An ion exchange membrane separated two electrode flow analyzer for continuous aqueous electrochemical heavy metal detection is disclosed. The electrochemical cell includes a gas diffusion counter/reference electrode, a flooded flow through working electrode, and an ion exchange membrane that separates the gas diffusion counter/reference electrode and the flooded flow through working electrode. A method of continuous fluid analysis using a multi-electrode flow analyzer is also disclosed, including passing an aqueous sample through a first inlet flow area and into a working electrode of a multi-electrode flow analyzer, passing a gas mixture through a second inlet flow area and into a counter/reference electrode of the multi-electrode flow analyzer, depositing an analyte onto a surface of the working electrode, stripping the analyte from the surface of the working electrode by sweeping a range of a potential applied to the surface of the working electrode.

An electrochemical cell comprises a first electrode, a second electrode, and a proton-conducting membrane between the first electrode and the second electrode. The first electrode comprises a layered perovskite having the general formula: DAB.sub.2O.sub.5+δ, wherein D consists of two or more lanthanide elements; A consists of one or more of Sr and Ba; B consists of one or more of Co, Fe, Ni, Cu, Zn, Mn, Cr, and Nd; and δ is an oxygen deficit. The second electrode comprises a cermet material including at least one metal and at least one perovskite. Related structures, apparatuses, systems, and methods are also described.

An electrochemical cell comprises a first electrode, a second electrode, and a proton-conducting membrane between the first electrode and the second electrode. The first electrode comprises a layered perovskite having the general formula: DAB.sub.2O.sub.5+δ, wherein D consists of two or more lanthanide elements; A consists of one or more of Sr and Ba; B consists of one or more of Co, Fe, Ni, Cu, Zn, Mn, Cr, and Nd; and δ is an oxygen deficit. The second electrode comprises a cermet material including at least one metal and at least one perovskite. Related structures, apparatuses, systems, and methods are also described.

The chamber frame element of the present invention, which has a smaller amount of voltage drop, consumes less reactive power than the prior art, and exhibits no metal corrosion, is a chamber frame element (14) for an electrolyzer or an electrodialysis cell. The chamber frame element (14) includes: a bag body (141); a frame (142) housed in an interior space of the bag body (141); and an inlet (143) and an outlet (144) to which piping can be attached, which are formed on the outer side of a region where the frame is housed in the bag body (141).

The chamber frame element of the present invention, which has a smaller amount of voltage drop, consumes less reactive power than the prior art, and exhibits no metal corrosion, is a chamber frame element (14) for an electrolyzer or an electrodialysis cell. The chamber frame element (14) includes: a bag body (141); a frame (142) housed in an interior space of the bag body (141); and an inlet (143) and an outlet (144) to which piping can be attached, which are formed on the outer side of a region where the frame is housed in the bag body (141).

Provided are methods of making aliphatic or aromatic compounds (e.g., small molecules or polymers) having one or more amine groups and/or imine groups. A method of the present disclosure is an electrohydrogenation method, where a potential is applied to an aliphatic or aromatic compound (e.g., small molecule or polymer) having one or more nitrile groups, where after the potential is applied one or more of the nitrile groups are reduced to an amine or imine. The electrohydrogenation may be carried out using non-pulsed or pulsed potential waveforms.

Provided are methods of making aliphatic or aromatic compounds (e.g., small molecules or polymers) having one or more amine groups and/or imine groups. A method of the present disclosure is an electrohydrogenation method, where a potential is applied to an aliphatic or aromatic compound (e.g., small molecule or polymer) having one or more nitrile groups, where after the potential is applied one or more of the nitrile groups are reduced to an amine or imine. The electrohydrogenation may be carried out using non-pulsed or pulsed potential waveforms.

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.

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.

A bipolar plate for an electrochemical reactor, including at least one anode sheet and one cathode sheet, each having an internal face and an external face, the anode and cathode sheets being in contact with each other via their internal face, each anode and cathode sheet including, on its external face, channels for circulating reactive fluids, the channels demarcating, at the internal faces of the anode and cathode sheets, cooling pipes for a flow of a heat transfer fluid, the channels of the anode and cathode sheets including alternating bosses and indentations, the bosses of the anode sheet being arranged in a staggered manner and the bosses of the cathode sheet being arranged in a staggered manner.