2918 results about "Flow battery" patented technology

The carbon electrode material of the present invention is used for a vanadium redox-flow cell. The carbon electrode material has quasi-graphite crystal structure in which <002> spacing obtained by X-ray wide angle analysis is 3.43 to 3.60 Å, size of a crystallite in c axial direction is 15 to 33 Å and size of crystallite in a axial direction is 30 to 70 Å. In addition, an amount of surface acidic functional groups obtained by XPS surface analysis is 0.1 to 1.2% and total number of surface bound-nitrogen atoms is 5% or smaller relative to total number of surface carbon atoms. The carbon electrode materials formed of a non-woven fabric of a carbonaceouss fiber is preferable.

A redox flow battery comprising an electrode cell including a negative electrode cell, a positive electrode cell and a separator for separating them, in which at least one of the negative electrode cell and the positive electrode cell includes a slurry type electrode solution, a porous current collector and a casing; a tank for storing the slurry type electrode solution; and a pipe for circulating the slurry type electrode solution between the tank and the electrode cell.

By realizing or installing check valve liquid vein interrupters in each compartment of the battery the phenomenon of slow discharge of the retained volumes of electrolytes during long periods of inactivity of a redox flow battery, with the electrolyte pumps stopped altogether, can be practically eliminated with the effect that the battery is perfectly ready to deliver electric power immediately upon request even after prolonged periods of inactivity. Moreover, the presence of liquid vein interrupters on each compartment in either an outlet or an inlet port substantially preventing by-pass current during a not pumping phase, permits to increase the by pumping the electrolytes through the compartments of a battery stack intermittently, in other words in a pulsed manner, with a certain duty-cycle. Relatively brief pumping phases at relatively high flow rate alternated to phases of not pumping provide for a volumetrically adequate refreshing of the electrolytes present in the battery compartments and contrast the formation of gradients in the bodies of electrolyte.

Embodiments of the invention generally provide for flow battery cells and systems containing a plurality of flow battery cells, and methods for improving metal plating within the flow battery cell, such as by flowing and exposing the catholyte to various types of cathodes. In one embodiment, a flow battery cell is provided which includes a cathodic half cell and an anodic half cell separated by an electrolyte membrane, wherein the cathodic half cell contains a plurality of cathodic wires extending perpendicular or substantially perpendicular to and within the catholyte pathway and in contact with the catholyte, and each of the cathodic wires extends parallel or substantially parallel to each other. In some examples, the plurality of cathodic wires may have at least two arrays of cathodic wires, each array contains at least one row of cathodic wires, and each row extends along the catholyte pathway.

A stack for use in a flow battery, the stack comprising an odd number of interior elements positioned between two end elements, the two end elements each including an electrode, and the odd number of interior elements including membrane elements alternating with electrode elements, wherein the membrane elements include an interior frame and a membrane, the electrode elements include the interior frame and an electrode, wherein the interior frame is rotated by 180° from the frame of the membrane elements.

A prior to charge vanadium halide redox cell, a vanadium halide redox cell which is at a state of charge selected from the group consisting of a zero state of charge and a near zero state of charge and vanadium halide redox cell which are fully charged and partially charged are described. The prior to charge vanadium halide redox cell comprises a positive half cell containing a positive half cell solution comprising a halide electrolyte, vanadium (III) halide and vanadium (IV) halide, a negative half cell containing a negative half cell solution comprising a halide electrolyte, vanadium (III) halide and vanadium (N) halide wherein the amounts of vanadium (III) halide, vanadium (IV) halide and halide ions in the positive and negative half cell solutions are such that in a first charging step comprising charging the prior to charge vanadium halide redox cell, a vanadium halide redox cell having a state of charge selected from the group consisting of a zero state of charge and a near zero state of charge comprising predominantly vanadium (N) halide in the positive half cell solution and predominantly V(III) halide in the negative half cell solution can be prepared. The vanadium halide redox cell which is at a state of charge selected from the group consisting of a zero state of charge and a near zero state of charge comprises a positive half cell containing a positive half cell solution comprising a halide electrolyte and a vanadium halide which is predominantly vanadium (N) halide, a negative half cell containing a negative half cell solution comprising a halide electrolyte and a vanadium halide which is predominantly vanadium (III) halide wherein the amount of vanadium (N) halide in the positive half cell solution and the amount of vanadium (III) halide in the negative half cell solution are such that the vanadium halide redox cell is at a state of charge selected from the group consisting of a zero state of charge and a near zero state of charge. The vanadium halide redox cell which is fully charged comprises a positive half cell containing a positive half cell solution comprising a halide electrolyte, a polyhalide complex, vanadium (IV) halide and vanadium (V) halide, a negative half cell containing a negative half cell solution comprising a halide electrolyte and vanadium (II) halide wherein the molar concentration of vanadium (V) and polyhalide complex:molar concentration of vanadium (II) halide is about stoichiometrically balanced. The vanadium halide redox cell which is partially charged comprises a positive half cell containing a positive half cell solution comprising a halide electrolyte, a polyhalide complex, vanadium (IV) halide and vanadium (V) halide, a negative half cell containing a negative half cell solution comprising a halide electrolyte, vanadium (II) halide and vanadium (III) halide wherein the number of moles of moles of polyhalide complex and vanadium (V): number of moles of vanadium (II) halide is about stoichiometrically balanced.

A flow battery includes a membrane having a thickness of less than approximately one hundred twenty five micrometers; and a solution having a reversible redox couple reactant, wherein the solution wets the membrane.

A flow battery with thermal management is presented. The flow battery is housed in an enclosure where fluid is uniformly circulated about holding tanks of electrolyte to control the temperature inside the enclosure.

The present invention provides a method of designing a redox flow battery system that can prevent system efficiency loss caused by weak generation power or load power at the time of electric charge or discharge, without using any lead storage battery, and can also provide further improved system efficiency. In the present invention, generating equipment that varies irregularly in output of power generation is provided with the redox flow battery to smooth the output of power generation. An average value of output distribution of the battery with respect to the smoothed output of power generation and standard deviation are determined. Then, at least either of a specified output of the battery and a specified output of the converter for converting the battery output is determined based on the standard deviation.

The invention relates to a water-soluble organic couple redox flow battery which comprises an anode, electrolyte thereof, a diaphragm thereof, a cathode and electrolyte thereof, wherein one of two active substances of the anode/cathode is a water-soluble organic couple, and the other one is an inorganic couple or organic couple; and the electrolyte of the anode/cathode is stored in an external storage tank, flows through the battery in a circulating way through a pump and undergoes oxidation/reduction reaction on the anode/cathode divided by the diaphragm to carry out the charging/discharging process. Organic couple materials are not limited by mining deposits, the charge capacity depends on the volume of the storage tank, the size of the battery can be singly designed according to the power requirement, and electrode potential and a reaction electron amount can be designed and controlled by organic molecules. Therefore, the redox flow battery has the advantages of rich raw materials, convenient preparation, high power conversion efficiency, environmental protection, safe use and the like and is suitable for scale electricity storage.

The invention relates to a graphite fiber felt surface modification method and a modified graphite fiber felt, and belongs to the all vanadium redox flow battery electrode manufacture technical field. The method step is that the electrochemical cathode modification treatment is conducted before the anode oxidation treatment. When used as an electrode, a modified graphite fiber felt greatly improves the electrochemical activity in the preparation of an all vanadium redox flow battery, promotes the voltage efficiency and the battery energy efficiency during the battery discharging, and increases the stable discharging time, so the recharging and discharging performance of the all vanadium redox flow battery is greatly improved. Moreover, the method is easy for implantation and low in the cost. No particular devices are required. The invention provides a good-performance electrode material for the battery manufacture field.

The invention relates to a redox flow cell containing a polyhalide/halide redox couple in the positive half-cell electrolyte and a V(III)/V(II) redox couple in the negative half-cell electrolyte. The invention also relates to a method of producing electricity by discharging the fully charged or partially charged redox flow cell, and a method of charging the discharged or partially discharged redox flow cell.

The utility model relates to a zinc-nickel sap fluid cell, which comprises a galvanic pile which is a multi-section series connection of cell monomers, electrolyte, a storage tank, a liquid pump and a plurality of pipelines; wherein, the cell monomer comprises a nickel electrode anode, a cathode current collector of deposit zinc, and electrolyte; wherein, the electrolyte is a zincous alkaline solution, and two cell monomers are connected in series via a bipolar plate. In the process of charge and discharge, the electrolyte continuously flows between the storage tank and the galvanic pile via the pipelines driven by the liquid pump. Zinc settles onto the cathode current collector and becomes a cathode active substance from the electrolyte at the time of charging, while zinc dissolves into the electrolyte from the cathode current collector at the time of discharging. The utility model has the advantages of simple fabrication technology, low cost, high cycle life and other advantages.

The invention provides an electrode for a vanadium battery, comprising a carbon basal body and a carbon nano-tube layer formed on the surface of the basal body, wherein the carbon basal body is selected from a graphite felt, a carbon felt, a carbon paper and carbon cloth. The invention also provides an all-vanadium redox flow battery containing the electrode. The electrode has improved electrochemical activity and reliable mechanical strength.

The present invention relates to a method to produce high concentration full vanadium ion oxidation and reduction liquid flow battery (vanadium battery) electrolyte, which produces 5-6mol/L vanadium battery electrolyte by proportionally adding organic-inorganic compound stabilizing agents. The present invention has the advantages of simple technical method, convenient operation and easy raw material acquisition, produces stable high-concentration vanadium battery electrolyte with excellent electrochemical reversibility and electrical conductivity approximate to conventional 2mol/L electrolyte and realizes battery charge and discharge.

The invention provides vanadium ion redox flow battery electrolyte, comprising vandic salt, sulphuric acid, additive, deionized water and metal salt can be dissolved in a sulphuric acid system. The electrolyte can greatly improve the cathode system evolution overpotential of the vanadium battery and anode system evolution overpotential, greatly reduce the ratio of gas evolution in the electrolyte caused by various polarizations in the process of operating the vanadium battery, and improve the stability of the electrolyte in the process of charge and discharge. The invention further provides a preparation method of the vanadium ion redox flow battery electrolyte, which eliminates a step of electrolyzing the obtained vanadyl sulfate solution to obtain 50% of trivalent vanadium and 50% of tetravalent vanadium, greatly simplifies the manufacture technology of the vanadium electrolyte which can be directly used for charging and discharging, reduces the lose of the vanadium in the process of preparation, and reduces the preparation cost of the electrolyte.

A method of rebalancing electrolytes in a redox flow battery system comprises directing hydrogen gas generated on the negative side of the redox flow battery system to a catalyst surface, and fluidly contacting the hydrogen gas with an electrolyte comprising a metal ion at the catalyst surface, wherein the metal ion is chemically reduced by the hydrogen gas at the catalyst surface, and a state of charge of the electrolyte and pH of the electrolyte remain substantially balanced.

The invention relates to the field of cell manufacturing and energy storage, and concretely relates to a method for preparing an electrode material for an all-vanadium flow battery. The method comprises the following steps: preparing a composite spinning liquid needed by experiments, uniformly mixing carbon nanotubes with the electrode catalysis, graphite oxide, a transition metal oxide or a transition metal nitrate or halide, and the like with the composite spinning liquid, preparing a raw electrode material through a static spinning process, preoxidizing an electrode material precursor (the raw electrode material) through utilizing a vacuum/atmosphere furnace (at 200-500DEG C), and carbonizing in an inert atmosphere (at 800-1500DEG C) to obtain the needed electrode material. The obtained electrode material can be subjected to charge and discharge tests of the cell after cleaning and drying. According to the vanadium cell electrode material prepared through adopting the method of the invention, the carbon fiber diameter is in the nanometer level, the specific surface area is substantially higher than specific surface areas of traditional used electrode materials, and the oxygen content of the fiber surface is greatly improved because of the late preoxidation processing.

An electrode structure of a vanadium redox flow battery is disclosed, which includes a proton-exchange membrane, two graphite papers, two graphite felt units, two pads, two graphite polar plates, two metal plates and a lock-fixing device which are symmetrically stacked in sequence from center to outside. wherein each graphite polar plate has the flow channels with a grooved structure, and each graphite felt unit is embedded in the flow channels of one of the graphite polar plates, and then the graphite felt units are covered by the graphite papers such that the different electrolytes flow in their corresponding flow channels. The storage tanks of vanadium electrolyte are connected through the connection pipelines, and the redox reaction is performed through the flows of the vanadium electrolyte. The electrode structure of the vanadium redox flow battery can be stacked for forming a large-scale electrode structure to increase the electrical power.