Shell Oil Comapny

Johan Willem Gosselink

Colin John Schaverien

Andries Hendrik Janssen

John William Harris

Nicolaas Wilhelmus Joseph Way

Andries Quirin Maria Boon

Sander Van Paasen

Antonius Adrianus Maria Roovers

Michiel Jan Groeneveld

Andreas Karl Nowak

Richard John Price

Johannes Anthonius Robert Van Veen

Hennie Schaper

Johannes Anthonius Van Veen

Martin Jean Pierre Cornelis Nieskens

Easwar Santhosh Ranganathan

Lucas R Groeneveld

Arend-Jan Van Welsenes

A process for regenerating a coked catalytic cracking catalyst which the carbon-containing deposits on the catalyst contains at least 1 wt % bio-carbon, based on the total weight of carbon present in the carbon-containing deposits is provided. Such coked catalytic cracking catalyst is contacted with an oxygen containing gas at a temperature of equal to or more than 550&#xb0; C. in a regenerator to produce a regenerated catalytic cracking catalyst, heat and carbon dioxide.

Process for regenerating a coked catalytic cracking catalyst

A process for converting a solid biomass material is provided. The solid biomass material is contacted with a catalytic cracking catalyst at a temperature of more than 400&#xb0; C. in a riser reactor to produce one or more cracked products. The riser reactor is an external riser reactor with a curve and/or low velocity zone at its termination and wherein a part of the catalytic cracking catalyst has deposited in the curve and/or low velocity zone.

Process for converting a solid biomass material

A process to prepare a suspension of solid biomass particles in a hydrocarbon-containing liquid for a catalytic cracking process is provided. A catalytic cracking process and subsequent processing of the cracked product from such suspension of solid biomass particles in the hydrocarbon-containing liquid is also provided.

Suspension of solid biomass particles in a hydrocarbon-containing liquid

A process for converting a solid biomass material by contacting the solid biomass material with a catalytic cracking catalyst at a temperature of more than 400&#xb0; C. in a riser reactor to produce one or more cracked products is provided, wherein the riser reactor is an internal riser reactor.

A liquid fuel composition containing a biofuel component, produced from a fraction of one or more cracking products produced by catalytic cracking of a biomass source. The liquid fuel composition contains in the range of 0.5 to 20 vol. % of C4-C8-olefins, which C4-C8-olefins contain in the range from equal to or more than 0.02 wt % to equal to or less than 100 wt % of bio-carbon, based on the total weight of carbon present in the C4-C8-olefins.

Liquid fuel composition

A process for converting a solid biomass material, comprising contacting the solid biomass material and a hydrocarbon co-feed with a catalytic cracking catalyst at a temperature of more than 400&#xb0; C. in a riser reactor to produce one or more cracked products, wherein the solid biomass material is introduced to the riser reactor at a location downstream of the location where the hydrocarbon co-feed is introduced to the riser reactor.

A process or a system for converting a solid biomass material is provided, comprising contacting the solid biomass material with a catalytic cracking catalyst at a temperature of more than 400&#xb0; C. in a riser reactor to produce one or more cracked products. The riser reactor contains: a riser reactor pipe, which riser reactor pipe has a diameter that increases in a downstream direction; and a bottom section connected to the riser reactor pipe, which bottom section has a larger diameter than the riser reactor pipe.

Conversion of a solid biomass material

A method for treating hydrocarbonaceous feedstock to produce hydrogen, electricity, and one or more liquid hydrocarbon product, the method comprising: (a) subjecting hydrocarbonaceous feedstock to hydrotreating hydrogen in the presence of supported catalyst under hydrotreating conditions effective to produce hydrotreated product comprising one or more liquid hydrocarbon product; (b) subjecting hydrotreated product to hydrogen production conditions effective to produce hydrogen product and hydrogen production remainder; (c) subjecting a first part of the hydrogen product to electricity generating conditions effective to produce electricity; and (d) recycling a second part of the hydrogen product as hydrotreating hydrogen.

Hydrocarbon hydroconversion process for the production of hydrogen, hydroprocessed hydrocarbons and electricity

Method for producing hydrogen and a hydroprocessed product from a hydrocarbonaceous feedstock by subjecting it to a catalytic hydrocracking treatment using hydrogen which has been at least partly produced from hydrocracked feedstock and subjecting at least pan of the hydrocracked feedstock, after having subjected it to a separation treatment in the event that hydroprocessed product is to be recovered, to a treatment to produce hydrogen in a single operation which hydrogen is at least partly recovered as product.

Hydrocarbon conversion process

Process for the preparation of a catalyst composition

The present invention provides a process for the preparation of a catalyst composition which comprises, as first cracking component, a zeolite beta with a silica to alumina molar ratio of at least 20 comprising crystals less than 100 nm in size, and a second cracking component selected from (i) crystalline molecular sieves having pores with diameters greater than 0.6 nm, and (ii) clays, the process comprising the steps of:

A process for converting hydrocarbon oils into products of lower average molecular weight and lower boiling point comprising contacting a hydrocarbon oil containing less than 200 ppm N at elevated temperature and pressure in the presence of hydrogen with a catalyst A comprising a wide pore zeolite, a binder and at least one hydrogenation component of a Group VI and/or Group VIII metal, wherein the hydrocarbon oil is subsequently, without intermediate separation or liquid recycle, contacted with an amorphous silica-alumina containing catalyst B comprising at least one hydrogenation component of a Group VI and/or Group VIII metal.

Growing community of inventors

Amsterdam, Netherlands

Johan Willem Gosselink