the solid housing component may be at least partially via an insert.
In some embodiments, the solid housing component is coupled to the solid plate via a lateral portion of the solid housing component adjacent to an exterior surface of the solid plate. A lateral portion of the solid housing component refers to one which can be substantially parallel to a lateral surface of the solid plate when the solid housing component and the solid plate are coupled in the housing of the battery pack. For example, referring to
The lateral portion of the solid housing component may have any of a variety of shapes depending on, for example, a desired deflection of the solid plate and/or pressure distribution within the battery pack. It has been realized that some shapes of lateral portions (e.g., relatively flat portions) can distribute force (e.g., from tension in the solid housing component) across the face of the solid plate more uniformly than, for example, solid plates coupled via discrete auxiliary fasteners (e.g., bolts with nuts) in contact with relatively small areas of the solid plate. A housing of this type may, in some embodiments, decrease a largest lateral pressure-applying dimension of the housing relative to a housing comprising, for example, auxiliary fasteners coupling solid plates.
The lateral portion of the solid housing component may be directly adjacent to the exterior surface of the solid plate (a surface of the plate facing away from the stack). However, in some embodiments, the lateral portion is indirectly adjacent to the exterior surface of the solid plate such that one or more intervening components (e.g., washers, layers of material, etc.) is between the lateral portion of the solid housing component and the exterior surface of the solid plate. In some embodiments, the lateral portion of the solid housing component and a remainder of the solid housing component form a unitary object.
In some embodiments, the battery pack further comprises a contoured solid article portion between a lateral exterior surface of the first electrochemical cell and a portion of the housing. The contoured solid article portion may comprise a surface adjacent (e.g., directly adjacent or indirectly adjacent) to the lateral exterior surface of the first electrochemical cell that is convex with respect to the lateral exterior surface in the absence of an applied force. In some embodiments, under at least one magnitude of applied force, the surface of the contoured solid article portion becomes less convex. Further description of contoured surfaces and related devices and methods is provided in International Patent Application Publication No. WO2020/257414, filed as International Patent Application No. PCT/US2020/038375 on Jun. 18, 2020, and entitled “METHODS, SYSTEMS, AND DEVICES FOR APPLYING FORCES TO ELECTROCHEMICAL DEVICES” and U.S. patent application Ser. No. 16/952,177, filed Nov. 19, 2020, and entitled “BATTERIES, AND ASSOCIATED SYSTEMS AND METHODS,” each which is incorporated herein by reference in its entirety for all purposes.
In some embodiments, the battery pack is a single battery having only a single pair of terminals (a positive terminal and a negative terminal) electronically coupled to the electrochemical cells of the battery. However, in some embodiments, the battery pack comprises multiple batteries at least partially enclosed by the housing. For example, the battery pack may comprise a first battery having a first electrochemical cell and a second battery having a second electrochemical cell, where both the first electrochemical cell and the second electrochemical cell are at least partially enclosed by a same housing of the battery pack. Each of the multiple batteries may operate as an independent battery by having its own pair of terminals (a positive terminal and a negative terminal) electronically coupled to the electrochemical cells of that battery within the battery pack. Further, in some embodiments, the same housing is configured to apply an anisotropic force having a component normal to an electrode active surface of the first electrochemical cell of the first battery and/or an electrode active surface of the second electrochemical cell of the second battery (e.g., during a least a portion of a discharging and/or charging process). It has been realized that applications of battery-powered electricity may require different batteries with different battery parameters (e.g., voltages, currents, charge/discharge rates) for different aspects of the application. However, it has further been realized in the context of this disclosure that efficiencies in space utilization and ease of incorporation into devices can be realized if multiple different batteries (e.g., with different battery parameters) are present in a single battery pack instead of in separate battery packs. For example, having multiple batteries within the same housing of a battery pack can allow for simultaneous application of force to the electrochemical cells of each of the multiple batteries rather than supplying force-applicating apparatuses for each battery separately. There is no practical limit to the number of batteries (e.g., battery modules) the battery pack may comprise at least partially enclosed by the housing. In some embodiments, the battery pack comprises at least 2, at least 3, at least 4, at least 5, and/or up to 10 batteries or more at least partially enclosed by the housing.
As an illustrative example,
In some embodiments the battery pack comprises multiple different batteries as multiple different battery modules, each battery module comprising multiple electrochemical cells. The battery modules may be at least partially enclosed by the housing of the battery pack. For example, in some embodiments in which a battery pack comprises a stack of electrochemical cells (e.g., at least partially enclosed by a housing), a first battery of the battery pack comprises a first battery module comprising a subset of the electrochemical cells and a second battery of the battery pack comprises a second battery module comprising a, different subset of the electrochemical cells. Each of the multiple battery modules may operate as an independent battery by having its own pair of terminals (a positive terminal and a negative terminal) electronically coupled to the electrochemical cells of that battery module. Referring to
In some embodiments, the first battery is configured to be part of a circuit having a first voltage, and the second battery is configured to be part of a circuit having a second, different voltage.
In some embodiments, a first battery module of the battery pack has a different number of electrochemical cells than does a second battery module of the battery pack. Having different numbers of electrochemical cells (which may each be a same type of electrochemical cell) for different batteries may provide for batteries modules with different battery parameters. For example, a voltage of a battery may depend at least in part on a number of electrochemical cells electronically coupled to a circuit in series. Therefore, different battery modules of the battery pack having different numbers of electrochemical cells in series will have different battery voltages. Such a battery pack configuration may be useful in instances where it is desirable for a single battery pack to power different components with different voltage requirements without requiring reconfiguration of the battery pack. As an illustrative example, in
It should be understood that while each electrochemical cell of each battery (e.g., battery module) of the battery pack may be a same type of electrochemical cell having a same battery chemistry (e.g., same anode active material and same cathode active material), other embodiments are possible. For example, at least some of the electrochemical cells of a first battery module of the battery pack may have a different battery chemistry (e.g., a different anode active material and/or a different cathode active material) than at least some of the electrochemical cells of a second battery module of the battery pack. Battery modules having electrochemical cells with differing battery chemistries may result in the different battery modules of the battery pack having different voltages, which may be desirable in some applications where the different uses of the different battery modules have different voltage requirements. In some embodiments where the first battery is configured to be part of a circuit having a first voltage, and the second battery is configured to be part of a circuit having a second, different voltage, the first battery has the same number of electrochemical cells as the second battery, but at least one electrochemical cell of the first battery has a different cell voltage than an electrochemical cell of the second battery (e.g., due to different cell chemistries).
It should also be understood that while each electrochemical cell of each battery (e.g., battery module) of the battery pack may be a same type of electrochemical cell having a same capacity, other embodiments are possible. For example, at least some of the electrochemical cells of a first battery module of the battery pack may have a different capacity than at least some of the electrochemical cells of a second battery module of the battery pack. For example, the first electrochemical cell of the first battery (e.g., first electrochemical cell 110 of first battery 191) may have a different capacity than the second electrochemical cell of the second battery (e.g., second electrochemical cell 120 of second battery 192) of the battery pack.
While
As mentioned above, the battery pack may comprise components having a potentially advantageous arrangement (e.g., for thermal management). For example, in some embodiments, a multicomponent stack is described comprising electrochemical cells, thermally conductive solid article portions, and thermally insulating compressible solid article portions. The multicomponent stack or stack of electrochemical cells may be part of a battery pack described herein. In some embodiments, a multicomponent stack comprises the following in the order listed: a first electrochemical cell; a thermally conductive solid article portion; and a thermally insulating compressible solid article portion. In some embodiments, a multicomponent stack comprises the following in the order listed: an electrochemical cell; a first thermally conductive solid article portion; a thermally insulating compressible solid article portion; a second thermally conductive solid article portion; and a second electrochemical cell. For example, referring to
In some embodiments, the arrangement of components of the battery pack may be repeated. For example, in
In some embodiments, a multicomponent stack comprises the following in the order listed: a first electrochemical cell; a thermally conductive solid article portion; a thermally insulating compressible solid article portion, and a second electrochemical cell. For example,
The abovementioned arrangements of thermally conductive and thermally insulating components may facilitate relatively rapid transfer of heat away from electrochemical cells in the stack while mitigating thermal transfer between electrochemical cells of the stack. For example, battery pack 100 may have a relatively low rate of thermal transfer in thickness direction 153 shown in
As mentioned above, some embodiments may comprise application of an anisotropic force (e.g., via a solid plate).
In some embodiments, the battery pack comprises thermally conductive solid article portions. For example, referring back to
In some embodiments, the thermally conductive solid article portion of the battery pack has a relatively high effective thermal conductivity. As mentioned above, such a high effective thermal conductivity may allow the thermally conductive solid article to assist with dissipating heat from one or more electrochemical cells of the battery pack. Thermal conductivity is generally understood to be an intrinsic property of a material related to its ability to conduct heat. Thermal conductivity is a temperature-dependent quantity and is typically reported in units of W m−1 K−1. The effective thermal conductivity of an article generally refers to the ability of an article to conduct heat, taking into account that the article may be made of a single material or may a non-homogeneous material that may be made of a combination of materials (e.g., a composite material such as a particulate material or layered material). An exemplary method for measuring the thermal conductivity or effective thermal conductivity of a thermally insulating compressible solid article portion is using a hot disk method, as described in ISO/DIS 22007-2.2.
In some embodiments, a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) has a relatively high effective thermal conductivity in an in-plane direction. Referring again to
The thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) may comprise any of a variety of suitable materials. In some embodiments, a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) comprises a metal and/or metal alloy. Exemplary metals include, but are not limited to transition metals (e.g., titanium, manganese, iron, nickel, copper, zinc), non-transition metals (e.g., aluminum), and alloys or other combinations thereof. In certain embodiments, a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) comprises or is made of aluminum, at least because aluminum has a relatively high effective thermal conductivity and a relatively low mass density, which in some cases contributes to an overall high specific energy density for the battery pack. One exemplary type of aluminum material of which a thermally conductive solid article portion may be made is 3003 H14 series aluminum, which is aluminum alloyed with 1.2% manganese to increase strength. In some embodiments, a relatively high percentage (e.g., greater than or equal to 50 weight percent (wt %), greater than or equal to 75 wt %, greater than or equal to 90 wt %, greater than or equal to 95 wt %, greater than or equal to 99 wt %, or more) of the thermally conductive solid article portion is metal and/or metal alloy.
In some embodiments, the thermally conductive solid article portion comprises or is made of a carbon-based material. Suitable carbon-based materials include, but are not limited to, graphite, carbon-fiber, graphene (e.g., as part of thermally conductive solid article comprising a solid substrate and associated with graphene), and combinations thereof. In some embodiments, the carbon-based material is present in a relatively high percentage (e.g., greater than or equal to 50 wt %, greater than or equal to 75 wt %, greater than or equal to 90 wt %, greater than or equal to 95 wt %, greater than or equal to 99 wt %, or more) of the thermally conductive solid article portion. In some embodiments, a carbon-based material of a thermally conductive solid article portion has graphite, carbon-fiber, graphene, or a combination thereof present in an amount of at least 25 wt %, at least 50 wt %, at least 75 wt %, at least 90 wt %, at least 95 wt %, at least 99 wt %, or 100 wt %.
The thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) may have any of a variety of form factors. In some embodiments, the thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) is in the form of a relatively planar object (notwithstanding the non-planarities and/or alignment features described below). For example, the thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) may be in the form of a sheet (e.g., a metal and/or metal alloy sheet). In some embodiments, the thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) is or comprises a fin (e.g., a metal and/or metal alloy fin). In some embodiments, the thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) is or comprises a solid plate. It should be understood that the surfaces of a sheet, fin, or solid plate do not necessarily need to be flat. For example, one of the sides of a sheet, fin, or solid plate could have any of the non-planarities and/or alignment features described herein.
The thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) may have a thickness as well as two orthogonal lateral dimensions that are orthogonal to each other as well as orthogonal to the thickness. For example, referring to
The dimensions of the thermally conductive solid article portion may be chosen based on any of a variety of considerations. For example, the thickness or lateral dimensions may be chosen based on the desired total size of the battery pack and/or a desired pack burden. In some embodiments, one or more lateral dimensions of the thermally conductive solid article portion is such that heat generated by the electrochemical cells, once conducted to the thermally conductive solid article portions, can be transferred a relatively long distance from the electrochemical active regions of the electrochemical cells. In some embodiments, the thermally conductive solid article portion has one or more lateral dimensions that extends at least 1 mm, at least 2 mm, at least 5 mm, at least 1 cm, at least 2 cm, at least 5 cm, and/or up to 10 cm or more past the electrochemical active region of the electrochemical cell coupled to the thermally conductive solid article portion.
In some embodiments, the thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) has at least one lateral dimension that is at least 5 times, at least 10 times, and/or up to 20 times, up to 50 times, up to 100 times or more greater than the maximum thickness of the thermally conductive solid article portion.
In some embodiments, the battery pack comprises a thermally insulating compressible solid article portion. The thermally insulating compressible solid article portion may be between two electrochemical cells of the battery pack. For example, referring back to
In some embodiments, the thermally conductive solid article portion is relatively smooth as compared to the thermally insulating compressible solid article portion. This may, in some cases, be advantageous, because, under high magnitudes of force, surface irregularities in certain types of thermally insulating compressible solid article portions (e.g., microcellular foams) may cause non-uniform pressure distributions on the electrode active surfaces of the battery pack. A relatively smooth thermally conductive solid article portion (e.g., a metal sheet) may, comparatively, have few irregularities and “smooth” out the pressure distribution. As one example, in
In some embodiments, the arrangement of components of the battery pack may be repeated. For example, in
In certain aspects, battery packs with components that may facilitate alignment of electrochemical active areas are generally described.
Each of the electrochemical cells in the battery packs described herein may have an electrochemical active region. For example,
In some embodiments, an electrochemical cell of the battery pack (e.g., first electrochemical cell, second electrochemical cell) is coupled to a non-planarity of a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) of the battery pack.
As used herein, a surface is said to be “facing” an object when a line extending normal to and away from the bulk of the material comprising the surface intersects the object. For example, a first surface and a second surface can be facing each other if a line normal to the first surface and extending away from the bulk of the material comprising the first surface intersects the second surface. A surface can be facing another object when it is in contact with the other object, or when one or more intermediate materials are positioned between the surface and the other object. For example, two surfaces that are facing each other can be in contact or can include one or more intermediate materials between them. In some instances, a surface and an object (e.g., another surface) facing each other are substantially parallel. In some embodiments, two surfaces can be substantially parallel if, for example, the maximum angle defined by the two planes is less than or equal to 10°, less than or equal to 5°, less than or equal to 2°, or less than or equal to 1°.
In some embodiments, the non-planarity of a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) of the battery pack is a recess in the thermally conductive solid article portion.
An electrochemical cell may be coupled to a recess in a thermally conductive solid article portion by having a shape such that the at least a portion of the electrochemical cell can fit into the recess. For example, referring again to
In some embodiments, the non-planarity of a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) of the battery pack is a protrusion. The protrusion may extend away from the main surface of the thermally conductive solid article portion facing the electrochemical cell. For example,
An electrochemical cell may be coupled to a protrusion in a thermally conductive solid article portion by having a shape such that the electrochemical cell can fit between protrusions. For example, referring again to
A non-planarity that is protrusion may take any of a variety of forms. For example, in some embodiments, a non-planarity that is a protrusion is a raised edge in the thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion). In some embodiments a non-planarity is a plurality of posts extending from the thermally conductive solid article portion.
Non-planarities in thermally conductive solid article portions (e.g., recesses, protrusions) may be formed in any of a variety of suitable ways, such as via machining, milling, molding, additive manufacturing (e.g., 3D-printing), etc.
In some embodiments, a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) comprises an alignment feature. An alignment feature may be, for example, a structural component of the thermally conductive solid article portion that can assist with the positioning of the thermally conductive solid article portion with respect to another thermally conductive solid article portion of the battery pack. In
An alignment feature may take any of a variety of suitable structural forms. For example, in some embodiments, an alignment feature of the thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) is a gap in the thermally conductive solid article portion.
In some embodiments, a thermally conductive solid article portion comprises multiple alignment features. In certain cases, using multiple alignment features per thermally conductive solid article portion may facilitate easier and/or more accurate alignment of components of the battery pack. Referring again to
Some embodiments comprise substantially aligning a first feature (e.g., a first alignment feature) of a first thermally conductive solid article portion with a second feature (e.g., a second alignment feature) of a second thermally conductive solid article portion. Such an alignment process may result in a first electrochemical active region of a first electrochemical cell coupled to a non-planarity of the first thermally conductive solid article portion being substantially aligned with a second electrochemical active region of a second electrochemical cell coupled to a non-planarity of the second thermally conductive solid article portion. In certain cases, the first alignment feature and the second alignment feature are located such that when the first alignment feature is substantially aligned with the second alignment feature, the first electrochemical active region and the second electrochemical active region are substantially aligned. For example, in
One non-limiting way in which alignment features of thermally conductive solid article portions of the battery pack may be substantially aligned when they are gaps is by passing an object through the alignment features (e.g., through the first alignment feature and the second alignment feature). As an example, in
Some embodiments may comprise substantially aligning two or more alignment features of the first thermally conductive solid article portion with two or more features of the second thermally conductive solid article portion. For example, alignment of components of the battery pack may comprise substantially aligning the first alignment feature of the first thermally conductive solid article portion with the second alignment feature of a second thermally conductive solid article portion and substantially aligning a third alignment feature of the first thermally conductive solid article portion with a fourth alignment feature of the second thermally conductive solid article portion. Aligning multiple alignment features of each thermally conductive solid article portion, can, in some cases, increase the accuracy and/or ease with which the components of the battery pack are aligned.
Another nonlimiting way of aligning features of a battery pack is by aligning components of the battery pack with a housing of the battery pack. For instance, in some embodiments, thermally conductive solid article portions may comprise alignment features that interlock with features of the housing. For example, an alignment feature such as non-planarity (e.g. a ridge) of a solid housing component of a housing may interlock with alignment features such as grooves of the thermally conductive solid article portions. In some embodiments, alignment may be achieved without the incorporation of alignment features, due to geometric constraints imposed by the housing (e.g., by one or more solid housing components described above) on components of the battery pack. Aligning components of the battery pack with the housing may prove advantageous to some embodiments by facilitating a reduction in the number of constituent parts of the housing, reducing a largest lateral pressure applying dimension of the housing, and/or increasing the battery pack's volumetric energy density.
In some embodiments, a thermally conductive solid article portion (e.g., first thermally conductive solid article portion, second thermally conductive solid article portion) is between electrochemical cells (e.g., first electrochemical cell, second electrochemical cell) in the battery pack.
In some embodiments, the first thermally conductive solid article portion and the second thermally conductive solid article portion are part of discrete articles. Referring again to
In some aspects, battery packs comprising solid articles that can compensate for dimensional changes of other battery pack components while also limiting heat transfer between electrochemical cells are generally described.
The thermally insulating compressible solid article portion may take any of a variety forms. For example, the thermally insulating compressible solid article portion may be in the form of a solid block, a foam sheet, a mesh, or any other suitable form, provided that it be thermally insulating and compressible. It should be understood that while the thermally insulating compressible solid article portion is referred to as a solid article, it may be at least partially hollow and/or contain pores or voids.
In some embodiments, the thermally insulating compressible solid article portion is a unitary object.
In some embodiments, the thermally insulating compressible solid article portion comprises a foam. A foam solid article generally refers to a solid containing pockets of (“cells”) capable of being occupied by a fluid. The pockets may be present throughout the dimensions of the solid. The foam may be present as a relatively high percentage of the thermally insulating compressible solid article portion (e.g., greater than or equal to 50 weight percent (wt %), greater than or equal to 75 wt %, greater than or equal to 90 wt %, greater than or equal to 95 wt %, greater than or equal to 99 wt %, or more). The use of thermally insulating compressible solid article portions comprising a relatively large amount of foam may, in some cases, contribute to a relatively high compressibility of the thermally insulating compressible solid article portion. For example, referring back to
In some embodiments, the thermally insulating compressible solid article portion is or comprises a closed-cell foam. A closed-cell foam solid generally refers to a foam comprising cells (gas pockets) that are discrete and completely surrounded by the solid material of the foam.
However, in some embodiments, the thermally insulating compressible solid article portion is or comprises an open-cell foam. An open-cell foam solid generally refers to a foam comprising cells connected to each other, thereby allowing for a gas or other fluid to travel from cell to cell.
In some embodiments, thermally insulating compressible solid article portion 140 comprises a microcellular foam. A microcellular foam generally refers to a foam whose cells have an average largest cross-sectional dimension on the order of microns (e.g., greater than or equal to 0.1 micron, greater than or equal to 1 micron, and/or up to 50 microns, up to 100 microns, or up to 500 microns). For example, in embodiments in which thermally insulating compressible solid article portion 140 in
In some embodiments, the thermally insulating compressible solid article portion comprises a mesh. As an example, in certain instances, the thermally insulating compressible solid article portion is a mesh structure made of strands of flexible, thermally-insulating material (e.g., fiber, plastic) that are attached and/or woven together.
In some embodiments, the thermally insulating compressible solid article portion is porous. As one example, referring again to
The porosity of a component of a battery pack (e.g., the thermally insulating compressible solid article portion comprising open cells) may be measured by physically separating the different regions of the electrochemical device by, for example, cutting out a region of the component, and then measuring the separated portion using the above-referenced ASTM Standard Test D4284-07.
In some instances, the thermally insulating compressible solid article portion (e.g., comprising an open-cell solid such as an open-cell foam) has a relatively high porosity. Having a relatively high porosity may contribute to the thermally insulating compressible solid article portion having a relatively low density, which in some instances can be advantageous as described above. A high porosity may also contribute, in some cases, to a relatively high compressibility. In some embodiments, the thermally insulating compressible solid article portion has a porosity of greater than or equal to 40%, greater than or equal to 50%, greater than or equal to 60%, or higher by volume. In some embodiments, the thermally insulating compressible solid article portion has a porosity of less than or equal to 90%, less than or equal to 80%, less than or equal to 70%, or less by volume. Combinations of these ranges are possible. For example, in some cases, the thermally insulating compressible solid article portion has a porosity of greater than or equal to 40% and less than or equal to 90%.
The thermally insulating compressible solid article portion may have any of a variety of suitable pore sizes, depending on, for example, the choice of material for the compressible solid article portion or the magnitude of force to be applied to the battery pack. For example, in some cases, the thermally insulating compressible solid article portion has an average pore size of greater than or equal to 0.1 microns, greater than or equal to 0.5 microns, greater than or equal to one micron, greater than or equal to 10 microns, greater than or equal to 50 microns, or greater. In some cases, the thermally insulating compressible solid article portion has an average pore size of less than or equal to 1 mm, less than or equal to 500 microns, less than or equal to 100 microns, or less. Combinations of these ranges are possible. For example, in some embodiments, the thermally insulating compressible solid article portion has an average pore size of greater than or equal to 0.1 microns and less than or equal to 1 mm, or greater than or equal to 1 micron and less than or equal to 100 microns.
In some embodiments, the thermally insulating compressible solid article portion has a relatively high void percentage. The voids of a solid object in this context generally refers to portions of the solids object not occupied by solid material. Voids may be occupied by a fluid such as a gas (e.g., air) or a liquid. It should be understood that pores such as open-cells may contribute to the void percentage, and closed-cells may also contribute to void percentage. As such, a thermally insulating compressible solid article portion comprising closed cells (e.g., a closed-cell foam such as thermally insulating compressible solid article portion 140a in
As a thermal insulator, the thermally insulating compressible solid article portion may contribute at least in part to advantageous thermal management of components of the battery pack. In some embodiments, the thermally insulating compressible solid article portion has a relatively low effective thermal conductivity (consequently making it a relatively good thermal insulator). The thermal insulating capability of the thermally insulating compressible solid article portion can, in some cases, contribute at least in part to thermally isolating one or more electrochemical cells and the battery pack from one or more other portions of the battery pack. For example, referring back to
In some embodiments, the thermally insulating compressible solid article portion has a relatively low effective thermal conductivity in the thickness direction. Referring again to
The compressibility of the thermally insulating compressible solid article portion may be useful in any of a variety of applications. As one example, in some instances in which one or more components of the battery pack change dimension during a charging and/or discharge process, a resulting compression of the thermally insulating compressible solid article portion may compensate for that change in dimension. In some such cases, the compressibility of the thermally insulating compressible solid article portion under stress may reduce the extent to which a battery pack expands or contracts when electrochemical cells within the battery pack undergo expansion and/or contraction during cycling.
In some embodiments, the application of force to the thermally insulating compressible solid article portion (e.g., via the first electrochemical cell and/or the second electrochemical cell or an intervening battery pack component) causes the thermally insulating compressible solid article portion to compress in the thickness direction. Referring again to
In some embodiments, the thermally insulating compressible solid article portion has a relatively low compression set. The compression set of an article generally refers to the amount of permanent (plastic) deformation that occurs when the article is compressed to a given deformation, for a given amount of time, at a given temperature. Compression set of an article can be measured, for example using ASTM D395. For elastomeric materials, having a low compression set is associated with an ability for the material to maintain elastic properties even after prolonged compressive stress. Having a relatively low compression set may be beneficial, in some cases, where it is desired that the thermally insulating compressible solid article portion be able to regain at least a portion of its thickness when an applied compressive stress is removed. As an example, in some cases where the thermally insulating compressible solid article portion is compressed due to an expansion of an electrochemical cell in the battery pack, a subsequent contraction of the electrochemical cell may reduce the compressive stress applied. Having a relatively low compression set may then allow the thermally insulating compressible solid article to expand in thickness as the electrochemical cell contracts, thereby compensating for the change in dimension. In some embodiments, the thermally insulating compressible solid article portion has a compression set of less than or equal 15%, less than or equal to 12%, or less. In some embodiments, the thermally insulating compressible solid article portion has a compression set of less than or equal to 10%, less than or equal to 5%, or less. In some embodiments, the thermally insulating compressible solid article portion has a compression set of greater than or equal to 1%, greater than or equal to 2%, or more. Combinations of these ranges are possible. For example, in some embodiments, the thermally insulating compressible solid article portion has a compression set of greater than or equal to 1% and less than or equal to 10%. In some embodiments, the thermally insulating compressible solid article portion has a compression set value in one of the ranges above determined using a constant force measurement (e.g., ASTM D395 Test Method A). In some embodiments, the thermally insulating compressible solid article portion has a compression set value in one of the ranges above determined using a constant displacement measurement (e.g., ASTM D395 Test Method B).
In some embodiments, the thermally insulating compressible solid article portion has a relatively high compressibility. The compressibility of an article generally refers to the relative dimensional change of an article as a response to a change in compressive stress. In some instances, for example, the change in thickness 147 relative to thickness 146 in
The compressive response of a thermally insulating compressible solid article portion may be considered as a compressive stress versus percent compression curve. The thermally insulating compressible solid article portion may have a compressive stress versus percent compression curve that is suitable for a battery pack in which a high magnitude of anisotropic force with a component normal to one or more of the electrochemical cells is applied. In some instances, the thermally insulating compressible solid article portion has a compressive stress versus percent compression curve that is suitable for a battery pack in which one or more electrochemical cell undergoes a relatively high change in dimension during charging and discharging (e.g., such as certain electrochemical cells comprising lithium metal and/or lithium metal anode active materials).
In some such embodiments, the thermally insulating compressible solid article has a compressive stress versus percent compression curve in the hatched region of
The measurement of the compressive stress versus percent compression curve (as shown in
In some embodiments, the thermally insulating compressible solid article portion has a relatively high resilience. The resilience of an article generally refers to the percentage of energy released when a deformed object recovers from deformation relative to the energy required to produce the deformation. Resilience can be measured, for example, using ASTM D3574 Test H (a ball drop resilience measurement). A relatively high resilience may contribute to the thermally insulating compressible solid article portion being durable under multiple repeated compressions and decompression of the battery pack (e.g., during charging and discharging). In some embodiments, the thermally insulating compressible solid article portion has a resilience of at least 60%, at least 65%, at least 75%, at least 90%, at least 95%, or more. In some embodiments, the thermally insulating compressible solid article portion has both a relatively high compressibility and a relatively high resilience (e.g., with values in the ranges described above), which may contribute to a high extent of compensation of dimensional changes in the battery pack while also being durable.
In some embodiments, the thermally insulating compressible solid article portion has a relatively high dynamic continuous load limit. A dynamic continuous load limit generally refers to the maximum compressive stress applied to the article before failure occurs. Having a relatively high dynamic continuous load limit may be useful in some embodiments where a relatively high magnitude of anisotropic force with a component normal to one or more electrochemical cells of the battery pack is applied, or where one or more of the electrochemical cells undergoes a relatively large expansion during cycling. In some embodiments, the thermally insulating compressible solid article portion has a dynamic continuous load limit of greater than or equal to 30 kgf/cm2, greater than or equal to 35 kgf/cm2, greater than or equal to 40 kgf/cm2, and/or up to 45 kgf/cm2, or greater.
In some embodiments, the thermally insulating compressible solid article portion has a relatively low uncompressed mass density. A low mass density may contribute, at least in part, to the battery pack having a relatively high specific energy density. The uncompressed mass density of the thermally insulating compressible solid article portion refers to the bulk mass per unit volume of the article portion in the absence of a load (e.g., compressive stress). In some embodiments, the thermally insulating compressible solid article portion has an uncompressed mass density of greater than or equal to 0.3 g/cm3, greater than or equal to 0.35 g/cm3, greater than or equal to 0.4 g/cm3, greater than or equal to 0.45 g/cm3, greater than or equal to 0.5 g/cm3, and/or up to 0.55 g/cm3, up to 0.6 g/cm3, up to 0.65 g/cm3, up to 0.7 g/cm3, or greater at 25° C.
The thermally insulating compressible solid article portion can be made of any of a variety of suitable materials, provided that it have one or more of the combinations of thermal and mechanical properties in the present disclosure. In some embodiments, the thermally insulating compressible solid article portion comprises a polymeric material. A relatively large percentage of the thermally insulating compressible solid article portion may be made of a polymeric material. For example, greater than or equal to 50 wt %, greater than or equal to 75 wt %, greater than or equal to 90 wt %, greater than or equal to 95 wt %, greater than or equal to 99 wt %, or more (e.g., 100 wt %) of the thermally insulating compressible solid article portion may be made of a polymeric material. In certain embodiments, the thermally insulating compressible solid article portion comprises a polymeric foam, such as a microcellular polymeric foam.
While any of a variety of polymeric materials may be suitable, in certain instances the thermally insulating compressible solid article portion comprises a relatively elastic polymer. In some embodiments, the thermally insulating compressible solid article portion is or comprises an elastomer. As one non-limiting example, the thermally insulating compressible solid article portion may comprise a polyurethane. Polyurethanes are polymers comprising organic repeat units linked by carbamate (urethane) units. Polyurethanes can be made using any of a variety of techniques, such as by reacting isocyanates and polyols. In some embodiments, the thermally insulating compressible solid article portion is or comprises a microcellular polyurethane foam (e.g., foam sheet or foam layer). Referring to
The thermally insulating compressible solid article may have a thickness as well as two orthogonal lateral dimensions that are orthogonal to each other as well as orthogonal to the thickness. For example, referring to
The dimensions of the thermally insulating compressible solid article portion may be chosen based on any of a variety of considerations. For example, the thickness (e.g., uncompressed thickness) or lateral dimensions may be chosen based on the desired total size of the battery pack and/or a desired pack burden (defined as one minus the mass of the electrochemical cells of the battery pack divided by the total mass of the battery pack). In some embodiments, the uncompressed thickness of the thermally insulating compressible solid article portion is such that a sufficient amount of compression can occur (e.g., to compensate for expansion of the first electrochemical cell and/or second electrochemical cell during cycling).
In some embodiments, the thermally insulating compressible solid article portion has an uncompressed thickness of greater than or equal to 1 mm, greater than or equal to 2 mm, greater than or equal to 3 mm, greater than or equal to 4 mm, greater than or equal to 5 mm, greater than or equal to 5.5 mm, greater than or equal to 6 mm, or greater. In some embodiments, the thermally insulating compressible solid article portion has an uncompressed thickness of less than or equal to 10 mm, less than or equal to 9 mm, less than or equal to 7 mm, less than or equal to 6 mm, less than or equal to 5 mm, less than or equal to 3 mm, or less. Combinations of these ranges are possible. For example, in some embodiments, the thermally insulating compressible solid article portion has an uncompressed thickness of greater than or equal to 1 mm and less than or equal to 10 mm, greater than or equal to 1 mm and less than or equal to 5 mm, or greater than or equal to 2 mm and less than or equal to 3 mm.
In some embodiments the thermally insulating compressible solid article portion has one or more lateral dimension of greater than or equal to 50 mm, greater than or equal to 65 mm, greater than or equal to 80 mm, and/or up to 90 mm, up to 100 mm, up to 200 mm, or more. In some embodiments, the thermally insulating compressible solid article portion has at least one lateral dimension that is at least 5 times, at least 10 times, and/or up to 20 times, up to 50 times, up to 100 times or more greater than the uncompressed thickness of the thermally insulating compressible solid article portion.
In some embodiments, the battery pack has more than one thermally insulating compressible solid article portion. For example, in some embodiments, the battery pack comprises a third electrochemical cell, and a second thermally insulating compressible solid article portion between the second electrochemical cell and the third electrochemical cell.
In some cases, the total number of thermally conductive solid article portions is equal to the total number of electrochemical cells in the stack of electrochemical cells (e.g., 12 electrochemical cells and 12 thermally conductive solid article portions, or 36 electrochemical cells and 36 thermally conductive solid article portions). In some such cases, the total number of thermally insulating compressible solid article portions is equal to one more than the total number of electrochemical cells in the battery pack (e.g., 12 electrochemical cells and 13 thermally insulating compressible solid article portions). For example, there may be an electrochemical cell between each of the thermally insulating compressible solid article portions.
In some embodiments, the first thermally insulating compressible solid article portion and the second thermally insulating compressible solid article portion are part of discrete articles. Referring again to
In some embodiments, the controller may interact with the power bus by measuring cell or cell group voltages and/or power bus current. In some embodiments, the controller may interact with the power bus by balancing cells or cell groups (which may also be called “cell sets” herein), connecting/disconnecting the power bus to/from the load, and/or measuring power bus temperatures.
In some embodiments, the substrate may be or include a printed circuit board. In some embodiments, the substrate may include a controller area network (CAN) bus (e.g., 515) and at least one circuit breaker (e.g., 517), all in a single board. Additionally, the substrate may include at least one electrochemical cell terminal to which the cell(s) may be connected. For example, the cell terminal(s) may rise directly out of the substrate.
In some embodiments, the cell(s) may be connected directly to the substrate. In some embodiments, the substrate may be physically connected to the cell(s) (which could be one or any number of cells) without wires, such as via a physical connection between the cell(s) and the power bus. The inventors have recognized and appreciated that, in accordance with certain embodiments, using this physical connection instead of wires may reduce the connection distance (e.g., the distance may be just the distance between cells, instead of having to go up and through bus), thereby reducing resistance and resulting waste heat and other inefficiencies, such as voltage loss.
In some embodiments, a physical connection between the substrate (via the power bus or otherwise) and the cell(s) may provide heat transfer to and/or from the cell(s). In some embodiments, the physical connection between the substrate and the cell(s) may provide heat transfer directly between multiple cells, and/or directly between the cell(s) and the substrate in either direction. Examples of these heat transfers are described in relation to
In some embodiments, cell(s) may be connected to the substrate at least in part by laser welding. In some embodiments, this laser welding or another kind of welding or permanent attachment may create the physical connection that provides the heat transfer to and/or from the cell(s). For example, ultrasonic, friction, and/or resistance welding may be used in addition to or alternatively to laser welding (or any other precision metal connection technique) to create the physical connection. In some embodiments, the physical connection may be both electrically and thermally low-resistance. For example, the physical connection may have on average an electrical resistivity of 3*10−8 ohm-meters or less and a thermal conductivity of 200 watts per meter-kelvin or more.
Various materials may be used to create the physical connection, such as thermally and electrically conductive materials. In some embodiments, the material(s) used to create the physical connection may provide a heat flux of at least 1500 watts per square meter through the connection when the cell(s) have a temperature of 100 degrees Celsius and the substrate has a temperature of 25 degrees Celsius. In some embodiments, materials like copper, aluminum, and/or stainless steel may be used for the physical connection.
In some embodiments, battery pack 500 may include a housing in which the at least one electrochemical cell and the substrate are disposed.
Optionally, battery pack 500 may include one or more sensors (e.g., 516). It should be appreciated that although only a single controller 514 and a single sensor 516 are shown in
In some embodiments, the controller may determine (e.g., using sensor 516) and/or communicate (e.g., using CAN bus 515) various information. Examples of this information include temperature information of the battery pack, voltage and/or current information of the cell(s) in the battery pack, balancing information of the battery pack, charging information of the battery pack, diagnostic information of the battery pack, and health information of the battery pack. The inventors have recognized and appreciate that, in accordance with certain embodiments, any of this various information may be more reliable due to it being obtained locally (e.g., on the single substrate) rather than sent from a remote location via wires.
In some embodiments, the power bus may include at least one layer of conductive material embedded in the substrate. In some embodiments, the layer(s) may be either or both thermally and electrically conductive. For example, the substrate may have embedded heavy copper inner layers, and, in some embodiments, heavy copper upper layers (e.g., the substrate may include up to 30 ounces of copper on each side). In some embodiments, the mass of the embedded inner layers (such as copper) may be between 10 and 30 ounces per square foot.
In some embodiments, the substrate itself may be thermally conductive. For example, the substrate may have a thermal conductivity of at least 200 watts per meter kelvin, such as between 350 and 400 watts per meter-kelvin. The inventors have recognized and appreciated that, in accordance with certain but not necessarily all embodiments, this may further improve heat management, including removal of waste heat and utilization of heat transfer where desirable. Thermal conductivity of the substrate and/or the power bus may be measured using any suitable method according to some embodiments, including steady-state methods and transient methods (such as the transient hot wire method). However, in some embodiments, the substrate itself has a relatively low thermal conductivity. For example, the substrate may have a thermal conductivity of less than or equal to 100 watts per meter kelvin, less than or equal to 50 watts per meter kelvin, less than or equal to 20 watts per meter kelvin, less than or equal to 10 watts per meter kelvin, less than or equal to 5 watts per meter kelvin, and/or as low as 3 watts per meter kelvin, as low as 2 watts per meter kelvin, or lower. For example, the substrate, in some instances, comprises a composite material having a relatively low thermal conductivity. One non-limiting example is of such a composite is one comprising woven fiberglass close with a binder (e.g., an epoxy resin binder). One such example is FR-4.
In some embodiments, the cell(s) may include alignment features that allow the substrate to be fitted on top of the cell(s) and/or allow the cell(s) to be inserted into the substrate. In some embodiments, the substrate includes at least one opening into which at least a portion of the cell(s) are inserted. For example, tab(s) of the cell(s) may be pulled through the opening(s) or inserted into them. In some embodiments, the tabs may be straight along the same axis as the cells, and then bent or otherwise rotated or deformed to make contact with the substrate (see
In some embodiments, the controller may balance charge and/or discharge between multiple cells. In some embodiments, the controller turns the balancing on or off, and the balancing is achieved at least in part through circuitry that is part of the battery management system. For example, the controller may ensure that the cell(s) attain the same state and/or depth of charge and/or discharge using passive balancing and/or active balancing. In some embodiments, balancing may be performed “at top of charge” such that when a cell reaches maximum charge voltage, it may be bypassed so other cells in series with it come up to that voltage value. Alternatively or additionally, balancing may be performed at “bottom of charge” or any other suitable configuration.
In some embodiments, the controller may use active balancing, such as by taking charge from either the entire battery pack or a cell that has more charge and give it to cell(s) with less charge, which can be done at any point of a cycle.
According to some embodiments, the cell(s) may include at least one lithium-metal electrode active material. Additionally, each set of cells (e.g., cell set 521) may include one or more cells (e.g., 521A-521C). In some embodiments, each set of cells may have a single cell. Alternatively, each set of cells may include multiple cells and may form a cell “block,” or multiple sets of cells may together form a cell block.
In some embodiments, system 700 may include at least one communication bus, such as power circuitry 717, which may be similar to breaker 517 described elsewhere herein. In some embodiments, power circuitry 717 may provide circuit breaking, power supplying, shunts, and so on. In some embodiments, system 700 may include at least one balancing component, such as balancing circuitry 720. In some embodiments, balancing circuitry 720 may perform cell grouping and cell group balancing. In some embodiments, system 700 may include at least one interface, such as interface 721, which may include a serial interface, such as for transistor-transistor logic serial communication.
In some embodiments, any combination of the components in
In some embodiments, the substrate may include at least one PCB via, such as the numerous vias 565. In some embodiments, the substrate may include at least one battery post, such as positive battery post 575 and negative battery post 576.
In some embodiments, each set of cells may have a single cell. Alternatively, each set of cells may include multiple cells and may form a cell “block,” or multiple sets of cells may together form a cell block. Additionally, each cell (either in a battery, all the batteries in a battery pack, or in a set of cells) or set of cells may utilize the same electrochemistry. That is to say, in some embodiments, each cell may make use of the same anode active material and the same cathode active material.
In some embodiments, the controller may use the multiplexing switch apparatus to selectively discharge and charge the cells or sets of cells at different, programmable rates. For example, the controller may use the multiplexing switch apparatus to selectively discharge the cells or sets of cells at a first rate at least 2 times higher than a second rate of charging the sets of cells (i.e., discharging twice as fast as charging). Alternatively or additionally, the first rate of discharging may be at least 4 times higher than the second rate of charging the sets of cells (i.e., discharging four times as fast as charging). The inventors have recognized and appreciated that, in accordance with certain embodiments, such ratios of discharge rate to charge rate may improve the performance and cycle life of the cells.
In some embodiments, the load may be at least one component of a vehicle. The vehicle may be any suitable vehicle, adapted for travel on land, sea, air, and/or space. For example, the vehicle may be an automobile, truck, motorcycle, boat, helicopter, airplane, rocket, spaceship, and/or any other suitable type of vehicle.
As mentioned above, the housing of the battery pack may comprise a substrate for facilitating electronic connections. In some embodiments, the battery pack comprises a substrate to which a tab of the first electrochemical cell and/or the second electrochemical cell can be connected.
The substrate may have locations between the above-mentioned spaces for electronically conductive interconnects. In some embodiments, the battery pack comprises an electronically conductive interconnect on the substrate connected to at least one tab of an electrochemical cell (e.g., the first electrochemical cell and/or the second electrochemical cell). Electronically conductive interconnects, which can be made of one or more electronically conductive solid materials, may be discrete objects separable from the substrate, or may be fabricated such that they are part of the substrate (e.g., the substrate may be molded at least partially surrounding the interconnects). When tabs from electrochemical cells pass through the spaces of the substrate, the tabs may then be connected to the electronically conductive interconnects to establish electronic connections (e.g., to an electronic circuit). In
In some embodiments, an electronically conductive interconnect on the substrate comprises a first material portion and a second material portion. In some embodiments, the electronically conductive interconnect comprises a first material portion connected to a first tab of the first electrochemical cell and a second material portion connected to a second tab of the second electrochemical cell. For example,
It has been recognized and appreciated that conventional techniques for management and operation of rechargeable electrochemical cells have resulted in the previously poor longevity and performance of cells (and batteries in which they may be included). For example, cells have suffered a short cycle life (e.g., a low number of complete cycles before capacity falls below 80% of original capacity, as cells typically do at some point after sufficient usage), particularly where charge and discharge rates are similar, or where the charge rate is higher than the discharge rate. For example, many users of cells in batteries have desired the batteries to have nearly identical charge and discharge rates (e.g., 4 hours to charge and 4 hours to discharge), and battery manufacturers have provided batteries and battery management systems that provide such nearly identical rates. Many users have also desired batteries to charge at higher rates than they discharge (e.g., 30 minutes to charge and 4 hours to discharge) for various reasons, such as to reduce inconvenience of waiting for charging to use the batteries and extended runtimes.
The term “charging step” is used herein to generally refer to a continuous period of time during which charging is performed without discharging, and the term “discharging step” is used herein to generally refer to a continuous period during which discharging is performed without charging. A charging step coupled with a discharging step may form a cycle, but the cycle may not necessarily be a complete cycle. The term “capacity” is used to generally refer to an amount of electrical charge a cell or cells can deliver at a given or rated voltage and is often measured in amp-hours (such as milliamp-hours or mAh). In some embodiments, capacity may be the mAh a cell or cells can hold at a given point in time (which may change over multiple cycles), it may be the mAh remaining in a cell or cells at a given point in time, or it may be the mAh a cell or cells need to fully re-charge.
The term “state of charge” (SOC) is used herein to refer to a level of charge of the cell relative to its capacity and is measured as a percentage. As examples, a state of charge of 100% refers to a fully charged cell, a state of charge of 40% refers to a cell that retains 40% of its capacity, and a state of charge of 0% refers to a fully discharged cell.
The term “state of charge range” (SOC range) is used herein to refer to a range of states of charge. For example, a state of charge range of 10% to 50% would include the states of charge of 10%, 50%, and all states of charge between 10% and 50%.
The “breadth” of the state of charge range is used herein to refer to the absolute value of the difference between the end points of a state of charge range. To illustrate, a state of charge range of 10% to 50% would have a breadth of 40% (because 50% minus 10% is 40%). As another example, a state of charge range of at least 2% and at most 5% would have a breadth of 3% (because 5% minus 2% is 3%).
It has been recognized and appreciated that the cycle life of a cell (and a battery including the cell), and consequently the longevity and performance of the cell (and battery), may be greatly improved by employing higher ratios of discharge rate to charge rate, higher ratios of charge rate to other charge rate(s) (such as a preceding or proceeding rate(s)), and/or higher ratios of discharge rate to other discharge rate(s). Furthermore, it has been recognized and appreciated that these ratios may be employed by providing a cell and/or battery management system that controls the cell or cells to provide such ratios.
It has been recognized and appreciated that such improvements and others described herein, such as improved cell cycle life, can be had even if not every charging step and/or every discharging step satisfies a target ratio, and/or even if the ratios are employed over only a portion of a charging step and/or a discharging step, and/or even if the ratios are employed over a state of charge range that constitutes only a portion of the full SOC range.
For example, some embodiments are directed to a cell management system that controls a cell such that the cell is discharged or charged over a SOC range (e.g., a range having breadth of at least 2% and at most 60%) to satisfy a rate ratio (such as by discharging at a rate at least 2 times an average charging rate of any of the last 5 cycles, or by charging to establish a similar ratio with discharging rate(s)) if the ratio has not been satisfied within the last 5 cycles. As another example, in some embodiments the cell is discharged over a SOC range to satisfy another rate ratio (such as by discharging at a rate at least 2 times an average discharging rate of any of the last 5 cycles, but discharging at most 4 times a maximum recommended continuous discharging rate) if the ratio has not been satisfied within the last 5 cycles.
As an additional example, in some embodiments, once a threshold SOC (e.g., 60% or less) is reached while discharging, the discharging rate is increased to at least 2 times an average charging rate of at least one cycle in the cycle history. In some embodiments, a charging step is terminated (e.g., at 60% SOC) and a discharge is initiated, whereupon the cell is discharged, over a SOC range having breadth of at least 1%, at a rate at least 2 times an average charging rate of the terminated charging step or of at least one cycle in the cycle history. In additional embodiments, the cell is discharged over a SOC range (e.g., a range having breadth of at least 2% and at most 60%), and then charged such that the discharging rate is at least 2 times the average charging rate.
In further embodiments, if a fast charging request has not been received, the cell is charged over a first SOC range (e.g., a range having breadth of at least 2% and at most 60%), and then charged over a second SOC range such that the rate over the first SOC range is at most 0.5 times the average rate over the second SOC range. In some embodiments, the cell is discharged, and then immediately charged over a first SOC range (e.g., a range having breadth of at least 2% and at most 60%), and a future charging schedule is set and executed such that by an end of the next 4 cycles, the cell is charged over a second SOC range such that the rate over the first SOC range is at most 0.5 times the average rate over the second SOC range.
Furthermore, it has been recognized and appreciated that analysis and control as described herein may be performed by a cell and/or battery management system (e.g., of a battery pack described herein).
Some embodiments, such as embodiments having multiple cells, are directed to a battery management system that multiplexes cells such that the cells can be charged all at once (or with multiple cells discharged at the same time) and discharged individually or in smaller sets. This may result in actual ratios of discharge rate to charge rate (or discharge rate to other discharge rate(s), or charge rate to other charge rate(s)) for the cells that improve their cycle life, while providing whatever output rates that are desired or required for particular loads and applications. Furthermore, the inventors have recognized and appreciated that discharging some but not all of the cells at once with homogeneous current distribution may also improve their cycle life.
For example, with a battery having 4 cells, 1 cell could be discharged at a time at 0.5 amps for 3 hours each, and then all 4 cells could be charged at 0.5 amps for 12 hours—such a configuration would provide an actual ratio of discharge rate to charge rate of 4:1, while the ratio from the user's perspective would be 1:1 because the cells are discharged individually for 3 hours each (totaling 12 hours of discharge time). The inventors have recognized and appreciated that such a battery management system may actually improve the cycle life of batteries while still providing users what they desire or need from the batteries. In some embodiments, the functionality providing this duo of benefits may be hidden from users and may be integrated into the cell blocks and/or batteries themselves.
It has been recognized and appreciated that the cycle life of batteries may be further improved by monitoring the cycles of the cells and various properties (such as the duration of a connection between a load and a cell or cells currently connected to the load, or a more complex function considering multiple parameters) and selecting which cells to discharge when based on this monitoring, especially compared to conventional techniques, which relied on much simpler selection processes like “round robin” or considering a number of prior cycles.
In some embodiments, such as embodiments having multiple cells, a multiplexing switch apparatus (not shown in
In some embodiments, the controller may control the cell such that, for at least a portion of a charging step of the cell, the cell is charged at a charging rate or current that is lower than a discharging rate or current of at least a portion of a previous discharging step. For example, the controller may cause the cell to be charged for some state of charge range (e.g., over a range having breadth of anywhere from 1% to 100%) at a charging rate or current that is on average at least 2 times lower than the discharging rate or current that has been used on average discharging for some state of charge range (e.g., over a range having breadth of anywhere from 1% to 100%) (i.e., the charging rate or current may be half as fast as the discharging rate or current). Alternatively or additionally, the controller may cause the cell to be charged at a charging rate or current that is at least 4 times lower than the discharging rate (e.g., as a result of this controlling, over the last cycle, the cell is charged for some range one-fourth as fast as the cell has been discharged for some range). The inventors have recognized and appreciated that such ratios of charge rate to discharge rate may improve the performance and cycle life of a cell.
In some embodiments, controlling the cell may include controlling when and how to start and stop charging and discharging, induce discharging, increase or decrease the rate or current of charging or discharging, and so on. For example, controlling charging or discharging of the cell may include, respectively, starting charging or discharging, stopping charging or discharging, increasing or decreasing the rate or current of charging or discharging, and so on.
In some embodiments, the cell is charged such that, over a period of time during which at least 5% (or at least 1%, or at least 10%, or at least 15%, or at least 25%, or anywhere between) of the capacity of the cell is charged, the average charge rate or current is lower than the average discharge rate or current used to discharge at least 5% (or at least 10%, or at least 15%, or at least 25%, or anywhere between) of the cell's capacity during a previous discharging step, which may be, for example, the immediately preceding discharging step or an earlier discharging step.
In some embodiments, a charging step is performed such that, for at least 5% (or at least 10%, at least 25%, at least 50%, or at least 75%) of the cell's or battery's capacity, the average of the charging rate and/or current is less than 50% (or less than 35%, or less than 25%) of an average discharging rate and/or current at which at least 5% (or at least 10%, at least 25%, at least 50%, or at least 75%) of the cell's or battery's capacity was discharged during a previous discharging step.
In certain embodiments, a charging step is performed such that, for at least 5% (or at least 10%, at least 25%, at least 50%, or at least 75%) of the cell's or battery's capacity, the average of the charging rate and/or current is less than 50% (or less than 35%, or less than 25%) of an average discharging rate and/or current at which at least 5% (or at least 10%, at least 25%, at least 50%, or at least 75%) of the cell's or battery's capacity was discharged during the immediately preceding discharging step.
In some embodiments, an average discharging rate or current during the previous discharging step may be equal to or less than an average charging rate or current during the charging step, and an average discharging rate or current during discharge of a state of charge range have breadth of at least 5% during the previous discharging step may be at least 2 times higher (or may be 4 times higher) than the average charging rate or current during the charging step. The inventors have recognized and appreciated that improvements described herein, such as improved cell cycle life, can still be had even if the average discharge rate for the cell is the same or even slower than the charge rate, so long as during discharge of at least a portion (such as state of charge range having breadth of 5%) during the previous discharging step, an average discharging rate or current is sufficiently higher than (such as at least double, triple, or quadruple) the average charging rate or current during that time.
As used herein, when a cell is charged at multiple different rates over a given period of time (e.g., over a portion of a charging step, over an entire charging step, or over a series of charging steps), the average charging rate over that given period of time is calculated as follows:
where CRAvg is the average charging rate over the given period of time, n is the number of different rates at which the cell is charged, CRi is the charging rate, CCapi is the portion of the cell's capacity that is charged at charging rate CRi during the given period of time, and CCapTotal is the total of the cell's capacity that is charged over the entire period of time. To illustrate, if, during a charging step, a cell is charged from 0% to 50% of its capacity at a rate of 20 mAh/minute and then from 50% to 80% of its capacity at a rate of 10 mAh/minute, then the average charging rate during the charging step would be calculated as:
As used herein, when a cell is discharged at multiple different rates over a given period of time (e.g., over a given charging step or series of charging steps), the average discharging rate over that given period of time is calculated as follows:
where DRAvg is the average discharging rate over the given period of time, n is the number of different rates at which the cell is discharged, DRi is the discharging rate, DCapi is the portion of the cell's capacity that is discharged at discharging rate DRi during the given period of time, and DCapTotal is the total of the cell's capacity that is discharged over the entire period of time. To illustrate, if, during a discharging step, a cell is discharged from 90% to 50% of its capacity at a rate of 25 mAh/minute and then from 50% to 20% of its capacity at a rate of 15 mAh/minute, then the average discharging rate during the discharging step would be calculated as:
It has been recognized and appreciated that a number of factors may go into determining charge rates that may improve the performance and cycle life of a cell such as a lithium metal cell, which may include rate of discharge, cell impedance, and/or cell State of Health (SOH). In some embodiments, the controller may be aware of these factors because it may measure parameters or characteristics (such as via sensor 116) that can be used to determine each of them. The controller may directly or indirectly measure charge and discharge current, Coulombs added or removed, cell impedance (capacitive and resistive), and/or cell pressure, size, and/or thickness.
In some embodiments, the controller may monitor such characteristic(s) of the cell. For example, the characteristic(s) may include at least a portion of a discharge history of the cell. Alternatively or additionally, the characteristic(s) may include at least one morphological characteristic of the cell. The controller may monitor any of these using sensor 116, such as a pressure sensor, a gauge to measure thickness, a sensor to measure or determine surface roughness and/or pits (such as pits in an anode), and/or a memory for storing cell charge/discharge history. For example, a pressure sensor may be included to measure uniaxial pressure and/or gas pressure (such as to determine if the cell generates an excessive amount of gas). Alternatively or additionally, a gauge may be included to measure a thickness of the cell, and the controller may determine and monitor at least one rate of increase of the thickness.
In some embodiments, the controller may use this information, such as the characteristic(s), to determine the charge method and/or rate to be used, which may include controlling rates or other parameters as described herein.
In some embodiments, the controller may consider any of several factors when determining the cell state of charge and State of Health (SOH). An impedance measurement may have two components: real and imaginary. The real component may be simply the DC resistance R=RS+RP. The imaginary (or reactive) component in this case may be XC, which may be affected inversely by frequency:
where f is frequency and c is capacitance. Impedance (Z) may be found at any particular frequency, and the phase angle may be known or determined as follows: Z=√{square root over (R2+XC2)}. Impedance may change both with SOC and SOH. The inventors have recognized and appreciated that these relationships may allow the controller to determine how to charge the cell in order to provide improvements described herein.
It has also been recognized and appreciated that, in certain instances, pulses of cycles and/or charging/discharging steps should not be applied faster than a rate equal to about double or triple RC time constants, because at a faster rate, most of the energy may not be effective in charging or discharging the cell. Rather, it may be mostly reactive in nature and most of the energy may be returned by the capacitance or dissipated in the resistance.
It has been further recognized and appreciated that a cell may grow and shrink in thickness with every cycle and that a portion of the growth is retained each cycle. This growth and shrinkage can be measured by monitoring the pressure and/or size change of the cell directly. These are additional inputs that may be used when determining SOC and SOH, and they can also be used in determining how to charge the cell.
In some embodiments, the controller may control charging of the cell based on the characteristic(s) of the cell. For example, if the cell has had a discharging step or history of discharging at a certain discharge rate or current (such as 300 mA) at least for a portion of the previous discharging step, the cell may be controlled to charge at a lower rate or current (such as at 150 mA or 75 mA) for at least a portion of the charging step.
In some embodiments including an induced discharge, the controller may control the cell such that, for at least a portion of the charging step (such as 5% of the cycle), the cell is charged at a charging rate or current that is lower than a discharging rate or current of at least a portion of a previous discharging step other than (i.e., not including) the induced discharge.
As another example, the controller may terminate usage of the cell if an applied anisotropic pressure falls below a threshold, which may indicate that the pressure applying system (examples of which are described in more detail below) is damaged. For example, in some embodiments such a threshold may be 1% to 50% of nominal applied anisotropic pressure. Alternatively or additionally, the controller may terminate usage of the cell if pressure is too high or the thickness has been increasing faster than a threshold rate. For example, in some embodiments such a threshold rate may be 1% to 3% of thickness increase or more per cycle.
In some embodiments, a multiplexing switch apparatus (e.g., 512) may include an array of switches. Additionally, the multiplexing switch apparatus may be connected to each set of cells and/or to each cell individually. In some embodiments, the controller, such as 514, may use the multiplexing switch apparatus to selectively discharge the cells or sets of cells based on at least one criterion.
For example, the criterion may include a sequence in which to discharge the cells or sets of cells, such as a predefined numbering or order associated with the sets of cells (e.g., starting with a first set, switching through each set to the last set, and then starting over with the first set), and/or an order based on the cell(s) or set(s) of cells with the next highest voltage or some other measure indicating the next strongest. The inventors have recognized and appreciated that using a sequence, especially a predefined numbering, may reduce the complexity of the operations performed by the system (e.g., a controller that is not a microprocessor) and may be usable by a wider array of systems.
Alternatively or additionally, the criterion may be context-sensitive, such as by considering any one or more of the following: a duration of a connection between a load and a set of cells currently connected to the load (which may be at least 0.01 seconds in some embodiments), a delivered capacity at the connection, and the value of a function having one or more parameters. In certain embodiments, the criterion may not include a number of prior discharging steps of the set of cells.
In some embodiments, the function may have parameters such as any one or more of the following: a capacity accumulated over several connections between the load and the set of cells, the delivered capacity at the connection, a current of the set of cells, a voltage of the set of cells and/or of at least one other set of cells, a cutoff discharge voltage of the set of cells, a power of the set of cells, an energy of the set of cells, a number of charging or discharging steps of the set of cells, an impedance of the set of cells, a rate of voltage fading of the set of cells during the connection, a temperature of the set of cells, and a pressure of the set of cells (e.g., the pressure on the cell(s) from their physical enclosure, which may indicate cell capacity and is discussed further below). According to some embodiments, the delivered capacity at a single connection may be in the range from 0.01% of nominal capacity to 100% (e.g., 95%) of set nominal capacity.
In some embodiments, a sensor (e.g., 516) may measure the criterion and/or any of the parameters of the function. For example, the sensor may include a current sensor that measures the current in amperes of a given set of cells. It should be appreciated that the criterion may be plural or singular and may relate to the currently discharging set of cells and/or may determine the next set of cells.
In some embodiments, the controller (e.g., 514) may include one or more processors, which may be of whatever complexity is suitable for the application. For example, evaluating the function of the criterion in some embodiments may rely on a microprocessor forming part or all of the controller.
In some embodiments, the controller may use the multiplexing switch apparatus to selectively discharge and charge the cells or sets of cells at different, programmable rates. For example, the controller may use the multiplexing switch apparatus to selectively discharge the cells or sets of cells at a first rate at least 2 times higher than a second rate of charging the sets of cells (i.e., discharging twice as fast as charging). Alternatively or additionally, the first rate of discharging may be at least 4 times higher than the second rate of charging the sets of cells (i.e., discharging four times as fast as charging). The inventors have recognized and appreciated that such ratios of discharge rate to charge rate may improve the performance and cycle life of the cells. According to some embodiments, the controller may temporally overlap the discharge of the sets of cells. For example, before a given cell or set of cells ceases discharging, another cell or set of cells may begin discharging. In some embodiments, the controller may continue to provide power from the sets of cells during switching between different sets. The inventors have recognized and appreciated that this temporal overlap of discharging and continuation of power may maintain the power requirements of the load even during transition between different cells of sets of cells, which may further improve the cycle life of the cell(s) compared to conventional techniques. Accordingly, multiple cells may discharge simultaneously during such an overlap. Additionally, such an overlap may provide smoother transition of voltage than has been possible with conventional techniques.
Alternatively or additionally, the controller may use the multiplexing switch apparatus (e.g., 512) to connect the sets of cells to a load in a topology employed or required by the load.
In some embodiments, the controller may use the multiplexing switch apparatus (e.g., 512) to isolate a single set of cells for discharging while other sets of cells are not discharging. Alternatively or additionally, a single cell may be isolated at a time. For example, the controller may use the multiplexing switch apparatus to isolate a single set of cells or a single cell for discharging while the other cells or sets of cells are not discharging. For a given cycle, each cell may be discharged once before any cell is discharged twice, according to some embodiments (e.g., where sequential discharging is used, but not limited to such embodiments).
As for charging, in some embodiments the controller may use the multiplexing switch apparatus to charge the sets of cells, and/or cells within a set, in parallel. For example, all the cells in the cell block, battery, or batteries may be charged in parallel at a rate one-fourth of the rate of discharge.
A variety of anode active materials are suitable for use with the anodes of the electrochemical cells described herein, according to certain embodiments. In some embodiments, the anode active material comprises lithium (e.g., lithium metal), such as lithium foil, lithium deposited onto a conductive substrate or onto a non-conductive substrate (e.g., a release layer), and lithium alloys (e.g., lithium-aluminum alloys and lithium-tin alloys). Lithium can be contained as one film or as several films, optionally separated. Suitable lithium alloys for use in the aspects described herein can include alloys of lithium and aluminum, magnesium, silicium (silicon), indium, and/or tin. In some embodiments, the anode active material comprises lithium (e.g., lithium metal and/or a lithium metal alloy) during at least a portion of or during all of a charging and/or discharging process of the electrochemical cell. In some embodiments, the anode active material comprises lithium (e.g., lithium metal and/or a lithium metal alloy) during a portion of a charging and/or discharging process of the electrochemical cell, but is free of lithium metal and/or a lithium metal alloy at a completion of a discharging process.
In some embodiments, the anode active material contains at least 50 wt % lithium. In some cases, the anode active material contains at least 75 wt %, at least 90 wt %, at least 95 wt %, or at least 99 wt % lithium.
In some embodiments, the anode is an electrode from which lithium ions are liberated during discharge and into which the lithium ions are integrated (e.g., intercalated) during charge. In some embodiments, the anode active material is a lithium intercalation compound (e.g., a compound that is capable of reversibly inserting lithium ions at lattice sites and/or interstitial sites). In some embodiments, the anode active material comprises carbon. In certain cases, the anode active material is or comprises a graphitic material (e.g., graphite). A graphitic material generally refers to a material that comprises a plurality of layers of graphene (i.e., layers comprising carbon atoms covalently bonded in a hexagonal lattice). Adjacent graphene layers are typically attracted to each other via van der Waals forces, although covalent bonds may be present between one or more sheets in some cases. In some cases, the carbon-comprising anode active material is or comprises coke (e.g., petroleum coke). In certain embodiments, the anode active material comprises silicon, lithium, and/or any alloys of combinations thereof. In certain embodiments, the anode active material comprises lithium titanate (Li4Ti5O12, also referred to as “LTO”), tin-cobalt oxide, or any combinations thereof.
A variety of cathode active materials are suitable for use with cathodes of the electrochemical cells described herein, according to certain embodiments. In some embodiments, the cathode active material comprises a lithium intercalation compound (e.g., a compound that is capable of reversibly inserting lithium ions at lattice sites and/or interstitial sites). In certain cases, the cathode active material comprises a layered oxide. A layered oxide generally refers to an oxide having a lamellar structure (e.g., a plurality of sheets, or layers, stacked upon each other). Non-limiting examples of suitable layered oxides include lithium cobalt oxide (LiCoO2), lithium nickel oxide (LiNiO2), and lithium manganese oxide (LiMnO2). In some embodiments, the layered oxide is lithium nickel manganese cobalt oxide (LiNixMnyCozO2, also referred to as “NMC” or “NCM”). In some such embodiments, the sum of x, y, and z is 1. For example, a non-limiting example of a suitable NMC compound is LiNi1/3Mn1/3Co1/3O2. In some embodiments, a layered oxide may have the formula (Li2MnO3)x(LiMO2)(1-x) where M is one or more of Ni, Mn, and Co. For example, the layered oxide may be (Li2MnO3)0.25(LiNi0.3Co0.15Mn0.55O2)0.75. In some embodiments, the layered oxide is lithium nickel cobalt aluminum oxide (LiNixCoyAlzO2, also referred to as “NCA”). In some such embodiments, the sum of x, y, and z is 1. For example, a non-limiting example of a suitable NCA compound is LiNi0.8Co0.15Al0.05O2. In certain embodiments, the cathode active material is a transition metal polyanion oxide (e.g., a compound comprising a transition metal, an oxygen, and/or an anion having a charge with an absolute value greater than 1). A non-limiting example of a suitable transition metal polyanion oxide is lithium iron phosphate (LiFePO4, also referred to as “LFP”). Another non-limiting example of a suitable transition metal polyanion oxide is lithium manganese iron phosphate (LiMnxFe1-xPO4, also referred to as “LMFP”). A non-limiting example of a suitable LMFP compound is LiMn0.8Fe0.2PO4. In some embodiments, the cathode active material is a spinel (e.g., a compound having the structure AB2O4, where A can be Li, Mg, Fe, Mn, Zn, Cu, Ni, Ti, or Si, and B can be Al, Fe, Cr, Mn, or V). A non-limiting example of a suitable spinel is a lithium manganese oxide with the chemical formula LiMxMn2-xO4 where M is one or more of Co, Mg, Cr, Ni, Fe, Ti, and Zn. In some embodiments, x may equal 0 and the spinel may be lithium manganese oxide (LiMn2O4, also referred to as “LMO”). Another non-limiting example is lithium manganese nickel oxide (LiNixM2-xO4, also referred to as “LMNO”). A non-limiting example of a suitable LMNO compound is LiNi0.5Mn1.5O4. In certain cases, the electrode active material of the second electrode comprises Li1.14Mn0.42Ni0.25Co0.29O2 (“HC-MNC”), lithium carbonate (Li2CO3), lithium carbides (e.g., Li2C2, Li4C, Li6C2, Li8C3, Li6C3, Li4C3, Li4Cs), vanadium oxides (e.g., V2O5, V2O3, V6O13), and/or vanadium phosphates (e.g., lithium vanadium phosphates, such as Li3V2(PO4)3), or any combination thereof.
In some embodiments, the cathode active material comprises a conversion compound. For instance, the cathode may be a lithium conversion cathode. It has been recognized that a cathode comprising a conversion compound may have a relatively large specific capacity. Without wishing to be bound by a particular theory, a relatively large specific capacity may be achieved by utilizing all possible oxidation states of a compound through a conversion reaction in which more than one electron transfer takes place per transition metal (e.g., compared to 0.1-1 electron transfer in intercalation compounds). Suitable conversion compounds include, but are not limited to, transition metal oxides (e.g., Co3O4), transition metal hydrides, transition metal sulfides, transition metal nitrides, and transition metal fluorides (e.g., CuF2, FeF2, FeF3). A transition metal generally refers to an element whose atom has a partially filled d sub-shell (e.g., Sc, Ti, V, Cr, Mn, Fe, Co, Ni, Cu, Zn, Y, Zr, Nb, Mo, Tc, Ru, Rh, Pd, Ag, Cd, Hf, Ta, W, Re, Os, Ir, Pt, Au, Hg, Rf, Db, Sg, Bh, Hs).
In some cases, the cathode active material may be doped with one or more dopants to alter the electrical properties (e.g., electrical conductivity) of the cathode active material. Non-limiting examples of suitable dopants include aluminum, niobium, silver, and zirconium.
In some embodiments, the cathode active material may be modified by a surface coating comprising an oxide. Non-limiting examples of surface oxide coating materials include: MgO, Al2O3, SiO2, TiO2, ZnO2, SnO2, and ZrO2. In some embodiments, such coatings may prevent direct contact between the cathode active material and one or more components of the electrolyte, thereby suppressing side reactions.
In certain embodiments, the cathode active material comprises sulfur. In some embodiments, the cathode active material comprises electrode active sulfur-containing materials. “Electrode active sulfur-containing materials,” as used herein, refers to electrode active materials which comprise the element sulfur in any form, wherein the electrochemical activity involves the oxidation or reduction of sulfur atoms or moieties. As an example, the electrode active sulfur-containing material may comprise elemental sulfur (e.g., S8). In some embodiments, the electrode active sulfur-containing material comprises a mixture of elemental sulfur and a sulfur-containing polymer. Thus, suitable electrode active sulfur-containing materials may include, but are not limited to, elemental sulfur, sulfides or polysulfides (e.g., of alkali metals) which may be organic or inorganic, and organic materials comprising sulfur atoms and carbon atoms, which may or may not be polymeric. Suitable organic materials include, but are not limited to, those further comprising heteroatoms, conductive polymer segments, composites, and conductive polymers. In some embodiments, an electrode active sulfur-containing material within an electrode (e.g., a cathode) comprises at least 40 wt % sulfur. In some cases, the electrode active sulfur-containing material comprises at least 50 wt %, at least 75 wt %, or at least 90 wt % sulfur.
Examples of sulfur-containing polymers include those described in: U.S. Pat. Nos. 5,601,947 and 5,690,702 to Skotheim et al.; U.S. Pat. Nos. 5,529,860 and 6,117,590 to Skotheim et al.; U.S. Pat. No. 6,201,100 issued Mar. 13, 2001, to Gorkovenko et al., and PCT Publication No. WO 99/33130, each of which is incorporated herein by reference in its entirety for all purposes. Other suitable electrode active sulfur-containing materials comprising polysulfide linkages are described in U.S. Pat. No. 5,441,831 to Skotheim et al.; U.S. Pat. No. 4,664,991 to Perichaud et al., and in U.S. Pat. Nos. 5,723,230, 5,783,330, 5,792,575 and 5,882,819 to Naoi et al., each of which is incorporated herein by reference in its entirety for all purposes. Still further examples of electrode active sulfur-containing materials include those comprising disulfide groups as described, for example in, U.S. Pat. No. 4,739,018 to Armand et al.; U.S. Pat. Nos. 4,833,048 and 4,917,974, both to De Jonghe et al.; U.S. Pat. Nos. 5,162,175 and 5,516,598, both to Visco et al.; and U.S. Pat. No. 5,324,599 to Oyama et al., each of which is incorporated herein by reference in its entirety for all purposes.
One or more electrodes may further comprise additional additives, such as conductive additives, binders, etc., as described in U.S. Pat. No. 9,034,421 to Mikhaylik et al.; and U.S. Patent Application Publication No. 2013/0316072, each of which is incorporated herein by reference in its entirety for all purposes.
Any of a variety of materials can be used as an electrolyte, in embodiments in which an electrolyte is present. The electrolyte can comprise, for example, a solution of ions, a solid electrolyte, a gel electrolyte, and/or a combination of these.
In some embodiments, the electrochemical cells of the battery pack further comprise a separator between two electrode portions (e.g., an anode portion and a cathode portion). The separator may be a solid non-conductive or insulative material, which separates or insulates the anode and the cathode from each other preventing short circuiting, and which permits the transport of ions between the anode and the cathode. In some embodiments, the porous separator may be permeable to the electrolyte.
The pores of the separator may be partially or substantially filled with electrolyte. Separators may be supplied as porous free standing films which are interleaved with the anodes and the cathodes during the fabrication of cells. Alternatively, the porous separator layer may be applied directly to the surface of one of the electrodes, for example, as described in PCT Publication No. WO 99/33125 to Carlson et al. and in U.S. Pat. No. 5,194,341 to Bagley et al.
A variety of separator materials are known in the art. Examples of suitable solid porous separator materials include, but are not limited to, polyolefins, such as, for example, polyethylenes (e.g., SETELA™ made by Tonen Chemical Corp) and polypropylenes, glass fiber filter papers, and ceramic materials. For example, in some embodiments, the separator comprises a microporous polyethylene film. Further examples of separators and separator materials suitable for use in this invention are those comprising a microporous xerogel layer, for example, a microporous pseudo-boehmite layer, which may be provided either as a free standing film or by a direct coating application on one of the electrodes, as described in U.S. Pat. Nos. 6,153,337 and 6,306,545 by Carlson et al. of the common assignee. Solid electrolytes and gel electrolytes may also function as a separator in addition to their electrolyte function.
As described above, in some embodiments, a force, or forces, is applied to portions of an electrochemical cell. Such application of force may reduce irregularity or roughening of an electrode surface of the cell (e.g., when lithium metal or lithium alloy anodes are employed), thereby improving performance. Electrochemical devices in which anisotropic forces are applied and methods for applying such forces are described, for example, in U.S. Pat. No. 9,105,938, issued Aug. 11, 2015, published as U.S. Patent Publication No. 2010/0035128 on Feb. 11, 2010, and entitled “Application of Force in Electrochemical Cells,” which is incorporated herein by reference in its entirety for all purposes.
In the embodiments described herein, battery packs may undergo a charge/discharge cycle involving deposition of metal (e.g., lithium metal or other active material) on a surface of an anode upon charging and reaction of the metal on the anode surface, wherein the metal diffuses from the anode surface, upon discharging. The uniformity with which the metal is deposited on the anode may affect cell performance. For example, when lithium metal is removed from and/or redeposited on an anode, it may, in some cases, result in an uneven surface. For example, upon redeposition it may deposit unevenly forming a rough surface. The roughened surface may increase the amount of lithium metal available for undesired chemical reactions which may result in decreased cycling lifetime and/or poor cell performance. The application of force to the electrochemical device has been found, in accordance with certain embodiments described herein, to reduce such behavior and to improve the cycling lifetime and/or performance of the cell.
In some embodiments, the battery pack (e.g., a housing of the battery pack) is configured to apply, during at least one period of time during charge and/or discharge of the device, an anisotropic force with a component normal to an electrode active surface of one of the electrochemical cells (e.g., first electrochemical cell, second electrochemical cell).
In some embodiments, an anisotropic force with a component normal to an electrode active surface of one of the electrochemical cells (e.g., first electrochemical cell, second electrochemical cell) is applied during at least one period of time during charge and/or discharge of the battery pack. In some embodiments, the force may be applied continuously, over one period of time, or over multiple periods of time that may vary in duration and/or frequency. The anisotropic force may be applied, in some cases, at one or more pre-determined locations, optionally distributed over an active surface of the one or more of the electrochemical cells of the battery pack. In some embodiments, the anisotropic force is applied uniformly over one or more active surfaces of the anode.
An “anisotropic force” is given its ordinary meaning in the art and means a force that is not equal in all directions. A force equal in all directions is, for example, internal pressure of a fluid or material within the fluid or material, such as internal gas pressure of an object. Examples of forces not equal in all directions include forces directed in a particular direction, such as the force on a table applied by an object on the table via gravity. Another example of an anisotropic force includes certain forces applied by a band arranged around a perimeter of an object. For example, a rubber band or turnbuckle can apply forces around a perimeter of an object around which it is wrapped. However, the band may not apply any direct force on any part of the exterior surface of the object not in contact with the band. In addition, when the band is expanded along a first axis to a greater extent than a second axis, the band can apply a larger force in the direction parallel to the first axis than the force applied parallel to the second axis.
A force with a “component normal” to a surface, for example an active surface of an electrode such as an anode, is given its ordinary meaning as would be understood by those of ordinary skill in the art and includes, for example, a force which, at least in part, exerts itself in a direction substantially perpendicular to the surface. Those of ordinary skill can understand other examples of these terms, especially as applied within the description of this document.
In some embodiments, the anisotropic force can be applied such that the magnitude of the force is substantially equal in all directions within a plane defining a cross-section of the battery pack, but the magnitude of the forces in out-of-plane directions is substantially unequal to the magnitudes of the in-plane forces.
In one set of embodiments, battery packs (e.g., housings) described herein are configured to apply, during at least one period of time during charge and/or discharge of the cell, an anisotropic force with a component normal to an electrode active surface of one of the electrochemical cells (e.g., first electrochemical cell, second electrochemical cell). Those of ordinary skill in the art will understand the meaning of this. In such an arrangement, the electrochemical cell may be formed as part of a container which applies such a force by virtue of a “load” applied during or after assembly of the cell, or applied during use of the battery pack as a result of expansion and/or contraction of one or more components of the battery pack itself.
The magnitude of the applied force is, in some embodiments, large enough to enhance the performance of the battery pack. An electrode active surface (e.g., anode active surface) and the anisotropic force may be, in some instances, together selected such that the anisotropic force affects surface morphology of the electrode active surface to inhibit increase in electrode active surface area through charge and discharge and wherein, in the absence of the anisotropic force but under otherwise essentially identical conditions, the electrode active surface area is increased to a greater extent through charge and discharge cycles. “Essentially identical conditions,” in this context, means conditions that are similar or identical other than the application and/or magnitude of the force. For example, otherwise identical conditions may mean a battery pack that is identical, but where it is not constructed (e.g., by couplings such as brackets or other connections) to apply the anisotropic force on the subject battery pack.
As described herein, in some embodiments, the surface of an anode can be enhanced during cycling (e.g., for lithium, the development of mossy or a rough surface of lithium may be reduced or eliminated) by application of an externally-applied (in some embodiments, uniaxial) pressure. The externally-applied pressure may, in some embodiments, be chosen to be greater than the yield stress of a material forming the anode. For example, for an anode comprising lithium, the cell may be under an externally-applied anisotropic force with a component defining a pressure of at least 3 kgf/cm2, at least 5 kgf/cm2, at least 8 kgf/cm2, at least 10 kgf/cm2, at least 20 kgf/cm2, or more. In some instances, this is because the yield stress of lithium is around 7-8 kgf/cm2. Thus, at pressures (e.g., uniaxial pressures) greater than this value, mossy Li, or any surface roughness at all, may be reduced or suppressed. The lithium surface roughness may mimic the surface that is pressing against it. Accordingly, when cycling such that at least a portion of the cycle the surface of the anode is under at least about 10 kgf/cm2, at least about 20 kgf/cm2, and/or up 30 kgf/cm2, up to 40 kgf/cm2 of externally-applied pressure, the lithium surface may become smoother with cycling when the pressing surface is smooth.
In some cases, one or more forces applied to the cell have a component that is not normal to an active surface of an anode. For example, in
In some cases, electrochemical cells may be pre-compressed before they are inserted into housings, and, upon being inserted to the housing, they may expand to produce a net force on the electrochemical cells. Such an arrangement may be advantageous, for example, if the electrochemical cells are capable of withstanding relatively high variations in pressure.
In some instances, frame 1, stop portions 2, inserts 3, and/or solid plate 4 are configured to apply an anisotropic force with a component normal to an active surface of electrochemical cells 8 of stack 850 during at least a portion of a charging or discharging process of battery pack 800. Such an anisotropic force may define a pressure of at least 3 kgf/cm2 at state of charge of 0% for at least some or all of the cells and of at least 12 kgf/cm2 (such as up to 15 kgf/cm2, up to 25 kgf/cm2, or higher) at a stage of charge of 100% for at least some or all of the cells in stack 850. In some embodiments, a first subset of electrochemical cells 8 are part of a first battery module within battery pack 800 (e.g., where the electrochemical cells are coupled in series to a first pair of terminals comprising a positive terminal and a negative terminal), and a second subset of electrochemical cells 8 are part of a second battery module within battery pack 800 (e.g., where the electrochemical cells are coupled in series to a second pair of terminals comprising a positive terminal and a negative terminal, not shown). The first battery module and second battery module within battery pack 800 may be charged and/or discharged independently (e.g., with or without multiplexing), in some instances at different rates.
In some instances, frame 21, stop portions 22, inserts 23, and/or solid plate 24 are configured to apply an anisotropic force with a component normal to an active surface of electrochemical cells 28 of stack 950 during at least a portion of a charging or discharging process of battery pack 900. Such an anisotropic force may define a pressure of at least 3 kgf/cm2 at state of charge of 0% for at least some or all of the cells and of at least 12 kgf/cm2 (such as up to 15 kgf/cm2, up to 25 kgf/cm2, or higher) at a stage of charge of 100% for at least some or all of the cells in stack 950. In some embodiments, a first subset of electrochemical cells 28 are part of a first battery module within battery pack 900 (e.g., where the electrochemical cells are coupled in series to a first pair of terminals comprising a positive terminal and a negative terminal), and a second subset of electrochemical cells 28 are part of a second battery module within battery pack 900 (e.g., where the electrochemical cells are coupled in series to a second pair of terminals comprising a positive terminal and a negative terminal, not shown). The first battery module and second battery module within battery pack 900 may be charged and/or discharged independently (e.g., with or without multiplexing), in some instances at different rates.
In some embodiments, the battery packs (e.g., comprising rechargeable batteries) described in this disclosure can be used to provide power to an electric vehicle or otherwise be incorporated into an electric vehicle. As a non-limiting example, battery packs described in this disclosure can, in certain embodiments, be used to provide power to a drive train of an electric vehicle. The vehicle may be any suitable vehicle, adapted for travel on land, sea, air, and/or space. For example, the vehicle may be an automobile, truck, motorcycle, boat, helicopter, airplane, spacecraft and/or any other suitable type of vehicle.
The following applications are incorporated herein by reference, in their entirety, for all purposes: U.S. Publication No. US-2007-0221265-A1 published on Sep. 27, 2007, filed as U.S. application Ser. No. 11/400,781 on Apr. 6, 2006, and entitled “RECHARGEABLE LITHIUM/WATER, LITHIUM/AIR BATTERIES”; U.S. Publication No. US-2009-0035646-A1, published on Feb. 5, 2009, filed as U.S. application Ser. No. 11/888,339 on Jul. 31, 2007, and entitled “SWELLING INHIBITION IN BATTERIES”; U.S. Publication No. US-2010-0129699-A1 published on May 17, 2010, filed as U.S. application Ser. No. 12/312,764 on Feb. 2, 2010; patented as U.S. Pat. No. 8,617,748 on Dec. 31, 2013, and entitled “SEPARATION OF ELECTROLYTES”; U.S. Publication No. US-2010-0291442-A1 published on Nov. 18, 2010, filed as U.S. application Ser. No. 12/682,011 on Jul. 30, 2010, patented as U.S. Pat. No. 8,871,387 on Oct. 28, 2014, and entitled “PRIMER FOR BATTERY ELECTRODE”; U.S. Publication No. US-2009-0200986-A1 published on Aug. 13, 2009, filed as U.S. application Ser. No. 12/069,335 on Feb. 8, 2008, patented as U.S. Pat. No. 8,264,205 on Sep. 11, 2012, and entitled “CIRCUIT FOR CHARGE AND/OR DISCHARGE PROTECTION IN AN ENERGY-STORAGE DEVICE”; U.S. Publication No. US-2007-0224502-A1 published on Sep. 27, 2007, filed as U.S. application Ser. No. 11/400,025 on Apr. 6, 2006, patented as U.S. Pat. No. 7,771,870 on Aug. 10, 2010, and entitled “ELECTRODE PROTECTION IN BOTH AQUEOUS AND NON-AQUEOUS ELECTROCHEMICAL CELLS, INCLUDING RECHARGEABLE LITHIUM BATTERIES”; U.S. Publication No. US-2008-0318128-A1 published on Dec. 25, 2008, filed as U.S. application Ser. No. 11/821,576 on Jun. 22, 2007, and entitled “LITHIUM ALLOY/SULFUR BATTERIES”; U.S. Publication No. US-2002-0055040-A1 published on May 9, 2002, filed as U.S. application Ser. No. 09/795,915 on Feb. 27, 2001, patented as U.S. Pat. No. 7,939,198 on May 10, 2011, and entitled “NOVEL COMPOSITE CATHODES, ELECTROCHEMICAL CELLS COMPRISING NOVEL COMPOSITE CATHODES, AND PROCESSES FOR FABRICATING SAME”; U.S. Publication No. US-2006-0238203-A1 published on Oct. 26, 2006, filed as U.S. application Ser. No. 11/111,262 on Apr. 20, 2005, patented as U.S. Pat. No. 7,688,075 on Mar. 30, 2010, and entitled “LITHIUM SULFUR RECHARGEABLE BATTERY FUEL GAUGE SYSTEMS AND METHODS”; U.S. Publication No. US-2008-0187663-A1 published on Aug. 7, 2008, filed as U.S. application Ser. No. 11/728,197 on Mar. 23, 2007, patented as U.S. Pat. No. 8,084,102 on Dec. 27, 2011, and entitled “METHODS FOR CO-FLASH EVAPORATION OF POLYMERIZABLE MONOMERS AND NON-POLYMERIZABLE CARRIER SOLVENT/SALT MIXTURES/SOLUTIONS”; U.S. Publication No. US-2011-0006738-A1 published on Jan. 13, 2011, filed as U.S. application Ser. No. 12/679,371 on Sep. 23, 2010, and entitled “ELECTROLYTE ADDITIVES FOR LITHIUM BATTERIES AND RELATED METHODS”; U.S. Publication No. US-2011-0008531-A1 published on Jan. 13, 2011, filed as U.S. application Ser. No. 12/811,576 on Sep. 23, 2010, patented as U.S. Pat. No. 9,034,421 on May 19, 2015, and entitled “METHODS OF FORMING ELECTRODES COMPRISING SULFUR AND POROUS MATERIAL COMPRISING CARBON”; U.S. Publication No. US-2010-0035128-A1 published on Feb. 11, 2010, filed as U.S. application Ser. No. 12/535,328 on Aug. 4, 2009, patented as U.S. Pat. No. 9,105,938 on Aug. 11, 2015, and entitled “APPLICATION OF FORCE IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2011-0165471-A9 published on Jul. 15, 2011, filed as U.S. application Ser. No. 12/180,379 on Jul. 25, 2008, and entitled “PROTECTION OF ANODES FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2006-0222954-A1 published on Oct. 5, 2006, filed as U.S. application Ser. No. 11/452,445 on Jun. 13, 2006, patented as U.S. Pat. No. 8,415,054 on Apr. 9, 2013, and entitled “LITHIUM ANODES FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2010-0239914-A1 published on Sep. 23, 2010, filed as U.S. application Ser. No. 12/727,862 on Mar. 19, 2010, and entitled “CATHODE FOR LITHIUM BATTERY”; U.S. Publication No. US-2010-0294049-A1 published on Nov. 25, 2010, filed as U.S. application Ser. No. 12/471,095 on May 22, 2009, patented as U.S. Pat. No. 8,087,309 on Jan. 3, 2012, and entitled “HERMETIC SAMPLE HOLDER AND METHOD FOR PERFORMING MICROANALYSIS UNDER CONTROLLED ATMOSPHERE ENVIRONMENT”; U.S. Publication No. US-2011-0076560-A1 published on Mar. 31, 2011, filed as U.S. application Ser. No. 12/862,581 on Aug. 24, 2010, and entitled “ELECTROCHEMICAL CELLS COMPRISING POROUS STRUCTURES COMPRISING SULFUR”; U.S. Publication No. US-2011-0068001-A1 published on Mar. 24, 2011, filed as U.S. application Ser. No. 12/862,513 on Aug. 24, 2010, and entitled “RELEASE SYSTEM FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2012-0048729-A1 published on Mar. 1, 2012, filed as U.S. application Ser. No. 13/216,559 on Aug. 24, 2011, and entitled “ELECTRICALLY NON-CONDUCTIVE MATERIALS FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2011-0177398-A1 published on Jul. 21, 2011, filed as U.S. application Ser. No. 12/862,528 on Aug. 24, 2010, patented as U.S. Pat. No. 10,629,947 on Apr. 21, 2020, and entitled “ELECTROCHEMICAL CELL”; U.S. Publication No. US-2011-0070494-A1 published on Mar. 24, 2011, filed as U.S. application Ser. No. 12/862,563 on Aug. 24, 2010, and entitled “ELECTROCHEMICAL CELLS COMPRISING POROUS STRUCTURES COMPRISING SULFUR”; U.S. Publication No. US-2011-0070491-A1 published on Mar. 24, 2011, filed as U.S. application Ser. No. 12/862,551 on Aug. 24, 2010, and entitled “ELECTROCHEMICAL CELLS COMPRISING POROUS STRUCTURES COMPRISING SULFUR”; U.S. Publication No. US-2011-0059361-A1 published on Mar. 10, 2011, filed as U.S. application Ser. No. 12/862,576 on Aug. 24, 2010, patented as U.S. Pat. No. 9,005,809 on Apr. 14, 2015, and entitled “ELECTROCHEMICAL CELLS COMPRISING POROUS STRUCTURES COMPRISING SULFUR”; U.S. Publication No. US-2012-0052339-A1 published on Mar. 1, 2012, filed as U.S. application Ser. No. 13/216,579 on Aug. 24, 2011, and entitled “ELECTROLYTE MATERIALS FOR USE IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2012-0070746-A1 published on Mar. 22, 2012, filed as U.S. application Ser. No. 13/240,113 on Sep. 22, 2011, and entitled “LOW ELECTROLYTE ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2011-0206992-A1 published on Aug. 25, 2011, filed as U.S. application Ser. No. 13/033,419 on Feb. 23, 2011, and entitled “POROUS STRUCTURES FOR ENERGY STORAGE DEVICES”; U.S. Publication No. US-2012-0082872-A1 published on Apr. 5, 2012, filed as U.S. application Ser. No. 13/249,605 on Sep. 30, 2011, and entitled “ADDITIVE FOR ELECTROLYTES”; U.S. Publication No. US-2012-0082901-A1 published on Apr. 5, 2012, filed as U.S. application Ser. No. 13/249,632 on Sep. 30, 2011, and entitled “LITHIUM-BASED ANODE WITH IONIC LIQUID POLYMER GEL”; U.S. Publication No. US-2013-0164635-A1 published on Jun. 27, 2013, filed as U.S. application Ser. No. 13/700,696 on Mar. 6, 2013, patented as U.S. Pat. No. 9,577,243 on Feb. 21 2017, and entitled “USE OF EXPANDED GRAPHITE IN LITHIUM/SULPHUR BATTERIES”; U.S. Publication No. US-2013-0017441-A1 published on Jan. 17, 2013, filed as U.S. application Ser. No. 13/524,662 on Jun. 15, 2012, patented as U.S. Pat. No. 9,548,492 on Jan. 17, 2017, and entitled “PLATING TECHNIQUE FOR ELECTRODE”; U.S. Publication No. US-2013-0224601-A1 published on Aug. 29, 2013, filed as U.S. application Ser. No. 13/766,862 on Feb. 14, 2013, patented as U.S. Pat. No. 9,077,041 on Jul. 7, 2015, and entitled “ELECTRODE STRUCTURE FOR ELECTROCHEMICAL CELL”; U.S. Publication No. US-2013-0252103-A1 published on Sep. 26, 2013, filed as U.S. application Ser. No. 13/789,783 on Mar. 8, 2013, patented as U.S. Pat. No. 9,214,678 on Dec. 15, 2015, and entitled “POROUS SUPPORT STRUCTURES, ELECTRODES CONTAINING SAME, AND ASSOCIATED METHODS”; U.S. Publication No. US-2015-0287998-A1 published on Oct. 8, 2015, filed as U.S. application Ser. No. 14/743,304 on Jun. 18, 2015, patented as U.S. Pat. No. 9,577,267 on Feb. 21, 2017, and entitled “ELECTRODE STRUCTURE AND METHOD FOR MAKING SAME”; U.S. Publication No. US-2013-0095380-A1 published on Apr. 18, 2013, filed as U.S. application Ser. No. 13/644,933 on Oct. 4, 2012, patented as U.S. Pat. No. 8,936,870 on Jan. 20, 2015, and entitled “ELECTRODE STRUCTURE AND METHOD FOR MAKING THE SAME”; U.S. Publication No. US-2012-0052397-A1 published on Mar. 1, 2012, filed as U.S. application Ser. No. 13/216,538 on Aug. 24, 2011, patented as U.S. Pat. No. 9,853,287 on Dec. 26, 2017, and entitled “ELECTROLYTE MATERIALS FOR USE IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2014-0123477-A1 published on May 8, 2014, filed as U.S. application Ser. No. 14/069,698 on Nov. 1, 2013, patented as U.S. Pat. No. 9,005,311 on Apr. 14, 2015, and entitled “ELECTRODE ACTIVE SURFACE PRETREATMENT”; U.S. Publication No. US-2014-0193723-A1 published on Jul. 10, 2014, filed as U.S. application Ser. No. 14/150,156 on Jan. 8, 2014, patented as U.S. Pat. No. 9,559,348 on Jan. 31, 2017, and entitled “CONDUCTIVITY CONTROL IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2014-0255780-A1 published on Sep. 11, 2014, filed as U.S. application Ser. No. 14/197,782 on Mar. 5, 2014, patented as U.S. Pat. No. 9,490,478 on Nov. 8, 2016, and entitled “ELECTROCHEMICAL CELLS COMPRISING FIBRIL MATERIALS”; U.S. Publication No. US-2014-0272594-A1 published on Sep. 18 2014, filed as U.S. application Ser. No. 13/833,377 on Mar. 15, 2013, and entitled “PROTECTIVE STRUCTURES FOR ELECTRODES”; U.S. Publication No. US-2014-0272597-A1 published on Sep. 18, 2014, filed as U.S. application Ser. No. 14/209,274 on Mar. 13, 2014, patented as U.S. Pat. No. 9,728,768 on Aug. 8, 2017, and entitled “PROTECTED ELECTRODE STRUCTURES AND METHODS”; U.S. Publication No. US-2015-0280277-A1 published on Oct. 1, 2015, filed as U.S. application Ser. No. 14/668,102 on Mar. 25, 2015, patented as U.S. Pat. No. 9,755,268 on Sep. 5, 2017, and entitled “GEL ELECTROLYTES AND ELECTRODES”; U.S. Publication No. US-2015-0180037-A1 published on Jun. 25, 2015, filed as U.S. application Ser. No. 14/576,570 on Dec. 19, 2014, patented as U.S. Pat. No. 10,020,512 on Jul. 10, 2018, and entitled “POLYMER FOR USE AS PROTECTIVE LAYERS AND OTHER COMPONENTS IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2015-0349310-A1 published on Dec. 3, 2015, filed as U.S. application Ser. No. 14/723,132 on May 27, 2015, patented as U.S. Pat. No. 9,735,411 on Aug. 15, 2017, and entitled “POLYMER FOR USE AS PROTECTIVE LAYERS AND OTHER COMPONENTS IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2014-0272595-A1 published on Sep. 18, 2014, filed as U.S. application Ser. No. 14/203,802 on Mar. 11, 2014, and entitled “COMPOSITIONS FOR USE AS PROTECTIVE LAYERS AND OTHER COMPONENTS IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2019-0006699-A1 published on Jan. 3, 2019, filed as U.S. application Ser. No. 15/727,438 on Oct. 6, 2017, and entitled “PRESSURE AND/OR TEMPERATURE MANAGEMENT IN ELECTROCHEMICAL SYSTEMS”; U.S. Publication No. US-2014-0193713-A1 published on Jul. 10, 2014, filed as U.S. application Ser. No. 14/150,196 on Jan. 8, 2014, patented as U.S. Pat. No. 9,531,009 on Dec. 27, 2016, and entitled “PASSIVATION OF ELECTRODES IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2014-0127577-A1 published on May 8, 2014, filed as U.S. application Ser. No. 14/068,333 on Oct. 31, 2013, patented as U.S. Pat. No. 10,243,202 on Mar. 26, 2019, and entitled “POLYMERS FOR USE AS PROTECTIVE LAYERS AND OTHER COMPONENTS IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2015-0318539-A1 published on Nov. 5, 2015, filed as U.S. application Ser. No. 14/700,258 on Apr. 30, 2015, patented as U.S. Pat. No. 9,711,784 on Jul. 18, 2017, and entitled “ELECTRODE FABRICATION METHODS AND ASSOCIATED SYSTEMS AND ARTICLES”; U.S. Publication No. US-2014-0272565-A1 published on Sep. 18, 2014, filed as U.S. application Ser. No. 14/209,396 on Mar. 13, 2014, patented as U.S. Pat. No. 10,862,105 on Dec. 8, 2020 and entitled “PROTECTED ELECTRODE STRUCTURES”; U.S. Publication No. US-2015-0010804-A1 published on Jan. 8, 2015, filed as U.S. application Ser. No. 14/323,269 on Jul. 3, 2014, patented as U.S. Pat. No. 9,994,959 on Jun. 12, 2018, and entitled “CERAMIC/POLYMER MATRIX FOR ELECTRODE PROTECTION IN ELECTROCHEMICAL CELLS, INCLUDING RECHARGEABLE LITHIUM BATTERIES”; U.S. Publication No. US-2015-0162586-A1 published on Jun. 11, 2015, filed as U.S. application Ser. No. 14/561,305 on Dec. 5, 2014, and entitled “NEW SEPARATOR”; U.S. Publication No. US-2015-0044517-A1 published on Feb. 12, 2015, filed as U.S. application Ser. No. 14/455,230 on Aug. 8, 2014, patented as U.S. Pat. No. 10,020,479 on Jul. 10, 2018, and entitled “SELF-HEALING ELECTRODE PROTECTION IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2015-0236322-A1 published on Aug. 20, 2015, filed as U.S. application Ser. No. 14/184,037 on Feb. 19, 2014, patented as U.S. Pat. No. 10,490,796 on Nov. 26, 2019, and entitled “ELECTRODE PROTECTION USING ELECTROLYTE-INHIBITING ION CONDUCTOR”; U.S. Publication No. US-2015-0236320-A1 published on Aug. 20, 2015, filed as U.S. application Ser. No. 14/624,641 on Feb. 18, 2015, patented as U.S. Pat. No. 9,653,750 on May 16, 2017, and entitled “ELECTRODE PROTECTION USING A COMPOSITE COMPRISING AN ELECTROLYTE-INHIBITING ION CONDUCTOR”; U.S. Publication No. US-2016-0118638-A1 published on Apr. 28, 2016, filed as U.S. application Ser. No. 14/921,381 on Oct. 23, 2015, and entitled “COMPOSITIONS FOR USE AS PROTECTIVE LAYERS AND OTHER COMPONENTS IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2016-0118651-A1 published on Apr. 28, 2016, filed as U.S. application Ser. No. 14/918,672 on Oct. 21, 2015, and entitled “ION-CONDUCTIVE COMPOSITE FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2016-0072132-A1 published on Mar. 10, 2016, filed as U.S. application Ser. No. 14/848,659 on Sep. 9, 2015, and entitled “PROTECTIVE LAYERS IN LITHIUM-ION ELECTROCHEMICAL CELLS AND ASSOCIATED ELECTRODES AND METHODS”; U.S. Publication No. US-2018-0138542-A1 published on May 17, 2018, filed as U.S. application Ser. No. 15/567,534 on Oct. 18, 2017, patented as U.S. Pat. No. 10,847,833 on Nov. 24, 2020 and entitled “GLASS-CERAMIC ELECTROLYTES FOR LITHIUM-SULFUR BATTERIES”; U.S. Publication No. US-2016-0344067-A1 published on Nov. 24, 2016, filed as U.S. application Ser. No. 15/160,191 on May 20, 2016, patented as U.S. Pat. No. 10,461,372 on Oct. 29, 2019, and entitled “PROTECTIVE LAYERS FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2020-0099108-A1 published on Mar. 26, 2020, filed as U.S. application Ser. No. 16/587,939 on Sep. 30, 2019, and entitled “PROTECTIVE LAYERS FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2017-0141385-A1 published on May 18, 2017, filed as U.S. application Ser. No. 15/343,890 on Nov. 4, 2016, and entitled “LAYER COMPOSITE AND ELECTRODE HAVING A SMOOTH SURFACE, AND ASSOCIATED METHODS”; U.S. Publication No. US-2017-0141442-A1 published on May 18, 2017, filed as U.S. application Ser. No. 15/349,140 on Nov. 11, 2016, and entitled “ADDITIVES FOR ELECTROCHEMICAL CELLS”; patented as U.S. patent Ser. No. 10/320,031 on Jun. 11, 2019, and entitled “ADDITIVES FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2017-0149086-A1 published on May 25, 2017, filed as U.S. application Ser. No. 15/343,635 on Nov. 4, 2016, patented as U.S. Pat. No. 9,825,328 on Nov. 21, 2017, and entitled “IONICALLY CONDUCTIVE COMPOUNDS AND RELATED USES”; U.S. Publication No. US-2018-0337406-A1 published on Nov. 22, 2018, filed as U.S. application Ser. No. 15/983,352 on May 18, 2018, patented as U.S. Pat. No. 10,868,306 on Dec. 15, 2020 and entitled “PASSIVATING AGENTS FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2018-0261820-A1 published on Sep. 13, 2018, filed as U.S. application Ser. No. 15/916,588 on Mar. 9, 2018, and entitled “ELECTROCHEMICAL CELLS COMPRISING SHORT-CIRCUIT RESISTANT ELECTRONICALLY INSULATING REGIONS”; U.S. Publication No. US-2020-0243824-A1 published on Jul. 30, 2020, filed as U.S. application Ser. No. 16/098,654 on Nov. 2, 2018, patented as U.S. Pat. No. 10,991,925 on Apr. 27, 2021 and entitled “COATINGS FOR COMPONENTS OF ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2018-0351158-A1 published on Dec. 6, 2018, filed as U.S. application Ser. No. 15/983,363 on May 18, 2018, patented as U.S. Pat. No. 10,944,094 on Mar. 9, 2021 and entitled “PASSIVATING AGENTS FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2018-0277850-A1, published on Sep. 27, 2018, filed as U.S. application Ser. No. 15/923,342 on Mar. 16, 2018, and patented as U.S. Pat. No. 10,720,648 on Jul. 21, 2020, and entitled “ELECTRODE EDGE PROTECTION IN ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2018-0358651-A1, published on Dec. 13, 2018, filed as U.S. application Ser. No. 16/002,097 on Jun. 7, 2018, and patented as U.S. Pat. No. 10,608,278 on Mar. 31, 2020, and entitled “IN SITU CURRENT COLLECTOR”; U.S. Publication No. US-2017-0338475-A1, published on Nov. 23, 2017, filed as U.S. application Ser. No. 15/599,595 on May 19, 2017, patented as U.S. Pat. No. 10,879,527 on Dec. 29, 2020 and entitled “PROTECTIVE LAYERS FOR ELECTRODES AND ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2019-0088958-A1, published on Mar. 21, 2019, filed as U.S. application Ser. No. 16/124,384 on Sep. 7, 2018, and entitled “PROTECTIVE MEMBRANE FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2019-0348672-A1, published on Nov. 14, 2019, filed as U.S. application Ser. No. 16/470,708 on Jun. 18, 2019, and entitled “PROTECTIVE LAYERS COMPRISING METALS FOR ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2017-0200975-A1, published Jul. 13, 2017, filed as U.S. application Ser. No. 15/429,439 on Feb. 10, 2017, and patented as U.S. Pat. No. 10,050,308 on Aug. 14, 2018, and entitled “LITHIUM-ION ELECTROCHEMICAL CELL, COMPONENTS THEREOF, AND METHODS OF MAKING AND USING SAME”; U.S. Publication No. US-2018-0351148-A1, published Dec. 6, 2018, filed as U.S. application Ser. No. 15/988,182 on May 24, 2018, and entitled “IONICALLY CONDUCTIVE COMPOUNDS AND RELATED USES”; U.S. Publication No. US-2018-0254516-A1, published Sep. 6, 2018, filed as U.S. application Ser. No. 15/765,362 on Apr. 2, 2018, and entitled “NON-AQUEOUS ELECTROLYTES FOR HIGH ENERGY LITHIUM-ION BATTERIES”; U.S. Publication No. US-2020-0044460-A1, published Feb. 6, 2020, filed as U.S. Application No. 16,527,903 on Jul. 31, 2019, and entitled “MULTIPLEXED CHARGE DISCHARGE BATTERY MANAGEMENT SYSTEM”; U.S. Publication No. US-2020-0220146-A1, published Jul. 9, 2020, filed as U.S. application Ser. No. 16/724,586 on Dec. 23, 2019, and entitled “ISOLATABLE ELECTRODES AND ASSOCIATED ARTICLES AND METHODS”; U.S. Publication No. US-2020-0220149-A1, published Jul. 9, 2020, filed as U.S. application Ser. No. 16/724,596 on Dec. 23, 2019, and entitled “ELECTRODES, HEATERS, SENSORS, AND ASSOCIATED ARTICLES AND METHODS”; U.S. Publication No. US-2020-0220197-A1, published Jul. 9, 2020, filed as U.S. application Ser. No. 16/724,612 on Dec. 23, 2019, and entitled “FOLDED ELECTROCHEMICAL DEVICES AND ASSOCIATED METHODS AND SYSTEMS”; U.S. Publication No. US-2020-0373578-A1 published Nov. 26, 2020, filed as U.S. application Ser. No. 16/879,861 on May 21, 2020, and entitled “ELECTROCHEMICAL DEVICES INCLUDING POROUS LAYERS”, International Patent Application Publication No. WO2020/237014, filed as International Application No. PCT/US2020/033938 on May 21, 2020, and entitled “ELECTRICALLY COUPLED ELECTRODES, AND ASSOCIATED ARTICLES AND METHODS”; U.S. Publication No. US-2020-0373551-A1 published Nov. 26, 2020, filed as U.S. application Ser. No. 16/879,839 on May 21, 2020, and entitled “ELECTRICALLY COUPLED ELECTRODES, AND ASSOCIATED ARTICLES AND METHODS”, International Patent Application Publication No. WO2020/257414, filed as International Patent Application No. PCT/US2020/038375 on Jun. 18, 2020, and entitled “METHODS, SYSTEMS, AND DEVICES FOR APPLYING FORCES TO ELECTROCHEMICAL DEVICES,” U.S. Publication No. US-2020-0395585-A1 published Dec. 17, 2020, filed as U.S. application Ser. No. 16/057,050 on Aug. 7, 2018, and entitled “LITHIUM-COATED SEPARATORS AND ELECTROCHEMICAL CELLS COMPRISING THE SAME”, U.S. Publication No. US-2021-0057753-A1 published Feb. 25, 2021, filed as U.S. application Ser. No. 16/994,006 on Aug. 14, 2020, and entitled “ELECTROCHEMICAL CELLS AND COMPONENTS COMPRISING THIOL GROUP-CONTAINING SPECIES”, U.S. Publication No. US-2021-0135297-A1 published on May 6, 2021, filed as U.S. application Ser. No. 16/670,905 on Oct. 31, 2019, and entitled SYSTEM AND METHOD FOR OPERATING A RECHARGEABLE ELECTROCHEMICAL CELL OR BATTERY″, U.S. Publication No. US-2021-0138673-A1 published on May 13, 2021, filed as U.S. application Ser. No. 17/089,092 on Nov. 4, 2020, and entitled “ELECTRODE CUTTING INSTRUMENT”, U.S. Publication No. US-2021-0135294-A1 published on May 6, 2021, filed as U.S. application Ser. No. 16/670,933 on Oct. 31, 2019, and entitled “SYSTEM AND METHOD FOR OPERATING A RECHARGEABLE ELECTROCHEMICAL CELL OR BATTERY”; U.S. Publication No. US-2021-0151839-A1 published on May 20, 2021, filed as U.S. application Ser. No. 16/952,177 on Nov. 19, 2020, and entitled “BATTERIES, AND ASSOCIATED SYSTEMS AND METHODS”; U.S. Publication No. US-2021-0151830-A1 published on May 20, 2021, filed as U.S. application Ser. No. 16/952,235 on Nov. 19, 2020, and entitled “BATTERIES WITH COMPONENTS INCLUDING CARBON FIBER, AND ASSOCIATED SYSTEMS AND METHODS”; U.S. Publication No. US-2021-0151817-A1 published on May 20, 2021, filed as U.S. application Ser. No. 16/952,228 on Nov. 19, 2020, and entitled “BATTERY ALIGNMENT, AND ASSOCIATED SYSTEMS AND METHODS”; U.S. Publication No. US-2021-0151841-A1 published on May 20, 2021, filed as U.S. application Ser. No. 16/952,240 on Nov. 19, 2020, and entitled “SYSTEMS AND METHODS FOR APPLYING AND MAINTAINING COMPRESSION PRESSURE ON ELECTROCHEMICAL CELLS”; U.S. Publication No. US-2021-0151816-A1 published on May 20, 2021, filed as U.S. application Ser. No. 16/952,223 on Nov. 19, 2020, and entitled “THERMALLY INSULATING COMPRESSIBLE COMPONENTS FOR BATTERY PACKS”; U.S. Publication No. US-2021-0151840-A1 published on May 20, 2021, filed as U.S. application Ser. No. 16/952,187 on Nov. 19, 2020, and entitled “COMPRESSION SYSTEMS FOR BATTERIES”; U.S. Publication No. US-2021-0193984-A1 published on Jun. 24, 2021, filed as U.S. application Ser. No. 17/125,124 on Dec. 17, 2020, and entitled “SYSTEMS AND METHODS FOR FABRICATING LITHIUM METAL ELECTRODES”; U.S. Publication No. US-2021-0193985-A1 published on Jun. 24, 2021, filed as U.S. application Ser. No. 17/125,110 on Dec. 17, 2020, and entitled “LITHIUM METAL ELECTRODES AND METHODS”; U.S. Publication No. US-2021-0193996-A1 published on Jun. 24, 2021, filed as U.S. application Ser. No. 17/125,070 on Dec. 17, 2020, and entitled “LITHIUM METAL ELECTRODES”; U.S. Publication No. US-2021-0194069-A1 published on Jun. 24, 2021, filed as U.S. application Ser. No. 17/126,390 on Dec. 18, 2020, and entitled “SYSTEMS AND METHODS FOR PROVIDING, ASSEMBLING, AND MANAGING INTEGRATED POWER BUS FOR RECHARGEABLE ELECTROCHEMICAL CELL OR BATTERY”; U.S. Publication No. US-2021-0218243 published on Jul. 15, 2021, filed as U.S. application Ser. No. 17/126,424 on Dec. 18, 2020, and entitled “SYSTEMS AND METHODS FOR PROTECTING A CIRCUIT, RECHARGEABLE ELECTROCHEMICAL CELL, OR BATTERY”.
U.S. Provisional Patent Application No. 63/166,549, filed Mar. 26, 2021, and entitled, “Battery Pack and Related Components and Methods” is incorporated herein by reference in its entirety for all purposes. U.S. Provisional Patent Application No. 63/223,663, filed Jul. 20, 2021, and entitled, “Battery Pack and Related Components and Methods” is incorporated herein by reference in its entirety for all purposes.
It should be understood that when a portion (e.g., layer, structure, region) is “on”, “adjacent”, “above”, “over”, “overlying”, or “supported by” another portion, it can be directly on the portion, or an intervening portion (e.g., layer, structure, region) also may be present. Similarly, when a portion is “below” or “underneath” another portion, it can be directly below the portion, or an intervening portion (e.g., layer, structure, region) also may be present. A portion that is “directly on”, “directly adjacent”, “immediately adjacent”, “in direct contact with”, or “directly supported by” another portion means that no intervening portion is present. It should also be understood that when a portion is referred to as being “on”, “above”, “adjacent”, “over”, “overlying”, “in contact with”, “below”, or “supported by” another portion, it may cover the entire portion or a part of the portion.
While several embodiments of the present invention have been described and illustrated herein, those of ordinary skill in the art will readily envision a variety of other means and/or structures for performing the functions and/or obtaining the results and/or one or more of the advantages described herein, and each of such variations and/or modifications is deemed to be within the scope of the present invention. More generally, those skilled in the art will readily appreciate that all parameters, dimensions, materials, and configurations described herein are meant to be exemplary and that the actual parameters, dimensions, materials, and/or configurations will depend upon the specific application or applications for which the teachings of the present invention is/are used. Those skilled in the art will recognize, or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the invention described herein. It is, therefore, to be understood that the foregoing embodiments are presented by way of example only and that, within the scope of the appended claims and equivalents thereto, the invention may be practiced otherwise than as specifically described and claimed. The present invention is directed to each individual feature, system, article, material, and/or method described herein. In addition, any combination of two or more such features, systems, articles, materials, and/or methods, if such features, systems, articles, materials, and/or methods are not mutually inconsistent, is included within the scope of the present invention.
The indefinite articles “a” and “an,” as used herein in the specification and in the claims, unless clearly indicated to the contrary, should be understood to mean “at least one.”
The phrase “and/or,” as used herein in the specification and in the claims, should be understood to mean “either or both” of the elements so conjoined, i.e., elements that are conjunctively present in some cases and disjunctively present in other cases. Other elements may optionally be present other than the elements specifically identified by the “and/or” clause, whether related or unrelated to those elements specifically identified unless clearly indicated to the contrary. Thus, as a non-limiting example, a reference to “A and/or B,” when used in conjunction with open-ended language such as “comprising” can refer, in one embodiment, to A without B (optionally including elements other than B); in another embodiment, to B without A (optionally including elements other than A); in yet another embodiment, to both A and B (optionally including other elements); etc.
As used herein in the specification and in the claims, “or” should be understood to have the same meaning as “and/or” as defined above. For example, when separating items in a list, “or” or “and/or” shall be interpreted as being inclusive, i.e., the inclusion of at least one, but also including more than one, of a number or list of elements, and, optionally, additional unlisted items. Only terms clearly indicated to the contrary, such as “only one of” or “exactly one of,” or, when used in the claims, “consisting of,” will refer to the inclusion of exactly one element of a number or list of elements. In general, the term “or” as used herein shall only be interpreted as indicating exclusive alternatives (i.e. “one or the other but not both”) when preceded by terms of exclusivity, such as “either,” “one of,” “only one of,” or “exactly one of.” “Consisting essentially of,” when used in the claims, shall have its ordinary meaning as used in the field of patent law.
As used herein in the specification and in the claims, the phrase “at least one,” in reference to a list of one or more elements, should be understood to mean at least one element selected from any one or more of the elements in the list of elements, but not necessarily including at least one of each and every element specifically listed within the list of elements and not excluding any combinations of elements in the list of elements. This definition also allows that elements may optionally be present other than the elements specifically identified within the list of elements to which the phrase “at least one” refers, whether related or unrelated to those elements specifically identified. Thus, as a non-limiting example, “at least one of A and B” (or, equivalently, “at least one of A or B,” or, equivalently “at least one of A and/or B”) can refer, in one embodiment, to at least one, optionally including more than one, A, with no B present (and optionally including elements other than B); in another embodiment, to at least one, optionally including more than one, B, with no A present (and optionally including elements other than A); in yet another embodiment, to at least one, optionally including more than one, A, and at least one, optionally including more than one, B (and optionally including other elements); etc.
In the claims, as well as in the specification above, all transitional phrases such as “comprising,” “including,” “carrying,” “having,” “containing,” “involving,” “holding,” and the like are to be understood to be open-ended, i.e., to mean including but not limited to. Only the transitional phrases “consisting of” and “consisting essentially of” shall be closed or semi-closed transitional phrases, respectively, as set forth in the United States Patent Office Manual of Patent Examining Procedures, Section 2111.0
This application claims priority under 35 U.S.C. § 119(e) to U.S. Provisional Patent Application No. 63/223,663, filed Jul. 20, 2021, and entitled, “Battery Pack and Related Components and Methods,” and to U.S. Provisional Patent Application No. 63/166,549, filed Mar. 26, 2021, and entitled, “Battery Pack and Related Components and Methods,” each of which is incorporated herein by reference in its entirety for all purposes.
Number | Date | Country | |
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63223663 | Jul 2021 | US | |
63166549 | Mar 2021 | US |