| Patent application number | Description | Published |
|---|
| 20120266525 | PROCESS FOR CONVERTING A SOLID BIOMASS MATERIAL - 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. | 10-25-2012 |
| 20120266838 | LIQUID FUEL COMPOSITION - 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. | 10-25-2012 |
| 20120271073 | PROCESS FOR REGENERATING A COKED CATALYTIC CRACKING CATALYST - 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. | 10-25-2012 |
| 20120271074 | PROCESS FOR CONVERTING A SOLID BIOMASS MATERIAL - 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. | 10-25-2012 |
| 20120271075 | SEPARATION OF PRODUCT STREAMS - A method of purifying a vapour product stream obtained from cracking of biomass catalysed by a fluidised solid catalyst is provided. The catalyst is separated from the vapour product stream to provide a de-catalysed vapour product stream. Solid biomass residue is cyclonically separated from the de-catalysed vapour product stream to provide a purified vapour product stream. | 10-25-2012 |
| 20120277499 | SUSPENSION OF SOLID BIOMASS PARTICLES IN A HYDROCARBON-CONTAINING LIQUID - 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. | 11-01-2012 |
| 20120289752 | PROCESS FOR CONVERTING A SOLID BIOMASS MATERIAL - 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. | 11-15-2012 |
| 20120291340 | CONVERSION OF A SOLID BIOMASS MATERIAL - 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:
| 11-22-2012 |
