Robert Boschgmbh

Nathan P Craig

Soo Kim

Jonathan Mailoa

Mordechai C Kornbluth

Georgy Samsonidze

Boris Kozinsky

Sondra L Hellstrom

Saravanan Kuppan

Lei Cheng

Michael Metzger

Jake Christensen

Christina Johnston

John F Christensen

Charles D Tuffile

Karim Gadelrab

Yelena Gorlin

Katherine Harry

Daniil A Kitchaev

Ulrich Berner

Jonathan Braaten

Dawei Zhang

Hany Basam Eitouni

Nikhil Ravi

Christopher Johnson

Nadezda Fomina

Young Shik Shin

Anika Marusczyk

Timothy Schultz

Abdul-Kader Srouji

Friedrich Muehleder

Matthias Kuntz

Matthias Martin Hanauer

Uma Krishnamoorthy

Cheol Woo Park

Morteza Rezaei Talarposhti

Kuppan Saravanan

Ramachandran Subbaraman

Kevin Gregory Gallagher

Giovanna Bucci

An electrochemical cell catalyst state of health monitoring device. The device includes a first magnetic device adjacent a first side of a first catalyst material associated with a first electrode. The device further includes a second magnetic device adjacent a second side of the first catalyst material. The first or second magnetic device is configured to generate a magnetic field. The other of the first and second magnetic devices is configured to receive a magnetic response from the first catalyst material. The device also includes a controller configured to receive the magnetic response and to determine magnetic response data of the first catalyst material in response to the magnetic response. The magnetic response data is indicative of a state of health.

Electrochemical cell catalyst state of health monitoring device

A computational method for determining a location and an amount of a transition metal M in surface facets of a Pt—M alloy using a density functional theory includes receiving a particle size and a surface facet distribution of the Pt—M alloy and a total concentration of M in the Pt—M alloy; calculating a total number of M atoms in the Pt—M alloy based on the particle size and the surface facet distribution of the Pt—M alloy and the total concentration of M in the Pt—M alloy; and predicting a mixing energy between Pt and at least one of the total number of M atoms in a subsurface layer of each of the surface facets of the Pt—M alloy when Pt is mixed with the at least one of the total number of M atoms.

Platinum-based alloy catalyst materials and computational methods relating thereto

An electrochemical cell (e.g., a fuel cell) includes an anode layer, a cathode layer, and an electrolyte membrane layer disposed between and spacing apart the anode layer and the cathode layer. The electrochemical cell further includes a functional layer disposed at an interface between the cathode layer and the electrode membrane layer. The functional layer includes a composition including a carbon material, an ionomer material, and optionally an amount of catalyst material.

Electrochemical cell with bilayer electrocatalyst structure

A desalination battery includes a working intercalation electrode in a first compartment, a counter intercalation electrode in a second compartment, both compartments including saline water solution with an elevated concentration of dissolved salts, an ion exchange membrane arranged between the compartments, a voltage source arranged to supply voltage to the electrodes, and a sacrificial compound configured to neutralize charge within the first compartment at a predetermined voltage while being consumed by oxidation or reduction reactions upon an activation of the working electrode.

Desalination device electrode activation

An electrode configuration for a battery cell includes a positive electrode, a negative electrode, and a separator interposed between the positive electrode and the negative electrode. The separator includes an electrically conductive protrusion inhibiting layer and a first insulating layer interposed between and electrically insulating the protrusion inhibiting layer from one of the positive and negative electrode.

Electrode configuration with a protrusion inhibiting separator

An electrostatic charging air cleaning device. The device includes a pre-charger configured to generate a corona discharge to electrostatically charge particulate matter in an air stream. The device further includes a separator downstream from the pre-charger configured to convey the electrostatically charged particulate matter and formed of an insulative material. The device also includes a collection electrode configured to receive and to absorb the conveyed electrostatically charged particulate matter. The collection electrode includes a substrate material and a coating layer coated onto the substrate material. The coating layer includes a carbon black material and a polymeric binder. The substrate material is a metal plate including mechanical perforations.

Electrostatic charging air cleaning device and collection electrode

Fuel cell alloy bipolar plates. The alloys may be used as a coating or bulk material. The alloys and metallic glasses may be particularly suitable for proton-exchange membrane fuel cells because of they may exhibit reduced weights and/or better corrosion resistance. The alloys may include any of the following AlCuTi, AlFeNi, AlMnNi, AlNiTi, CuFeTi, CuNiTi, AlFeSi, AlMnSi, AlNiSi, NiSiTi, and CFeSi. The alloys or metallic glass may be doped with various dopants to improve glass forming ability, mechanical strength, ductility, electrical or thermal conductivities, hydrophobicity, and/or corrosion resistance.

Fuel cell bipolar plate alloys

A fuel cell stack includes a first end region, a second end region, and a middle region. At least one of a first number of fuel cell units in the first end region is a first fuel cell unit including a membrane electrode assembly (MEA) with a first catalyst material on either or both an anode and a cathode of the first fuel cell unit. At least one of a second number of fuel cell units in the second end region is a second fuel cell unit including an MEA with a second catalyst material on either or both an anode and a cathode of the first fuel cell unit. The middle region is situated between the first and the second end region. At least one of a third number of fuel cell units in the middle region is a third fuel cell unit including an MEA with a third catalyst material on either or both an anode and a cathode of the first fuel cell unit. At least one of the first, the second, and the third catalyst material are different.

Catalyst materials for a fuel cell stack

A device for removing chloride-containing salts from water includes a container configured to contain saline water, a first electrode arranged in fluid communication with the saline water, and a power source. The first electrode includes a conversion material that is substantially insoluble in the saline water and has a composition that includes at least two or more of aluminum, chlorine, copper, iron, oxygen, and potassium. The composition varies over a range with respect to a quantity of chloride ions per formula unit. The power source supplies current to the first electrode in a first operating state so as to induce a reversible conversion reaction in which the conversion material bonds to the chloride ions in the saline water to generate a treated water solution. The conversion material dissociates the chloride ions therefrom into the saline water solution in a second operating state to generate a wastewater solution.

Conversion materials for electrochemical removal of chloride-containing salts from water

A water softening device includes a container configured to contain water, first and second electrodes arranged in fluid communication with the water, and a power source. The first electrode includes a conversion material that has a first composition and a second composition coexisting with the first composition. The first composition includes calcium ions bonded thereto and the second composition includes sodium ions bonded thereto. The power source supplies current in a first operating state such that the second composition exchanges sodium ions for calcium ions in the water to generate a soft water solution. The first and second electrodes are connected in a second operating state such that the first composition exchanges calcium ions for sodium ions in the water to generate a wastewater solution. The conversion material undergoes a reversible conversion reaction to convert between the first and second compositions within the water stability window.

Conversion materials for electrochemical water softening

A desalination battery includes a first electrode, a second electrode, an intercalation compound contained in the first electrode, a container configured to contain a saline water solution, and a power source. The intercalation compound includes at least one of a metal oxide, a metalloid oxide, a metal oxychloride, a metalloid oxychloride, and a hydrate thereof with each having a ternary or higher order. The first and second electrodes are configured to be arranged in fluid communication with the saline water solution. The power source is configured to supply electric current to the first and second electrodes in different operating states to induce a reversible intercalation reaction within the intercalation compound. The intercalation compound reversibly stores and releases target anions from the saline water solution to generate a fresh water solution in one operating state and a wastewater solution in another operating state.

Anion insertion electrode materials for desalination water cleaning device

A desalination device includes a container, first and second electrodes, an anion exchange membrane (AEM), and a power source. The container contains saline water that has an elevated concentration of dissolved salts. The AEM separates the container into first and second compartments into which the first and second electrodes, respectively, are arranged. The AEM has a continuous porous structure and a plurality of negatively-charged oxygen functional groups coupled to the porous structure. The power source is configured to selectively apply a voltage to one of the first and second electrodes. The AEM has a selective permeability when the voltage is applied such that cations in the saline water solution have a first diffusion rate dtherethrough and anions in the saline water solution have a second diffusion rate dtherethrough. The first diffusion rate dis less than the second diffusion rate dand greater than or equal to zero.

Voltage-controlled anion exchange membrane enabling selective ion affinities for water desalination and device containing the same

A computational method simulating the motion of elements within a multi-element system using a graph neural network (GNN). The method includes converting a molecular dynamics snapshot of the elements into a directed graph comprised of nodes and edges. The method further includes the step of initially embedding the nodes and the edges to obtain initially embedded nodes and edges. The method also includes updating the initially embedded nodes and edges by passing a first message from a first edge to a first node using a first message function and passing a second message from the first node to the first edge using a second message function to obtain updated embedded nodes and edges, and predicting a force vector for one or more elements based on the updated embedded edges and a unit vector pointing from the first node to a second node or the second node to the first node.

Graph neural network force field computational algorithms for molecular dynamics computer simulations

A catalyst support material for a proton exchange membrane fuel cell (PEMFC). The catalyst support material includes a metal material of an at least partially oxidized form of TiNbOreactive with HO, HF and/or SOto form reaction products in which the metal material of the at least partially oxidized form of TiNbOaccounts for a stable molar percentage of the reaction products.

Catalyst support materials for fuel cells

A solid state electrolyte material including a decontaminated lithium conducting ceramic oxide material including a decontaminated surface thickness. The decontaminated surface thickness is less than or equal to 5 nm. The decontaminated surface thickness may be greater than or equal to 1 nm. The decontaminated lithium conducting ceramic oxide material may be selected from the group consisting of LiLaZrO(LLZO), LiLaTaO(LLTO), LiLaCaTaO(LLCTO), LiLaANbO(A is Ca or Sr), LiAlGe(PO)(LAGP), LiAl(GeTi)(PO)(LAGTP), perovskite LiLaTiO(LLTO), LiLaZr(PO)(LLZP), LiTiAl(PO)(LTAP), LiTiAlSi(PO)(LTASP), LiTiZr(PO)(LTZP), LiNdTeSbOand mixtures thereof.

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Burlingame, CA, United States of America

Nathan P Craig