An anode material having 0.8≤0.06×(Dv50).sup.2−2.5×Dv50+Dv99≤12 (1); and 1.2≤0.2×Dv50−0.006×(Dv50).sup.2+BET≤5 (2), where Dv50 represents a value in the volume-based particle size distribution of the anode material that is greater than the particle size of 50% of the particles, Dv99 represents a value in the volume-based particle size distribution of the anode material that is greater than the particle size of 99% of the particles, and BET is a specific surface area of the anode material, wherein Dv50 and Dv99 are expressed in μm and BET is expressed in m.sup.2/g. The anode material is capable of significantly improving the rate performance of electrochemical devices.

Energy sources embodying the invention include one or more cells, where each cell includes an electrode (anode or cathode) which is a non-metal and another electrode which is a metal or non-metal, with the electrodes positioned relative to each other to produce a potential differential. The electrodes may be placed in a water solution or kept in air (dry). They may be spaced apart or be in direct contact. A conduction enhancing layer may be placed between the electrodes.

A nanowire energy storage device such as a nanowire battery or a capacitor having a cathode comprising a plurality of nanowires and an anode comprising a plurality of nanowires interlaced with the plurality of nanowires of the cathode, and embedded in a PMMA gel electrolyte.

A method for determining an average oxidation state (AOS) of a redox flow battery system includes measuring a charge capacity for a low potential charging period starting from a discharged state of the redox flow battery system to a turning point of a charge voltage; and determining the AOS using the measured charge capacity and volumes of anolyte and catholyte of the redox flow battery system. Other methods can be used to determine the AOS for a redox flow battery system or use discharge voltage instead of charging voltage.

An anode material composition is provided for a metal-ion battery that comprises an active material coating, a current conductive current collector, and a conductive interlayer coupling the active material coating to the current collector. The active material coating may have a capacity loading of at least 2 mAh/cm.sup.2 and comprise active material particles that exhibit volume expansion in the range of about 8 vol. % to about 160 vol. % during a first charge-discharge cycle and volume expansion in the range of about 4 vol. % to about 50 vol. % during one or more subsequent charge-discharge cycles.

A tab, a preparation method thereof, and a battery including the tab are disclosed. The tab is a copper foil material, a surface of the copper foil material having a large compressive stress is an S surface, a surface having a small compressive stress is an M surface, and only the M surface is provided with an indentation or a reinforcing rib. In the preparation method of the tab of the disclosure, the S surface/M surface of the copper foil material are identified, and it is ensured that a feed direction is oriented so that the M surface faces outward (or inward), and winding/unwinding directions of each process and a mounting direction of an embossing device are reasonably fixed, so as to ensure that a tab emboss pattern of a product is pressed on the M surface of the copper foil material rather than the S surface or both surfaces.

A method including providing, on a substrate, first and second stacks for an energy storage device with a groove therebetween is provided. The first and second stacks each, respectively, include a first electrode layer on the substrate, an electrolyte layer on the first electrode layer, and a second electrode layer on the electrolyte layer. A first material is deposited within the groove and a second material is deposited over the first stack, the first material and the second stack to electrically connect the second electrode layers of the first and second stacks, via the second material. The first material prevents the second material from contacting the first electrode layer of the first and second stacks and the electrolyte layer of the first and second stacks, to electrically insulate the first electrode layer of the first and second stacks and the electrolyte layer of the first and second stacks from the second material.

A battery includes: a power generating element that includes at least one solid-state battery cell that includes a positive electrode, a solid electrolyte layer, and a negative electrode which are laminated; a first pressurizing member in contact with a first principal surface of the power generating element; a second pressurizing member in contact with a second principal surface of the power generating element, the second principal surface being opposite to the first principal surface. The first pressurizing member includes a first void. The second pressurizing member includes a second void. The insulating member includes a side surface portion that covers a side surface of the power generating element, and an extending portion that extends from the side surface portion into each of the first void and the second void.

In an embodiment an electrochemical cell includes a first electrode having a first surface area A1, a second electrode having a second surface area A2, an electrolyte arranged between the first electrode and the second electrode, wherein the electrochemical cell is configured to provide a first electrochemical half-cell reaction at the first electrode and provide a second electrochemical half-cell reaction at the second electrode, and wherein a surface area ratio A1/A2 is larger than a stoichiometric ratio of the first half-cell reaction and the second half-cell reaction.

The invention relates to a process for the production of lithium metal and lithium alloy mouldings, wherein solutions of metallic lithium in ammonia having the composition Li(NH.sub.3).sub.4+n and n=0-10 are brought into contact with metallic or electronically conductive deposition substrates and the ammonia is removed at temperatures of −100 to 100° C. by overflowing with inert gas or at pressures of 0.001 to 700 mbar, so that the remaining lithium is deposited on the deposition substrate or/and it is doped with lithium or alloyed by it.