C01B2203/1094

Catalyst composition for the production of syngas from methane, process therefore and process for CO2 reforming therewith

A catalyst for performing carbon dioxide reforming of methane to produce syngas, that includes cobalt, nickel and magnesium oxides disposed a support.

METHOD AND PLANT FOR CHEMICAL LOOPING OXIDATION-REDUCTION COMBUSTION OF A GASEOUS HYDROCARBON FEEDSTOCK WITH IN-SITU CATALYTIC REFORMING OF THE FEED

The invention relates to a method and to a plant for chemical looping oxidation-reduction combustion (CLC) of a gaseous hydrocarbon feed, for example natural gas essentially containing methane. According to the invention, catalytic reforming of the feed is performed within the reduction zone where combustion of the feed is conducted on contact with an oxidation-reduction active mass in form of particles. The reforming catalyst comes in form of untransported fluidized particles within the reduction zone. The catalyst thus confined in the reduction zone does not circulate in the CLC loop.

METHOD AND PLANT FOR CHEMICAL LOOPING OXIDATION-REDUCTION COMBUSTION OF A GASEOUS HYDROCARBON FEEDSTOCK WITH INTERMEDIATE CATALYTIC STEAM REFORMING OF THE FEED

The invention relates to a method and to a plant for chemical looping oxidation-reduction combustion (CLC) of a gaseous hydrocarbon feed, for example natural gas essentially containing methane. According to the invention, catalytic steam reforming of the feed is performed between two successive feed combustion steps on contact with an oxidation-reduction active mass in form of particles. The reforming catalyst is arranged in a fixed bed in an intermediate reforming zone (130) between the two reduction zones (120, 140) where the two combustion steps are conducted.

FIG. 2 to be published.

Base oil production via dry reforming

A system and method for converting (dry reforming) natural gas (methane) and carbon dioxide via reformer catalyst in a dry reformer into syngas including carbon monoxide and hydrogen, and discharging the syngas to a Fischer-Tropsch (FT) reactor. Supplemental hydrogen is generated via water electrolysis and added to the syngas in route to the FT reactor to increase the molar ratio of hydrogen to carbon monoxide in the syngas. The syngas may be converted via FT catalyst in the FT reactor into FT waxes.

BI-REFORMING OF HYDROCARBONS TO PRODUCE SYNTHESIS GAS

Disclosed are catalysts, methods, and systems for the bi-reforming of hydrocarbons. The method includes contacting a catalyst material with a reactant feed that includes hydrogen (H.sub.2), carbon monoxide (CO), carbon dioxide (CO.sub.2), methane (CH.sub.4), and water (H.sub.2O) to produce a product stream that has a H.sub.2/CO molar ratio of 1.4:1 to 2:1. The catalyst can have a metal oxide core, a redox metal oxide layer deposited on a surface of the metal oxide core, and a catalytically active metal deposited on the surface of the redox metal oxide layer. A dopant can be included in the redox metal oxide layer. The catalyst can have a corm-shell type structure.

MICROWAVE CATALYSIS FOR MODULAR PRODUCTION OF CARBON NANOMATERIALS FROM NATURAL GAS
20210371277 · 2021-12-02 ·

In one aspect, the disclosure relates to CO.sub.2-free and/or low-CO.sub.2 methods of co-producing hydrogen and solid forms of carbon via natural gas decomposition using microwave radiation. The methods are efficient, self-sustaining, and environmentally benign. In a further aspect, the disclosure relates to recyclable and recoverable catalysts useful for enhancing the disclosed methods, wherein the catalysts are supported by solid forms of carbon. Methods for recycling the catalysts are also disclosed. This abstract is intended as a scanning tool for purposes of searching in the particular art and is not intended to be limiting of the present disclosure.

A CATALYST COMPOSITION AND METHOD OF MAKING THEREOF FOR PURE HYDROGEN PRODUCTION

The present invention provides an impregnated catalyst composition for production of pure hydrogen comprising: 10 wt %-50 wt % metal oxide; 1 wt %-15 wt % promoter; and 60 wt %-90 wt % support material. Another aspect of the present invention is to provide a method of preparation of an impregnated catalyst for pure hydrogen production (10) and a method for producing pure hydrogen (20) according to the impregnated catalyst of the present invention. The present invention is able to reduce the reaction temperature by 1 to 2 folds and also able to reduce the usage of energy but maintain its good production quality. Besides, selectivity of the present invention is high, hence able to produce high purity of hydrogen.

HETEROJUNCTION PHOTOCATALYST, PHOTOCATALYST COMPOSITE, METHOD FOR PRODUCING HETEROJUNCTION PHOTOCATALYST, AND METHOD FOR PRODUCING HYDROGEN
20230338941 · 2023-10-26 · ·

The present invention provides a heterojunction photocatalyst having higher photocatalytic activity than that of a conventional heterojunction photocatalyst. Further, the present invention provides a photocatalyst composite having the heterojunction photocatalyst on a substrate, a method for producing the heterojunction photocatalyst, and a method for producing hydrogen using the heterojunction photocatalyst or the photocatalyst composite The het junction photocatalyst of the present invention has a solid mediator between a hydrogen-evolution photocatalyst and an oxygen-evolution photocatalyst, and the solid mediator is selectively joined to an electrons collecting surface of the oxygen-evolution photocatalyst.

SYSTEMS AND METHODS FOR PROCESSING AMMONIA
20220395810 · 2022-12-15 ·

The present disclosure provides methods for fabricating catalysts for ammonia decomposition. The method may comprise (a) subjecting a catalyst support to one or more physical or chemical processes to optimize one or more pores, morphologies, and/or surface chemistry or property of the catalyst support; (b) depositing a composite support material on the catalyst support, wherein the composite support material comprises a morphology or surface chemistry or property; and (c) depositing one or more active metals on at least one of the composite support material and the catalyst support, wherein the one or more active metals comprise one or more nanoparticles configured to conform to the morphology of the composite support material and/or catalyst support material, thereby optimizing one or more active sites on the nanoparticles for ammonia processing.

SELECTIVE PRODUCTION OF PROPYLENE AND BUTYLENE FROM METHANE
20220274902 · 2022-09-01 ·

Disclosed are processes for producing propylene and butylene. The processes can include contacting a first stream containing methane with an oxidant and oxidizing at least a portion of the methane under conditions suitable to produce a second stream containing carbon monoxide (CO) and hydrogen (H.sub.2), contacting the second stream with a CO hydrogenation catalyst under conditions suitable to produce a third stream containing propanol and butanol, and contacting the third stream with an dehydration catalyst under conditions suitable to dehydrate at least a portion of the propanol and butanol and produce a products stream containing propylene and butylene.