Patent classifications
C25B1/04
Method for Electrochemical Production of a Product in a Cell Comprising a Polyelectrolyte
The invention relates to a method for electrochemical production of a product in an electrochemical cell comprising an extraction compartment. The extraction compartment comprises a liquid comprising a dissolved polyelectrolyte. The method comprises producing cations at an anode, producing anions at a cathode and transporting the ions through ion- selective membranes into the extraction compartment where the product is formed. The invention further relates to an electrochemical cell for use in the method.
AMMONIA SYNTHESIS METHODS AND SYSTEMS
Systems and methods for producing ammonia are described. In one embodiment, hydrogen, carbon dioxide, and nitrogen are dissolved in a solution. A glutamine synthetase inhibitor and autotrophic diazotroph bacteria are also placed in the solution.
AMMONIA SYNTHESIS METHODS AND SYSTEMS
Systems and methods for producing ammonia are described. In one embodiment, hydrogen, carbon dioxide, and nitrogen are dissolved in a solution. A glutamine synthetase inhibitor and autotrophic diazotroph bacteria are also placed in the solution.
SYSTEMS AND APPARATUS FOR PRODUCING ELECTROLYZED ALKALINE AND OXIDIZING WATER
The present invention relates to systems and methods for cleaning materials, such as flooring and upholstery. In some cases, the systems and methods use an electrolytic cell to electrolyze a solution comprising sodium carbonate, sodium bicarbonate, sodium acetate, sodium percarbonate, potassium carbonate, potassium bicarbonate, and/or any other suitable chemical to generate electrolyzed alkaline water and/or electrolyzed oxidizing water. In some cases, the cell comprises a recirculation loop that recirculates anolyte through an anode compartment of the cell. In some cases, the cell further comprises a senor and a processor, where the processor is configured to automatically change an operation of the cell, based on a reading from the sensor. In some cases, a fluid flows past a magnet before entering the cell.
In some additional cases, fluid from the cell is conditioned by being split into multiple conduits that run in proximity to each other. Additional implementations are described.
SYSTEMS AND APPARATUS FOR PRODUCING ELECTROLYZED ALKALINE AND OXIDIZING WATER
The present invention relates to systems and methods for cleaning materials, such as flooring and upholstery. In some cases, the systems and methods use an electrolytic cell to electrolyze a solution comprising sodium carbonate, sodium bicarbonate, sodium acetate, sodium percarbonate, potassium carbonate, potassium bicarbonate, and/or any other suitable chemical to generate electrolyzed alkaline water and/or electrolyzed oxidizing water. In some cases, the cell comprises a recirculation loop that recirculates anolyte through an anode compartment of the cell. In some cases, the cell further comprises a senor and a processor, where the processor is configured to automatically change an operation of the cell, based on a reading from the sensor. In some cases, a fluid flows past a magnet before entering the cell.
In some additional cases, fluid from the cell is conditioned by being split into multiple conduits that run in proximity to each other. Additional implementations are described.
ELECTRODE CATALYST INK OF WATER ELECTROLYSIS CELL, ELECTRODE CATALYST, WATER ELECTROLYSIS CELL, AND WATER ELECTROLYZER
The electrode catalyst ink for a water electrolysis cell includes a catalyst including a layered double hydroxide, an organic polymer, and a solvent. The Hansen solubility parameter distance R.sub.a1 between the solvent and the catalyst is 15.0 MPa.sup.½ or more and less than 20.5 MPa.sup.½. The Hansen solubility parameter distance R.sub.a2 between the solvent and the organic polymer is 10.0 MPa.sup.½ or more and 14.0 MPa.sup.½ or less.
ELECTRODE CATALYST INK OF WATER ELECTROLYSIS CELL, ELECTRODE CATALYST, WATER ELECTROLYSIS CELL, AND WATER ELECTROLYZER
The electrode catalyst ink for a water electrolysis cell includes a catalyst including a layered double hydroxide, an organic polymer, and a solvent. The Hansen solubility parameter distance R.sub.a1 between the solvent and the catalyst is 15.0 MPa.sup.½ or more and less than 20.5 MPa.sup.½. The Hansen solubility parameter distance R.sub.a2 between the solvent and the organic polymer is 10.0 MPa.sup.½ or more and 14.0 MPa.sup.½ or less.
RENEWABLE METHANOL PRODUCTION MODULE
The present invention is directed to a renewable methanol production system generally comprising: 1. a water capture module for directly capturing water from air to provide water in a liquid form; 2. an electrolysis module for electrolysis of the liquid water to produce hydrogen; 3. an exothermic reactor for reacting the hydrogen from the electrolysis module with carbon dioxide to produce renewable methanol.
RENEWABLE METHANOL PRODUCTION MODULE
The present invention is directed to a renewable methanol production system generally comprising: 1. a water capture module for directly capturing water from air to provide water in a liquid form; 2. an electrolysis module for electrolysis of the liquid water to produce hydrogen; 3. an exothermic reactor for reacting the hydrogen from the electrolysis module with carbon dioxide to produce renewable methanol.
Carbon Dioxide Gas Phase Reduction Apparatus and Method
A carbon dioxide gas phase reduction device includes an oxidation tank including an oxidation electrode, a reduction tank to which carbon dioxide is supplied, an intermediate tank that is disposed between the oxidation tank and the reduction tank and capable of pouring and discharging an electrolytic solution, an ion exchange membrane disposed between the oxidation tank and the intermediate tank, a gas reduction sheet in which an ion exchange membrane and a reduction electrode are laminated and which is disposed between the reduction tank and the intermediate tank with the ion exchange membrane facing the intermediate tank and the reduction electrode facing the reduction tank, and a conducting wire connecting the oxidation electrode to the reduction electrode.