Abstract: An electrochemical cell active hydrogen capture and release system including a first zone having a target predetermined concentration of hydrogen c1 and housing: an electrical component, an adsorbing electrode including a hydrogen adsorbing material, a counter electrode separated from the adsorbing electrode, and an electric circuit connecting the adsorbing and counter electrodes to apply electrical bias configured to facilitate capture and release of hydrogen gas from the adsorbing electrode; and a second zone having a target predetermined concentration of hydrogen c2, c2 being greater than c1.

Abstract: Microcracked and crack-free catalyst layers such as for electrodes in electrochemical cells (e.g., fuel cells) and method of making the same are disclosed. The microcracks may improve durability by better tolerating stresses without inducing or propagating into macrocracks. The microcracks also improve efficiency by providing reactant (e.g., oxygen) passages to catalyst in the catalyst layer. The microcracks may be formed in a predetermined pattern to further localize additional reactant passages is conventionally starved or more starved locations.

Abstract: An electrochemical cell active hydrogen capture and release system including a first zone having a target predetermined concentration of hydrogen c1 and housing: an electrical component, an adsorbing electrode including a hydrogen adsorbing material, a counter electrode separated from the adsorbing electrode, and an electric circuit connecting the adsorbing and counter electrodes to apply electrical bias configured to facilitate capture and release of hydrogen gas from the adsorbing electrode; and a second zone having a target predetermined concentration of hydrogen c2, c2 being greater than c1.

Abstract: A direct air capture (DAC) system includes a porous sorbent structure for CO2 capture, the structure including nanopores sized 4-10 nm forming an interpenetrating network of channels for CO2 access to an interior volume of the sorbent, macropores for CO2 diffusion within the sorbent, and nanoparticles sized about 4-10 nm and located within the network of channels.

Abstract: An electrochemical cell includes first and second electrodes. The first electrode includes first catalyst particles enhancing activity in the electrochemical cell. The second electrode including second catalyst particles enhancing activity in the electrochemical cell. One or both of the first and second catalyst particles are at least partially encapsulated in a silica encapsulation formed from a precursor of a silicon-based copolymer. The silica encapsulation sustains the activity of the first and/or second catalyst particles.

Abstract: An electrochemical system includes a hydrogen diffusion barrier physically separating the system into a hydrogen rich zone and a hydrogen poor zone, an electronic component located in the hydrogen poor zone and exposed to hydrogen diffusing from the hydrogen rich zone, a hydrogen pump, located in the hydrogen rich zone and the hydrogen poor zone, including: a cathode, an anode, an electrolyte separating the cathode and the anode, an anode encapsulation contacting the anode and a portion of the electrolyte, and an external electrical circuit biased to drive H+ current from the anode to the cathode to pump hydrogen diffusing from the hydrogen rich zone into the hydrogen poor zone back into the hydrogen rich zone.

Abstract: An electrochemical cell cathode catalyst layer includes electrocatalyst particles, an electrocatalyst support having an electronically conductive porous material including a plurality of pores with a diameter of less than or equal to 10 nm having a surface morphology comprising a plurality of peaks and valleys, the surface morphology being configured to contain the electrocatalyst particles within the plurality of pores and to enhance mass transport of molecular oxygen to the electrocatalyst particles by adsorbing molecular oxygen to the surface morphology, and an ionomer adhered to the electrocatalyst, the electrocatalyst support, or both.

Abstract: An electrochemical cell includes a membrane, a catalyzed electrode facing the membrane, the electrode including a magnetic electrocatalyst in contact with an ionomer, an electromagnet, and a controller programmed to activate the electromagnet to form an oscillating magnetic field arranged to selectively increase temperature of the magnetic electrocatalyst, based on one or more conditions, to increase kinetics of a reaction at the catalyzed electrode or remove water from the electrode.

Abstract: An atmospheric CO2 capture system includes a compartment housing a solid CO2 sorbent, an exchange fluid including a chemical component with selectivity towards CO2, and an electrochemical cell in fluid communication with the compartment, the system having a cycle including a first state of sorbing CO2 from incoming air onto the solid CO2 sorbent until a saturation point is reached; a second state of regenerating the sorbent by flooding the compartment with the exchange fluid to detach CO2 from the saturated sorbent and bind the detached CO2 to the chemical component; and a third state of regenerating the chemical component by detaching CO2 from the chemical component in the electrochemical cell and releasing the CO2 from the system.

Abstract: An atmospheric CO2 capture system includes a compartment housing a solid CO2 sorbent, an exchange fluid including a chemical component with selectivity towards CO2, and an electrochemical cell in fluid communication with the compartment, the system having a cycle including a first state of sorbing CO2 from incoming air onto the solid CO2 sorbent until a saturation point is reached; a second state of regenerating the sorbent by flooding the compartment with the exchange fluid to detach CO2 from the saturated sorbent and bind the detached CO2 to the chemical component; and a third state of regenerating the chemical component by detaching CO2 from the chemical component in the electrochemical cell and releasing the CO2 from the system.

Abstract: A device includes a tribological assembly including first and second mechanical components in relative motion with respect to each other, the assembly having a silver-alloy surface and an additive lubricant including at least one component of the formulas (Ia) or (II): MxNOy (Ia), where M is Ca, V, Sb, Ni, or Ag, x (M:N ratio) is any number between 0.25 and 2, and y (O:N ratio) is any number between 1 and 8; MxSiOy (II), where M is Mg or Al, x (M:Si ratio) is any number between 0.5 and 2, and y (O:Si ratio) is any number between 2.5 and 6, the device being a sealed constant-pressure device.

Abstract: A tribological system includes a tribological contact area including a first tribological contact surface of a first mechanical component and a second tribological contact surface of a second mechanical component, the first and second mechanical components being in relative motion with respect to each other; an external circuit connected to the first and second mechanical components and providing Joule heating; and an additive in contact with the tribological contact area, the additive having a first viscosity in a first state before the external circuit is activated, a second viscosity in a second state when the external circuit is activated to produce Joule heating, and a third viscosity in a third state when the external circuit is deactivated after activation, the second viscosity being lower than the third viscosity.

Abstract: A device includes a tribological assembly including first and second mechanical components in relative motion with respect to each other, the assembly having a silver-alloy surface and an additive lubricant including at least one component of the formulas (Ia) or (II): MxNOy (Ia), where M is Ca, V, Sb, Ni, or Ag, x (M:N ratio) is any number between 0.25 and 2, and y (O:N ratio) is any number between 1 and 8; MxSiOy (II), where M is Mg or Al, x (M:Si ratio) is any number between 0.5 and 2, and y (O:Si ratio) is any number between 2.5 and 6, the device being a sealed constant-pressure device.

Abstract: A cathode catalyst layer includes a substrate and an ionomer structured as a biphasic lamellar film in contact with the substrate, the lamellar film including a plurality of alternating layers of hydrophobic backbones and hydrophilic sidechains, the film having an outermost layer formed by the hydrophobic backbone affixed in place, the outermost layer being free of hydrophilic groups and forming a hydrophobic surface throughout the cathode catalyst layer.

Abstract: An electrochemical cell includes an anode, a cathode, and a membrane physically separating the anode from the cathode, the cathode having a cathode catalyst layer including an ionomer and an electrocatalyst support substrate forming an ionomer-support interface having a covalent bond between the substrate and the ionomer via a grafting compound, the substrate further having a plurality of terminated hydrophilic groups.

Abstract: An electrochemical cell cathode catalyst layer includes electrocatalyst particles, an electrocatalyst support having an electronically conductive porous material including a plurality of pores with a diameter of less than or equal to 10 nm having a surface morphology comprising a plurality of peaks and valleys, the surface morphology being configured to contain the electrocatalyst particles within the plurality of pores and to enhance mass transport of molecular oxygen to the electrocatalyst particles by adsorbing molecular oxygen to the surface morphology, and an ionomer adhered to the electrocatalyst, the electrocatalyst support, or both.

Abstract: Microcracked and crack-free catalyst layers such as for electrodes in electrochemical cells (e.g., fuel cells) and method of making the same are disclosed. The microcracks may improve durability by better tolerating stresses without inducing or propagating into macrocracks. The microcracks also improve efficiency by providing reactant (e.g., oxygen) passages to catalyst in the catalyst layer. The microcracks may be formed in a predetermined pattern to further localize additional reactant passages is conventionally starved or more starved locations.

Abstract: 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.

Abstract: An electrochemical cell active hydrogen capture and release system including a first zone having a target predetermined concentration of hydrogen c1 and housing: an electrical component, an adsorbing electrode including a hydrogen adsorbing material, a counter electrode separated from the adsorbing electrode, and an electric circuit connecting the adsorbing and counter electrodes to apply electrical bias configured to facilitate capture and release of hydrogen gas from the adsorbing electrode; and a second zone having a target predetermined concentration of hydrogen c2, c2 being greater than c1.

Abstract: An electrochemical system includes a hydrogen diffusion barrier physically separating the system into a hydrogen rich zone and a hydrogen poor zone, an electronic component located in the hydrogen poor zone and exposed to hydrogen diffusing from the hydrogen rich zone, a hydrogen pump, located in the hydrogen rich zone and the hydrogen poor zone, including: a cathode, an anode, an electrolyte separating the cathode and the anode, an anode encapsulation contacting the anode and a portion of the electrolyte, and an external electrical circuit biased to drive H+ current from the anode to the cathode to pump hydrogen diffusing from the hydrogen rich zone into the hydrogen poor zone back into the hydrogen rich zone.