Embodiments are directed to composite membranes having a microporous polymer structure, and an ion exchange material forming a continuous ionomer phase within the composite membrane. The continuous ionomer phase refers to absence of any internal interfaces in a layer of ionomer or between any number of layers coatings of the ion exchange material provided on top of one another. The composite membrane exhibits a haze change of 0% or less after being subjected to a blister test procedure. No bubbles or blisters are formed on the composite membrane after the blister test procedure. A haze value of the composite membrane is between 5% and 95%, between 10% and 90% or between 20% and 85%. The composite membrane may have a thickness of more than 17 microns at 0% relative humidity.

The present application provides a new type of glucose fuel cell in which a layer of proton-conducting metal oxide is interposed between the anode and cathode electrodes. Such metal oxides can serve in the form of thin-layer fuel cell membrane materials for novel, all-solid state fuel cell designs.

The present application provides a new type of glucose fuel cell in which a layer of proton-conducting metal oxide is interposed between the anode and cathode electrodes. Such metal oxides can serve in the form of thin-layer fuel cell membrane materials for novel, all-solid state fuel cell designs.

A carbon foam formed of carbon fibers, where, at 90% or more of any 20 locations, the carbon fibers have a fiber diameter that is within ±20% of an average fiber diameter.

The present disclosure relates generally to a carbon-neutral process for the generation of carbon-neutral hydrogen and carbon-neutral electricity. More specifically, the present disclosure relates to compositions, methods and apparatus employing a carbon-neutral process for generating electricity employing a liquid organic hydrogen carrier (LOHC) for supplying hydrogen for generating the carbon neutral electricity. The present disclosure also relates more specifically to carbon-neutral compositions consisting of liquid organic hydrogen carriers used for supplying hydrogen to generate electricity that may be regenerated in a carbon-neutral process using an apparatus with a net zero atmospheric emission of carbon oxides.

The present disclosure relates generally to a carbon-neutral process for the generation of carbon-neutral hydrogen and carbon-neutral electricity. More specifically, the present disclosure relates to compositions, methods and apparatus employing a carbon-neutral process for generating electricity employing a liquid organic hydrogen carrier (LOHC) for supplying hydrogen for generating the carbon neutral electricity. The present disclosure also relates more specifically to carbon-neutral compositions consisting of liquid organic hydrogen carriers used for supplying hydrogen to generate electricity that may be regenerated in a carbon-neutral process using an apparatus with a net zero atmospheric emission of carbon oxides.

A zinc iodine flow battery includes a positive end plate, a positive current collector, a negative current collector, a positive electrode with a flow frame, a membrane, a negative electrode with a flow frame, a negative end plate. The negative electrolyte is circulated between the negative storage tank and the negative cavity by pump. The negative pipe is provided with a branch pipe for the positive electrolyte circulation. The porous membrane between the positive and negative electrodes can realize the conduction of supporting electrolyte and prevent the diffusion of I3− to the negative electrolyte. In a duel-flow battery system, same electrolyte serves as both the positive electrolyte and the negative electrolyte, which is a mixed aqueous solution containing iodized and zinc salt. The membrane is porous membrane does not contain ion exchange group. Both the positive and negative electrolyte are neutral solutions.

Provided is an ion-conductive solid electrolyte compound, as a crystalline oxide, including a stoichiometric formula of “A.sub.x(M.sub.2TO.sub.8).sub.y”. In the stoichiometric formula, A is a cation having an oxidation state of +1, M is a cation having an oxidation state of +4, +5, or +6, T is a cation having an oxidation state of +4, +5, or +6, and x and y are each independently a real number greater than 0, wherein x is equal to or less than 3y. The ion-conductive solid electrolyte compound has a high ionic conductivity and a low electronic conductivity.

The present invention relates to a rechargeable battery, and a rechargeable battery including: a liquid cathode portion including a sodium-containing solution and a cathode current collector impregnated in the sodium-containing solution; an anode portion including a liquid organic electrolyte, an anode current collector impregnated in the liquid organic electrolyte, and an anode active material provided in the surface of the anode current collector; and a solid electrolyte provided between the cathode portion and the anode portion can be provided.

The present invention relates to a rechargeable battery, and a rechargeable battery including: a liquid cathode portion including a sodium-containing solution and a cathode current collector impregnated in the sodium-containing solution; an anode portion including a liquid organic electrolyte, an anode current collector impregnated in the liquid organic electrolyte, and an anode active material provided in the surface of the anode current collector; and a solid electrolyte provided between the cathode portion and the anode portion can be provided.