A redox flow battery system includes an anolyte; a catholyte; a first half-cell including a first electrode in contact with the anolyte; a second half-cell including a second electrode in contact with the catholyte; a separator separating the anolyte in the first half-cell from the catholyte in the second half-cell; at least one state measurement device configured for intermittently, periodically, or continuously making a measurement of a value indicative of a state of charge of the anolyte or the catholyte before entering or after leaving the first half-cell or second half-cell, respectively; and a controller coupled to the at least one state measurement device for generating a temporal energy profile of the anolyte or the catholyte, respectively, using the measurements.

Systems and methods are provided for a redox flow battery. In one example, the redox flow battery includes a bipolar plate assembly including a bipolar plate formed of a thermoplastic composite material. The thermoplastic composite material of the bipolar plate allows the bipolar plate to be directly bonded to a dielectric frame of the bipolar plate assembly, thereby simplifying a manufacturing process of the bipolar plate assembly.

A bipolar plate for an electrochemical system. The bipolar plate comprising a first individual plate and a second individual plate which are joined together. Each individual plate comprising: an electrochemically active region, an outer edge, and a perimeter sealing element. The outer edge region spans between the edge of the perimeter sealing element and the outer edge. Some emobidments of the outer edges protrude out of a plate plane defined by the bipolar plate. A plurality of stiffening structures stiffening the outer edge region of the bipolar plate.

The present disclosure provides an integrated flow battery stack with a heat exchanger for thermal control of the battery during operation. The battery can comprise a stack consisting a plurality of electrochemical cells, each cell comprising a pair of electrodes separated by a membrane and sandwiched between a pair of bipolar plates. Each bipolar plate is shared between two adjacent cells. The stack is connected to an external electrical circuit by two current collectors placed at each end of the stack. At least one current collector plate is thermally coupled to a heat exchange plate which can be configured to have its temperature varied through external means. The heat exchange plate exchanges heat with the battery stack and maintains the temperature of the stack, by implication, maintains the temperature of the circulating electrolytes.

A redox flow battery cell includes: an electrode to which an electrolyte solution is supplied; and a bipolar plate with which the electrode is arranged, wherein the bipolar plate has at least one groove portion through which the electrolyte solution flows, on a face on the electrode side, the electrode is made of a carbon fiber aggregate containing carbon fibers, and has a buried portion that is pressed toward the bipolar plate side and buried into the groove portion, and an amount of burial of the buried portion is not less than 0.2 mm and not more than 1.4 mm.

Systems and methods are provided for a redox flow battery. In one example, a method for the redox flow battery includes operating the redox flow battery in a short-term idle mode by discharging a current density as a pulse of a duration shorter than a duration of the short term idle mode. By discharging the current density, a plating surface at a negative electrode of the redox flow battery system may be maintained.

An all solid secondary battery includes an electrode assembly, and a case accommodating the electrode assembly, wherein the electrode assembly includes a unit cell portion, an anode current collector portion, and a cathode current collector portion, the case includes first and second cases insulated from each other, the anode current collector portion contacts the first case, and the cathode current collector portion contacts the second case.

One embodiment is a redox flow battery system that includes an anolyte; a catholyte; an anolyte tank configured for holding at least a portion of the anolyte; a catholyte tank configured for holding at least a portion of the catholyte; a primary redox flow battery arrangement, and a second redox flow battery arrangement. The primary and secondary redox flow battery arrangements share the anolyte and catholyte tanks and each includes a first half-cell including a first electrode in contact with the anolyte, a second half-cell including a second electrode in contact with the catholyte, a separator separating the first half-cell from the second half-cell, an anolyte pump, and a catholyte pump. The peak power delivery capacity of the secondary redox flow battery arrangement is less than the peak power delivery capacity of the primary redox flow battery arrangement.

A method and a device for producing bipolar plates for fuel cells. A bipolar plate is formed by joining an anode plate to a cathode plate, wherein the anode plate and the cathode plate are formed by forming a substrate plate. In order to provide a cost-effective and automated method, it is proposed that a plate already provided with a reactive coating or catalyst coating, which is transported, automatically driven, via a transport device from the forming device to the joining device, is used as substrate plate.

The present disclosure is directed to a single sheet electrochemical cell bipolar plate for stack assembly comprising a single sheet of formable material having an anode side and a cathode side opposite the anode side, wherein the anode side and the cathode side have a different structural configuration, a plurality of water channels on the anode side, a plurality of hydrogen channels on the cathode side, a plurality of lands comprise a groove and a flange, and a seal positioned within the flange to provide a variable groove depth for the land.