| Patent application number | Description | Published |
|---|
| 20090026112 | FLUID CATALYTIC CRACKING PROCESS - A fluid catalytic cracking process for the preparation of cracked products by contacting in a reactor a hydrocarbon feedstock with a cracking catalyst, wherein the hydrocarbon feedstock comprises a paraffinic feedstock and triglycerides. | 01-29-2009 |
| 20100163455 | SYSTEMS AND METHODS FOR MAKING A MIDDLE DISTILLATE PRODUCT AND LOWER OLEFINS FROM A HYDROCARBON FEEDSTOCK - A system comprising a riser reactor comprising a gas oil feedstock and a first catalyst under catalytic cracking conditions to yield a riser reactor product comprising a cracked gas oil product and a first used catalyst; a intermediate reactor comprising at least a portion of the cracked gas oil product and a second catalyst under high severity conditions to yield a cracked intermediate reactor product and a second used catalyst; wherein the intermediate reactor feedstock comprises at least one of a fatty acid and a fatty acid ester. | 07-01-2010 |
| 20110119994 | PROCESS FOR CATALYTIC HYDROTREATMENT OF A PYROLYSIS OIL - A process for catalytic hydrotreatment of a pyrolysis oil derived from lignocelluloses is provided. | 05-26-2011 |
| 20110257446 | PROCESS FOR PRODUCING HYDROCARBONS FROM MICROBIAL LIPIDS - A process for producing hydrocarbons from microbial lipids is provided by: contacting a feed comprising microbial lipids, wherein the microbial lipids comprise a triglyceride content in the range of from 40 wt % to 70 wt % and a free fatty acid content in the range of from 10 wt % to 30 wt %, with a hydrogenation catalyst and hydrogen at a temperature in the range of from 250 to 380° C. and a total pressure in the range of from 20 to 160 bar (absolute), to obtain an effluent comprising paraffinic hydrocarbons and water; optionally separating a liquid stream rich in paraffinic hydrocarbons from the effluent; contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerisation catalyst at a temperature in the range of from 280 to 450° C. and a total pressure in the range of from 20 to 160 bar (absolute); and separating at least one product fraction from the product stream. | 10-20-2011 |
| 20110257447 | PROCESS FOR PRODUCING HYDROCARBONS FROM MICROBIAL LIPIDS - A process for producing hydrocarbons from microbial lipids is provided by contacting a feed comprising microbial lipids with a hydrogenation catalyst and hydrogen at a temperature in the range of from 250 to 380° C. and a total pressure in the range of from 20 to 160 bar (absolute), to obtain an effluent comprising paraffinic hydrocarbons and water; optionally separating a liquid stream rich in paraffinic hydrocarbons from the effluent; contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerisation catalyst at a temperature in the range of from 280 to 450° C. and a total pressure in the range of from 20 to 160 bar (absolute); and separating at least one product fraction from the product stream obtained, wherein the hydrogenation catalyst and/or the hydroisomerisation catalyst comprises a sulfided hydrogenation catalyst. | 10-20-2011 |
| 20120151829 | PROCESS FOR CATALYTIC CRACKING OF AQUATIC MICROBIAL BIOMASS - 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. | 06-21-2012 |
| 20120151831 | CATALYTIC CRACKING PROCESS OF A LIPID-CONTAINING FEEDSTOCK - A process for catalytic cracking of a lipid-containing feedstock is provided. The lipid-containing feedstock contains lipids derived from microalgae and a hydrocarbon feedstock. The lipid-containing feedstock is contacted with at least one cracking catalyst at a temperature of at least 450° C., to obtain a product stream; and separating at least one hydrocarbon fraction from the product stream. | 06-21-2012 |
| 20120151832 | CATALYTIC CRACKING PROCESS OF A LIPID-CONTAINING FEEDSTOCK - A process for catalytic cracking of a lipid-containing feedstock is provided. The lipid-containing feedstock contains lipids derived from a diatomic microalgae species. The lipid-containing feedstock is contacted with at least one cracking catalyst at a temperature of at least 450° C., to obtain a product stream; and separating at least one hydrocarbon fraction from the product stream. | 06-21-2012 |
| 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 |
| 20130109892 | PROCESS FOR CONVERTING A SOLID BIOMASS MATERIAL | 05-02-2013 |
| 20130118059 | PROCESS FOR CONVERSION OF A CELLULOSIC MATERIAL - A process for conversion of a cellulosic material comprising
| 05-16-2013 |
| 20130178672 | PROCESS FOR MAKING A DISTILLATE PRODUCT AND/OR C2-C4 OLEFINS - A process for making a distillate product and one or more C2-C4 olefins from a FCC feedstock containing a cellulosic material and a hydrocarbon co-feed is provided. | 07-11-2013 |
| 20130276360 | PROCESS FOR CONVERTING A SOLID BIOMASS MATERIAL - 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. | 10-24-2013 |
| 20140115951 | PROCESS FOR CONVERTING A SOLID BIOMASS MATERIAL - A process for converting a solid biomass material comprising a) providing a pneumatic fluid; b) dispersing the solid biomass material into the pneumatic fluid to prepare a pneumatic dispersion and transporting the pneumatic dispersion to a reactor; and c) contacting the pneumatic dispersion with a catalyst in the reactor to produce a product stream comprising one or more conversion products. | 05-01-2014 |
| 20140296592 | PROCESS FOR THE FLUID CATALYTIC CRACKING OF OXYGENATED HYDROCARBON COMPOUNDS FROM BIOLOGICAL ORIGIN - A process for the fluid catalytic cracking of oxygenated hydrocarbon compounds from biological origin. The process comprises (a) contacting a feed comprising the oxygenated hydrocarbon compounds with a fluid catalytic cracking catalyst at elevated temperature to produce a cracked products stream, the feed comprising an amount of sulphur; (b) separating catalyst from the cracked products stream; (c) separating a light fraction from the cracked products stream; and (d) removing hydrogen sulphide from the light fraction by means of an amine treating process. The fluid catalytic cracking process involves the presence or use of water and/or steam and comprises a working-up process of the cracked products stream. In the working-up process, one or more chemical additives for reducing or hindering the formation of foam in amine liquids selected from defoamers and demulsifiers are added to the amine solvent in one or more amine treaters. | 10-02-2014 |
| 20140296593 | PROCESS FOR THE FLUID CATALYTIC CRACKING OF OXYGENATED HYDROCARBON COMPOUNDS FROM BIOLOGICAL ORIGIN - A process for the fluid catalytic cracking of oxygenated hydrocarbon compounds from biological origin. The process comprises contacting a feed comprising the oxygenated hydrocarbon compounds from biological origin and an amount of sulphur with a fluid cracking catalyst at a temperature of equal to or more than 400° C. to produce a products stream. The process further comprises separating fluid cracking catalyst from the products stream and separating a light fraction from the products stream; and removing hydrogen sulphide from the light fraction by means of an amine treating process. Activated carbon is used to treat at least part of an amine solution used in the amine treating process or to treat at least part of the feed to the amine treating process. | 10-02-2014 |
| 20140296594 | PROCESS FOR THE FLUID CATALYTIC CRACKING OF OXYGENATED HYDROCARBON COMPOUNDS FROM BIOLOGICAL ORIGIN - A process for the fluid catalytic cracking of oxygenated hydrocarbon compounds from biological origin. The process comprises (a) contacting a feed comprising the oxygenated hydrocarbon compounds from biological origin with a fluid cracking catalyst at a temperature of equal to or more than 400° C. to produce a products stream; (b) separating fluid cracking catalyst from the products stream and separating a fraction comprising one or more C1-C4 hydrocarbon compounds from the products stream; and (c) processing the fraction comprising one or more C1-C4 hydrocarbon compounds in a work-up process, which comprises one or more oil/water separation steps. One or more de-emulsifiers are added to one or more oil/water separation steps. | 10-02-2014 |
| 20140330057 | PROCESS FOR CONVERTING A BIOMASS MATERIAL - A process for converting a biomass material comprising a) pyrolyzing a biomass material to produce a biomass-derived pyrolysis product; b) mixing at least part of the biomass-derived pyrolysis product and a petroleum-derived hydrocarbon composition, which petroleum derived hydrocarbon composition has a C7-asphaltenes content of equal to or more than 0.2 wt %, based on the total weight of the petroleum-derived hydrocarbon composition, to produce a hydrocarbon-containing mixture; c) dewatering the hydrocarbon-containing mixture to produce a dewatered hydrocarbon-containing mixture; d) contacting the dewatered hydrocarbon-containing mixture with hydrogen in one or more ebullating bed reactors comprising a catalyst at a temperature in the range from 350 to 500° C. to produce a reaction product. | 11-06-2014 |
