Patent classifications
B01J23/468
CONVERSION OF ETHANE TO ETHYLENE
Methods of converting ethane to ethylene at relatively low temperatures are described. Ir02-based catalysts are used in the conversion. Methods of converting a base gas to a first gas by exposing the base gas to an IrO2-based catalyst and forming the first gas are described. The base gas can be an alkane. The first gas can include an alkene, an alkyne, an alcohol, an aldehyde, or combinations thereof.
Supported bimetallic core-shell structure catalyst and its preparation method
The purpose of the invention is to provide a supported bimetallic core-shell structure catalyst and its preparation method. Supporter, metal salt and reducing agent solution are mixed to synthesize the catalyst M@PdM/ZT by using a one-step synthesis method, wherein the active metal particle M@PdM as core-shell structure, M Is the core representing one of the Ag, Pt, Au and Ir. ZT is the supporter, representing one of hydrotalcite (Mg.sub.2Al-LDH), alumina (Al.sub.2O.sub.3) and silica (SiO.sub.2). By changing the temperature and the reaction time to control the kinetic behavior of the reduction of two kinds of metal ions to realize the construction of core-shell structure. Active metal particle composition and shell thickness are regulated by controlling metal ion concentration. The bimetallic core-shell catalyst prepared by this method showed excellent selectivity and stability in acetylene selective hydrogenation and anthraquinone hydrogenation.
N.SUB.2.O removal from automotive exhaust for lean/rich systems
A nitrous oxide (N.sub.2O) removal catalyst composition for treating an exhaust stream of an internal combustion engine is provided, containing a platinum group metal (PGM) component on a metal oxide-based support, wherein the N.sub.2O removal catalyst composition is in a substantially reduced form, such that it has an oxygen deficiency of about 0.05 mmol oxygen atoms/g or greater, and wherein the N.sub.2O removal catalyst composition provides effective removal of at least a portion of N.sub.2O from the exhaust stream under lean conditions at a temperature of about 350 C. or lower. N.sub.2O removal catalytic articles, systems, and methods are also provided for removing at least a portion of N.sub.2O from an exhaust stream under lean, low temperature conditions.
SUPPORTED BIMETALLIC CORE-SHELL STRUCTURE CATALYST AND ITS PREPARATION METHOD
The purpose of the invention is to provide a supported bimetallic core-shell structure catalyst and its preparation method. Supporter, metal salt and reducing agent solution are mixed to synthesize the catalyst M@PdM/ZT by using a one-step synthesis method, wherein the active metal particle M@PdM as core-shell structure, M Is the core representing one of the Ag, Pt, Au and Ir. ZT is the supporter, representing one of hydrotalcite (Mg.sub.2Al-LDH), alumina (Al.sub.2O.sub.3) and silica (SiO.sub.2). By changing the temperature and the reaction time to control the kinetic behavior of the reduction of two kinds of metal ions to realize the construction of core-shell structure. Active metal particle composition and shell thickness are regulated by controlling metal ion concentration. The bimetallic core-shell catalyst prepared by this method showed excellent selectivity and stability in acetylene selective hydrogenation and anthraquinone hydrogenation.
HIGHLY DISPERSED ULTRA-SMALL SIZE CARBON-SUPPORTED NOBLE METAL CATALYST AND PREPARATION METHOD THEREOF
The invention provides a highly dispersed ultra-small size carbon-supported noble metal catalyst and a preparation method thereof. The preparation method comprises: Step S1, mixing a carbon material with a hydrogenated borophene dispersion, wherein in a mixed solution, a mass ratio of the carbon material to the hydrogenated borophene is 1:0.01-1, and then dispersing the activated carbon in the mixed solution sufficiently and uniformly to obtain a uniform carbon material-supported hydrogenated borophene dispersion; Step S2, adding an aqueous solution of a noble metal precursor to the uniform carbon material-supported hydrogenated borophene dispersion according to a mass ratio of the carbon material to the noble metal of 1:0.001-0.5, and fully stirring to obtain a suspension; and Step S3, filtering the suspension, and after treatment, to obtain the highly dispersed ultra-small size carbon-supported noble metal catalyst.
Immiscible composite catalyst for synthesis of hydrogen peroxide and methods for synthesizing of hydrogen peroxide using the same
A catalyst for synthesizing hydrogen peroxide is provided. The catalyst includes first material capable of dissociating hydrogen molecules; and second material capable of suppressing dissociation of oxygen molecules, where one or more interfaces are formed between the first material and the second material. The catalyst can be used as an alternative to the expensive palladium catalysts. In particular, the catalyst can be used for the direct synthesis of hydrogen peroxide.
METHOD FOR THE SYNTHESIS AND ISOLATION OF FACIAL-TRIS-HOMOLEPTIC PHENYLPYRIDINATO IRIDIUM (III) PHOTOCATALYSTS
Methods of synthesizing and isolating facial-tris-homoleptic phenylpyridinato iridium (III) photocatalysts are disclosed. Also disclosed are methods of recovering excess 2-phenylpyridine ligands from said syntheses.
BIPOLAR MEMBRANES
A bipolar membrane comprising a first member comprising at least one anion exchange material; a second member comprising at least one cation exchange material, wherein the first member and the second member together form an interface junction; and disposed within the interface junction a first layer comprising a first water dissociation catalyst and a second layer comprising a second water dissociation catalyst, wherein the first water dissociation catalyst is different than the second water dissociation catalyst.
HYDROPROCESSING CATALYST FOR THE REDUCTION OF METALS AND SULFUR IN HEAVY FEEDS
A catalyst comprising a carrier and a metals component impregnated in the carrier, the carrier comprising alumina; and the metals component comprising a first metals fraction and a second metals fraction, the first metals fraction comprising at least one metal selected from chromium, molybdenum, or tungsten, and the second metals fraction comprising at least two metals selected from cobalt, rhodium, iridium, nickel, palladium, or platinum, wherein the catalyst has a first pore volume of 0.28 to 0.45 mL/g for pores having a pore diameter of 12 nm to less than 16 nm, and a second pore volume of 0.15 to 0.28 mL/g for pores of 2.0 nm to less than 12.0 nm.
Catalysts and related methods for photocatalytic production of H.SUB.2.O.SUB.2 .and thermocatalytic reactant oxidation
Catalysts, catalytic systems and related synthetic methods for in situ production of H.sub.2O.sub.2 and use thereof in reaction with oxidizable substrates.