An electrochemical cell includes a permeable fuel electrode configured to support a metal fuel thereon, and an oxidant reduction electrode spaced from the fuel electrode. An ionically conductive medium is provided for conducting ions between the fuel and oxidant reduction electrodes, to support electrochemical reactions at the fuel and oxidant reduction electrodes. A charging electrode is also included, selected from the group consisting of (a) the oxidant reduction electrode, (b) a separate charging electrode spaced from the fuel and oxidant reduction electrodes, and (c) a portion of the permeable fuel electrode. The charging electrode is configured to evolve gaseous oxygen bubbles that generate a flow of the ionically conductive medium. One or more flow diverters are also provided in the electrochemical cell, and configured to direct the flow of the ionically conductive medium at least partially through the permeable fuel electrode.

The invention relates to a battery comprising liquid electrolyte, used in moving vehicles, wherein the battery includes a battery housing comprising side walls, a housing floor and a cover, a liquid electrolyte, the level of which is within predetermined tolerance limits, electrodes, a flow channel plate arranged at least on one side wall so as to form a flow channel, wherein the upper end of said flow channel serves as exhaust port, a mixing vessel comprising a mixing vessel floor and mixing vessel side walls being arranged above the electrodes wherein the mixing vessel side wall adjoining the exhaust port is formed as an overflow the mixing vessel floor being located below the minimum level for the liquid electrolyte, which minimum level is provided for operational reasons, and at least one floor opening being provided in the mixing vessel floor.

A zinc-air cell, a battery which is a low weight, low volume, or higher energy system, or a combination thereof and an apparatus for recharging the same are disclosed.

High performance flow batteries, based on alkaline zinc/ferro-ferricyanide rechargeable (ZnFe) and similar flow batteries, may include one or more of the following improvements. First, the battery design has a cell stack comprising a low resistance positive electrode in at least one positive half cell and a low resistance negative electrode in at least one negative half cell, where the positive electrode and negative electrode resistances are selected for uniform high current density across a region of the cell stack. Second, a flow of electrolyte, such as zinc species in the ZnFe battery, with a high level of mixing through at least one negative half cell in a Zn deposition region proximate a deposition surface where the electrolyte close to the deposition surface has sufficiently high zinc concentration for deposition rates on the deposition surface that sustain the uniform high current density.

Provided is a rechargeable electrochemical cell system for generating electrical current using a fuel and an oxidant. The system includes a plurality of electrochemical cells. A controller is configured to apply an electrical current between charging electrode(s) and a fuel electrode with the charging electrode(s) functioning as an anode and the fuel electrode functioning as a cathode, such that reducible metal fuel ions in the ionically conductive medium are reduced and electrodeposited as metal fuel in oxidizable form on the fuel electrode. The controller may selectively apply current to a charging electrode and third electrode between fuel electrodes of separate cells to increase uniformity of the metal fuel being electrodeposited on the fuel electrode. The controller controls a number of switches to apply current to the electrodes and select different modes for the system. Also provided are methods for charging and discharging an electrochemical cell system, and selecting different modes.

A microfluidic fuel cell with flow-through architecture is provided. The anode and the cathode are porous electrodes and comprise an interstitial pore network. A virtual insulator is located between the electrodes, in an electrolyte channel. The virtual insulator is comprised of a co-laminar flow of an electrolyte. An inlet directs substantially all the flow of liquid reactant through the porous electrode.

A frame body for a cell frame of a redox flow battery, the frame body including an outer peripheral portion, the outer peripheral portion including a thin region whose thickness gradually decreases in a direction from the center of the frame body toward the outer periphery of the frame body.

A frame body that is a part of a flat cell frame for a cell stack of a redox flow battery, and that supports, on an outer peripheral side of a bipolar plate of the cell frame, the bipolar plate,

the frame body including a frame-facing surface that is to face, when a plurality of the cell frames are stacked, a frame body of another cell frame that is adjacent to the cell frame in a stacking direction, wherein the frame-facing surface has a surface roughness Ra of 0.03 m or more and 3.2 m or less.

The present disclosure relates to lead-acid batteries and the manufacture of lead-acid batteries containing acid pump devices to promote the circulation of electrolyte within the battery and/or battery cells to reduce acid stratification and improve battery performance. In various embodiments, battery cell components are assembled within an acid pump assembly that encloses the battery cell components on at least the bottom and ends. In various embodiments, at least a portion of the acid pumps may be integrally molded with or secured to various parts of the battery housing including the cover, side walls, and cell walls. In various embodiments; space for the acid pumps is created by varying the shape of the battery housing (e.g., the side walls or cell walls) and/or by modifying the shape, size, and or position of one or more of the battery electrodes or separators.

An electrolyte-circulating battery in which the electrolyte temperature is easily controlled is provided. An electrolyte-circulating battery includes a battery cell and a circulation channel that circulates an electrolyte to the battery cell. The electrolyte-circulating battery comprises a heat exchanger installed in the circulation channel and configured to cool the electrolyte; a bypass flow channel that connects an electrolyte inflow side and an electrolyte outflow side of the heat exchanger to each other so as to bypass the heat exchanger; and a flow rate variable mechanism capable of varying a flow rate of the electrolyte flowing through the heat exchanger and a flow rate of the electrolyte flowing through the bypass flow channel.