An apparatus for forming a C1 to C5 oxygenate from carbon dioxide and a C1 to C4 hydrocarbon is described. The apparatus comprises: a dielectric barrier discharge, DBD, device arranged to generate a plasma; and a passageway having an inlet for the carbon dioxide and the C1 to C4 hydrocarbon and an outlet for the oxygenates. In one example the passageway includes therein a catalyst. The passageway extends, at least in part, through the DBD device wherein, in use, the carbon dioxide in reacted with the C1 to C4 hydrocarbon in the generated plasma, thereby forming the oxygenates from at least some of the carbon dioxide and the C1 to C4 hydrocarbon. The DBD device comprises a conducting liquid as a ground electrode. A method and a use are also described.

An apparatus for forming a C1 to C5 oxygenate from carbon dioxide and a C1 to C4 hydrocarbon is described. The apparatus comprises: a dielectric barrier discharge, DBD, device arranged to generate a plasma; and a passageway having an inlet for the carbon dioxide and the C1 to C4 hydrocarbon and an outlet for the oxygenates. In one example the passageway includes therein a catalyst. The passageway extends, at least in part, through the DBD device wherein, in use, the carbon dioxide in reacted with the C1 to C4 hydrocarbon in the generated plasma, thereby forming the oxygenates from at least some of the carbon dioxide and the C1 to C4 hydrocarbon. The DBD device comprises a conducting liquid as a ground electrode. A method and a use are also described.

The present disclosure is directed to microporous crystalline aluminosilicate structures with GME topologies having pores containing organic structure directing agents (OSDAs) comprising at least one piperidinium cation, the compositions useful for making these structures, and methods of using these structures. In some embodiments, the crystalline zeolite structures have a molar ratio of Si:Al that is greater than 3.5.

The present disclosure is directed to microporous crystalline aluminosilicate structures with GME topologies having pores containing organic structure directing agents (OSDAs) comprising at least one piperidinium cation, the compositions useful for making these structures, and methods of using these structures. In some embodiments, the crystalline zeolite structures have a molar ratio of Si:Al that is greater than 3.5.

The present disclosure is directed to microporous crystalline aluminosilicate structures with GME topologies having pores containing organic structure directing agents (OSDAs) comprising at least one piperidinium cation, the compositions useful for making these structures, and methods of using these structures. In some embodiments, the crystalline zeolite structures have a molar ratio of Si:Al that is greater than 3.5.

The present disclosure provides natural gas and petrochemical processing systems including oxidative coupling of methane reactor systems that integrate process inputs and outputs to cooperatively utilize different inputs and outputs of the various systems in the production of higher hydrocarbons from natural gas and other hydrocarbon feedstocks.

The present disclosure provides natural gas and petrochemical processing systems including oxidative coupling of methane reactor systems that integrate process inputs and outputs to cooperatively utilize different inputs and outputs of the various systems in the production of higher hydrocarbons from natural gas and other hydrocarbon feedstocks.

Disclosed are catalysts that include a doped atomic monolayer (e.g., graphene or hexagonal boron nitride) bonded to a nickel-based component. The dopant can be a transition metal or nonmetal dopant and the nickel-based component can be pure nickel (e.g., Ni(111)) or nickel/metal alloys. Also disclosed are processes for catalyzing reactions that include adsorbing a small molecule to the catalyst and contacting the adsorbed small molecule with a reactant. Catalyzed reactions include oxidation reactions including oxidation of methane to methanol, oxidation of carbon monoxide (e.g., in a PROX reaction).

Disclosed are catalysts that include a doped atomic monolayer (e.g., graphene or hexagonal boron nitride) bonded to a nickel-based component. The dopant can be a transition metal or nonmetal dopant and the nickel-based component can be pure nickel (e.g., Ni(111)) or nickel/metal alloys. Also disclosed are processes for catalyzing reactions that include adsorbing a small molecule to the catalyst and contacting the adsorbed small molecule with a reactant. Catalyzed reactions include oxidation reactions including oxidation of methane to methanol, oxidation of carbon monoxide (e.g., in a PROX reaction).

Disclosed are catalysts that include a doped atomic monolayer (e.g., graphene or hexagonal boron nitride) bonded to a nickel-based component. The dopant can be a transition metal or nonmetal dopant and the nickel-based component can be pure nickel (e.g., Ni(111)) or nickel/metal alloys. Also disclosed are processes for catalyzing reactions that include adsorbing a small molecule to the catalyst and contacting the adsorbed small molecule with a reactant. Catalyzed reactions include oxidation reactions including oxidation of methane to methanol, oxidation of carbon monoxide (e.g., in a PROX reaction).