Described herein are techniques for converting carbonate in a carbonate loaded solution into syngas or C2+ products within an electrolysis cell that includes a cathodic compartment, an anodic compartment and preferably a bipolar membrane separating the compartments. The carbonate ions are converted in situ by reaction with protons generated by the bipolar membrane to produce CO.sub.2 that is in turn electrocatalytically converted into the product. The electrolysis cell can be coupled to an air or flue gas capture system that produces the carbonate loaded solution, and the depleted solution released by the electrolysis cell can be recycled back into the capture system and the feed of the electrolysis cell. The cathode can include a porous substrate that is hydrophilic, and a catalyst metal deposited on the substrate can be Cu, Ag or an alloy depending on the target product.

The present disclosure provides a high-performance electrode for water electrolysis using electrospray, a membrane electrode assembly including the same, a water electrolysis device including the electrode for water electrolysis, and a method for manufacturing the electrode for water electrolysis. The present disclosure is to provide a membrane electrode assembly (MEA) having increased porosity by using electrospray, and to apply the membrane electrode assembly to electrolysis.

The present disclosure provides a high-performance electrode for water electrolysis using electrospray, a membrane electrode assembly including the same, a water electrolysis device including the electrode for water electrolysis, and a method for manufacturing the electrode for water electrolysis. The present disclosure is to provide a membrane electrode assembly (MEA) having increased porosity by using electrospray, and to apply the membrane electrode assembly to electrolysis.

Provided are graphitic carbon materials and methods of making graphitic carbon materials. Also provided are compositions of the graphitic carbon materials with nanoparticles disposed thereon and methods of making the compositions. Also disclosed are devices utilizing the graphitic carbon materials and/or the compositions. The graphitic carbon materials are porous and have a desirable graphitic content. The graphitic materials may be nitrogen- and/or metal-doped. The nanoparticles may be platinum or platinum/transition metal nanoparticles. The compositions may be used in oxygen reduction reaction applications.

Provided are graphitic carbon materials and methods of making graphitic carbon materials. Also provided are compositions of the graphitic carbon materials with nanoparticles disposed thereon and methods of making the compositions. Also disclosed are devices utilizing the graphitic carbon materials and/or the compositions. The graphitic carbon materials are porous and have a desirable graphitic content. The graphitic materials may be nitrogen- and/or metal-doped. The nanoparticles may be platinum or platinum/transition metal nanoparticles. The compositions may be used in oxygen reduction reaction applications.

A reduction catalyst body for carbon dioxide of an embodiment includes a metal layer, and a projection provided on the metal layer. The projection is constituted of an aggregate of fine metal particles, and possesses a polyhedral structure having surfaces of three faces or more of a polygon. The projection has a site of reducing carbon dioxide, as at least a part of the surfaces.

A reduction catalyst body for carbon dioxide of an embodiment includes a metal layer, and a projection provided on the metal layer. The projection is constituted of an aggregate of fine metal particles, and possesses a polyhedral structure having surfaces of three faces or more of a polygon. The projection has a site of reducing carbon dioxide, as at least a part of the surfaces.

A water electrolyzer comprises an electrolyzer stack comprising at least two electrochemical cells. Each cell comprises an anion exchange membrane, a base metal anode electrocatalyst, a base metal cathode electrocatalyst, and a sufficiently long ion conduction path between adjacent cells such that shunt currents are less than 1% of the total current supplied to the stack.

A water electrolyzer comprises an electrolyzer stack comprising at least two electrochemical cells. Each cell comprises an anion exchange membrane, a base metal anode electrocatalyst, a base metal cathode electrocatalyst, and a sufficiently long ion conduction path between adjacent cells such that shunt currents are less than 1% of the total current supplied to the stack.

Improvements in an electrolysis electrode structure where fluid or gas enters a chamber with cathode and anode charged conductors to polarize and separate the flow into two separate paths for electrolysis of the fluid or gas. The conductors wrap around magnets to extend the range of the polarizing field beyond the range of the electrode conductors. Iron particles fan-out from the conductors and magnets to further extend the polarizing field from the magnets as well as creating increased surface area for gas or liquids to flow within and around the conductors, magnet and iron particles. Noble metal provides a thin plating that locks the position of the particles and provides an open structure to allow for the flow of gas or fluids at a high rate of flow and prevents the iron particles from being eroded by the flow.