B01J23/63

Exhaust gas-purifying three-way catalyst and method for producing same, and integral structure type exhaust gas-purifying catalyst

Provided is, for example, an exhaust gas-purifying three-way catalyst which is suppressed in particle growth due to sintering of a catalytically active component on a carrier in exposure to a high temperature and thus is enhanced in purification performance, and a method for producing the same, as well as an integral structure type exhaust gas-purifying catalyst using the same. The exhaust gas-purifying three-way catalyst of the present invention includes a composite particle which contains a base material particle having a pore size of 100 to 650 nm as measured by a mercury intrusion method and a catalytically active particle of a platinum group element supported on the base material particle, in which a content proportion of the catalytically active particle is 0.001 to 30% by mass in total in terms of metal of the platinum group element, based on a total amount of the composite particle.

DEHYDROGENATION CATALYST SYSTEMS AND METHODS FOR USING THEM
20230090285 · 2023-03-23 ·

The present disclosure relates to mixed-bed systems comprising a particulate dehydrogenation catalyst based on one or more certain group 13 and 14 elements that further include additional metal components and a particulate non-catalytic additive comprising a heat-generating material, and to methods for dehydrogenating hydrocarbons using such systems. One aspect of the disclosure provides a mixed-bed system comprising a particulate dehydrogenation catalyst and a particulate non-catalytic additive. The particulate dehydrogenation catalyst includes a primary species P1 selected from Ga, In, TI, Ge, Sn Pb, and any mixture thereof; a primary species P2 selected from the lanthanides and any mixture thereof; a promoter M1 selected from Ni, Pd, Pt, La, Ir, Zn, Fe, Rh, Ru, Mn, Co, W, and any mixture thereof; and a promoter M2 selected from Li, Na, K, Rb, Cs, Be, Mg, Ca, Sr, Ba, and any mixture thereof on a support S1 selected from silica, alumina, zirconia, titania, yttria, and any mixture thereof. The particulate non-catalytic additive includes a heat-generating material and a carrier selected from inorganic oxides, clays, and any mixture thereof.

DEHYDROGENATION CATALYST SYSTEMS AND METHODS FOR USING THEM
20230090285 · 2023-03-23 ·

The present disclosure relates to mixed-bed systems comprising a particulate dehydrogenation catalyst based on one or more certain group 13 and 14 elements that further include additional metal components and a particulate non-catalytic additive comprising a heat-generating material, and to methods for dehydrogenating hydrocarbons using such systems. One aspect of the disclosure provides a mixed-bed system comprising a particulate dehydrogenation catalyst and a particulate non-catalytic additive. The particulate dehydrogenation catalyst includes a primary species P1 selected from Ga, In, TI, Ge, Sn Pb, and any mixture thereof; a primary species P2 selected from the lanthanides and any mixture thereof; a promoter M1 selected from Ni, Pd, Pt, La, Ir, Zn, Fe, Rh, Ru, Mn, Co, W, and any mixture thereof; and a promoter M2 selected from Li, Na, K, Rb, Cs, Be, Mg, Ca, Sr, Ba, and any mixture thereof on a support S1 selected from silica, alumina, zirconia, titania, yttria, and any mixture thereof. The particulate non-catalytic additive includes a heat-generating material and a carrier selected from inorganic oxides, clays, and any mixture thereof.

DEFECT ENGINEERING AND MODIFICATION OF SUBSTRATES FOR SUPPORTED METAL/METAL OXIDE CATALYSTS
20220347668 · 2022-11-03 ·

Methods for fabricating thermally stable reducible metal oxide catalyst support structures on a base material using a multi-step incipient wetness impregnation (IWI) process are disclosed. For example, reducible metal oxide catalyst support structures having high surface area and high thermal stability may be formed using a multi-step IWI process, where the support structure is generated through high-temperature calcination between IWI steps. The metal or metal oxide catalysts fabricated using the methods are also disclosed. The generation of engineered surface defects on reducible metal oxides using a gas reduction process to serve as anchoring sites for metal or metal oxide catalysts is also disclosed. Generating engineered defects through a gas reduction process may be a relatively low-cost and scalable process suitable for fabricating efficient catalysts using a wide range of materials.

Device and method for recovering by-product oxygen of hydrogen production from electrolyzed water by low-temperature method

A device and a method for recovering by-product oxygen from water-electrolysis hydrogen production using a low-temperature method are provided, solving the waste problem of by-product oxygen in the green water-electrolysis hydrogen production system. The device according to the present disclosure comprises an oxygen clarifying system, a pressurizing and heat exchanging system, and a circulating gas compression and expansion refrigeration system. The recovering method according to the present disclosure comprises the following steps: first clarifying and purifying the by-product oxygen from water-electrolysis hydrogen production is to remove hydrogen, carbon monoxide, carbon dioxide, water and other impurities in the oxygen; and then, liquefying, pressurizing and heat exchanging the pure oxygen to obtain the product oxygen and liquid oxygen with required pressure. In the whole process, the cooling capacity is provided by the circulating gas expansion refrigeration system.

Device and method for recovering by-product oxygen of hydrogen production from electrolyzed water by low-temperature method

A device and a method for recovering by-product oxygen from water-electrolysis hydrogen production using a low-temperature method are provided, solving the waste problem of by-product oxygen in the green water-electrolysis hydrogen production system. The device according to the present disclosure comprises an oxygen clarifying system, a pressurizing and heat exchanging system, and a circulating gas compression and expansion refrigeration system. The recovering method according to the present disclosure comprises the following steps: first clarifying and purifying the by-product oxygen from water-electrolysis hydrogen production is to remove hydrogen, carbon monoxide, carbon dioxide, water and other impurities in the oxygen; and then, liquefying, pressurizing and heat exchanging the pure oxygen to obtain the product oxygen and liquid oxygen with required pressure. In the whole process, the cooling capacity is provided by the circulating gas expansion refrigeration system.

METHODS FOR EXHAUST GAS PURIFICATION

Methods for exhaust gas purification, including the steps of: attaching an exhaust gas purification catalyst to an exhaust system of an internal combustion engine, and supplying an exhaust gas to the exhaust gas purification catalyst, where the exhaust gas purification catalyst includes an upper layer containing first carrier particles which are particles of an inorganic oxide and rhodium, and a lower layer containing second carrier particles which are particles of an inorganic oxide, the upper layer includes a rhodium-rich portion near the surface of the upper layer on the upstream side of the exhaust gas flow, and the existence range of the rhodium-rich portion is in a range of greater than 50% to 80% of the length of the upper layer from a downstream side end of an exhaust gas flow and of less than 20 μm in the depth direction from an outermost surface of the upper layer.

METHODS FOR EXHAUST GAS PURIFICATION

Methods for exhaust gas purification, including the steps of: attaching an exhaust gas purification catalyst to an exhaust system of an internal combustion engine, and supplying an exhaust gas to the exhaust gas purification catalyst, where the exhaust gas purification catalyst includes an upper layer containing first carrier particles which are particles of an inorganic oxide and rhodium, and a lower layer containing second carrier particles which are particles of an inorganic oxide, the upper layer includes a rhodium-rich portion near the surface of the upper layer on the upstream side of the exhaust gas flow, and the existence range of the rhodium-rich portion is in a range of greater than 50% to 80% of the length of the upper layer from a downstream side end of an exhaust gas flow and of less than 20 μm in the depth direction from an outermost surface of the upper layer.

PRECIOUS METAL-SUPPORTED EGGSHELL CATALYST AS WELL AS PREPARATION METHOD AND USE THEREOF

A precious metal-supported eggshell catalyst with a preparation method and an application are provided. The precious metal-supported eggshell catalyst includes a carrier, a precious metal and a promoter. As an active component, the precious metal and the promoter are evenly distributed on surface of the carrier, wherein the promoter includes one or more than two of a precious metal, an alkaline earth metal, a transition metal lanthanide series metal, an actinium series metal and/or a metal oxide thereof. With a highly utilization of the precious metal, the precious metal-supported eggshell catalyst showed high conversion, good selectivity and excellent stability, and the precious metal-supported eggshell catalyst is used more than 300 hours with no obvious loss of activity in preparing 1,3-propanediol through hydrogenation of 3-hydroxypropionaldehyde aqueous solution. Furthermore, with large particles the precious metal-supported eggshell catalyst is easily separated from reaction products.

PRECIOUS METAL-SUPPORTED EGGSHELL CATALYST AS WELL AS PREPARATION METHOD AND USE THEREOF

A precious metal-supported eggshell catalyst with a preparation method and an application are provided. The precious metal-supported eggshell catalyst includes a carrier, a precious metal and a promoter. As an active component, the precious metal and the promoter are evenly distributed on surface of the carrier, wherein the promoter includes one or more than two of a precious metal, an alkaline earth metal, a transition metal lanthanide series metal, an actinium series metal and/or a metal oxide thereof. With a highly utilization of the precious metal, the precious metal-supported eggshell catalyst showed high conversion, good selectivity and excellent stability, and the precious metal-supported eggshell catalyst is used more than 300 hours with no obvious loss of activity in preparing 1,3-propanediol through hydrogenation of 3-hydroxypropionaldehyde aqueous solution. Furthermore, with large particles the precious metal-supported eggshell catalyst is easily separated from reaction products.