Abstract: 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° C. in a regenerator to produce a regenerated catalytic cracking catalyst, heat and carbon dioxide.

Abstract: 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° 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.

Abstract: 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.

Abstract: 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° C. in a riser reactor to produce one or more cracked products is provided, wherein the riser reactor is an internal riser reactor.

Abstract: 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.

Abstract: 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° 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.

Abstract: 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° C. in a regenerator to produce a regenerated catalytic cracking catalyst, heat and carbon dioxide.

Abstract: 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° C. in a regenerator to produce a regenerated catalytic cracking catalyst, heat and carbon dioxide.

Abstract: 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° 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.

Abstract: 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° 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.

Abstract: 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° C. in a riser reactor to produce one or more cracked products is provided, wherein the riser reactor is an internal riser reactor.

Abstract: 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° 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.

Abstract: A process for converting a solid biomass material is provided. The solid biomass material and a fluid hydrocarbon feed is contacted with a catalytic cracking catalyst at a temperature of more than 400° C. in a catalytic cracking reactor to produce one or more cracked products which are then fractionated to produce one or more product fractions; then hydrodeoxygenated to produce one or more hydrodeoxygenated products.

Abstract: 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.

Abstract: A process for converting a solid biomass material is provided. The solid biomass material and a fluid hydrocarbon feed is contacted with a catalytic cracking catalyst at a temperature of more than 400° C. in a riser reactor to produce one or more cracked products. The solid biomass material is supplied to the riser reactor at a location upstream of the location where the fluid hydrocarbon feed is supplied to the riser reactor.

Abstract: 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° C. in a regenerator to produce a regenerated catalytic cracking catalyst, heat and carbon dioxide.

Abstract: 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° 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.

Abstract: 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.

Abstract: A process for catalytically cracking aquatic microbial biomass is provided. Aquatic microbial biomass is catalytically cracked over a cracking catalyst at a temperature of at least 450° C. to obtain a product stream. At least one hydrocarbon fraction is separated from the product stream.

Abstract: 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.