Patent classifications
C25B9/16
Chemically modified graphene
This disclosure relates to graphene derivatives, as well as related devices including graphene derivatives and methods of using graphene derivatives.
Divided electrochemical cell and low cost high purity hydride gas production process
This invention is an apparatus and a method for continuously generating a hydride gas of M.sub.1 which is substantially free of oxygen in a divided electrochemical cell. An impermeable partition or a combination of an impermeable partition and a porous diaphragm can be used to divide the electrochemical cell. The divided electrochemical cell has an anode chamber and a cathode chamber, wherein the cathode chamber has a cathode comprising M.sub.1, the anode chamber has an anode comprising M.sub.2 and is capable of generating oxygen, an aqueous electrolyte solution comprising a hydroxide M.sub.3OH partially filling the divided electrochemical cell. Hydride gas generated in the cathode chamber and oxygen generated in the anode chamber are removed through independent outlets. M.sub.1 can be selenium, phosphorous, silicon, metal or metal alloy, M.sub.2 is metal or metal alloy suitable for anionic oxygen generation, and M.sub.3 is NH.sub.4 or an alkali or alkaline earth metal.
Aqueous solution method for manufacturing palladium doped electrode
A method for manufacturing a palladium coated doped metal oxide conducting electrode including immersing a metal oxide conducting electrode into an aqueous solution having a palladium precursor salt to form the metal oxide conducting electrode having at least one surface coated with palladium precursor. To form a layer of palladium nanoparticles on the metal oxide conducting electrode the palladium precursor on the metal oxide conducting is reduced with a borohydride compound. The palladium nanoparticles on the metal oxide conducting electrode have an average diameter of 8 nm to 22 nm and are present on the surface of the metal oxide conducting electrode at a density from 1.510.sup.3 Pd.Math.nm.sup.2 to 3.510.sup.3 Pd.Math.nm.sup.2.
Method for making a Pd-doped zinc oxide conducting electrode
A method for manufacturing a palladium coated doped metal oxide conducting electrode including immersing a metal oxide conducting electrode into an aqueous solution having a palladium precursor salt to form the metal oxide conducting electrode having at least one surface coated with palladium precursor. To form a layer of palladium nanoparticles on the metal oxide conducting electrode the palladium precursor on the metal oxide conducting is reduced with a borohydride compound. The palladium nanoparticles on the metal oxide conducting electrode have an average diameter of 8 nm to 22 nm and are present on the surface of the metal oxide conducting electrode at a density from 1.510.sup.3 Pd.Math.nm.sup.2 to 3.510.sup.3 Pd.Math.nm.sup.2.
Intermediate frame, electrochemical systems, and methods
Provided herein are intermediate frame systems and methods, comprising one or more arrays of channels on upper and/or lower edges of the intermediate frame wherein the channels are configured to provide a spatially uniform flow of electrolyte through the plane of the intermediate frame.
Alkali source and/or sink using ion-conducting solid electrolyte and mixed ion-electron conductor electrode
Some variations provide an alkali metal or alkaline earth metal atom source (e.g., vapor cell) with a solid ionic conductor and a mixed ion-electron conductor electrode. Mixed ion-electron conductor electrodes are used as efficient sources and/or as sinks for alkali metal or alkaline earth metal atoms, thus enabling electrical control over metal atom content in the vapor cell. Some variations provide a vapor-cell system comprising: a vapor-cell region configured to allow a vapor-cell optical path into a vapor-cell vapor phase; a first electrode containing an mixed ion-electron conductor that is conductive for an ion of at least one element selected from Rb, Cs, Na, K, or Sr; a second electrode electrically isolated from the first electrode; and an ion-conducting layer between the first electrode and the second electrode. The ion-conducting layer is ionically conductive for at least one ionic species selected from Rb.sup.+, Cs.sup.+, Na.sup.+, K.sup.+, or Sr.sup.2+.
Disposable wipes with treatment agent safely formed insitu
A wipe that can be used deodorize, disinfect, and/or sterilize an object. A wipe manipulator may be used with a wipe to create, energize, or enhance one or more treatment agent in a wipe to improve its efficacy. Desirably, a wipe manipulator is flexible to accommodate to curved surfaces. A wipe includes a flexible membrane or cloth-like element that may apply, distribute, and/or remove a treatment agent to, over, or from a surface of the object. An enhanced treatment agent, such as peracetic acid, may be applied to the surface subsequent to being formed in the wipe as a result of installation of the wipe onto a manipulator, or otherwise activating the wipe. A wipe manipulator may include one or more rechargeable reservoir to contain and apply a synergistic treatment agent to the wipe to create the enhanced treatment agent.
GRAPHENE AND THE PRODUCTION OF GRAPHENE
Compositions comprising hydrogenated and dehydrogenated graphite comprising a plurality of flakes. At least one flake in ten has a size in excess of ten square micrometers. For example, the flakes can have an average thickness of 10 atomic layers or less.
Electrolyzer
Provided are an electrolyzer having excellent durability against reverse current. The electrolyzer 300 includes an anode 314, an anode chamber 310 housing the anode 314, a cathode 330, a cathode chamber 320 housing the cathode 330, and a diaphragm that separates the anode chamber 310 and the cathode chamber 320, wherein a reverse current absorption body 334 formed of a sintered compact containing nickel is disposed in at least one of an inside of the cathode chamber 320 and an inside of the anode chamber 310, and the reverse current absorption body 334 is not directly coupled to the cathode 330 and the anode 314 but is electrically connected to at least one of the cathode 330 and the anode 314.
Graphene and the production of graphene
Compositions comprising hydrogenated and dehydrogenated graphite comprising a plurality of flakes. At least one flake in ten has a size in excess of ten square micrometers. For example, the flakes can have an average thickness of 10 atomic layers or less.