Patent application number | Description | Published |
20090308787 | PROCESS FOR CONVERTING CARBON-BASED ENERGY CARRIER MATERIAL - A process is disclosed process for converting a solid or highly viscous carbon-based energy carrier material to liquid and gaseous reaction products, said process comprising the steps of: a) contacting the carbon-based energy carrier material with a particulate catalyst material b) converting the carbon-based energy carrier material at a reaction temperature between 200° C. and 450° C., preferably between 250° C. and 350° C., thereby forming reaction products in the vapor phase. In a preferred embodiment the process comprises the additional step of: c) separating the vapor phase reaction products from the particulate catalyst material within 10 seconds after said reaction products are formed; In a further preferred embodiment step c) is followed by: d) quenching the reaction products to a temperature below 200° C. | 12-17-2009 |
20110197511 | PROCESS FOR CONVERTING CARBON-BASED ENERGY CARRIER MATERIAL - A process is disclosed process for converting a solid or highly viscous carbon-based energy carrier material to liquid and gaseous reaction products, said process comprising the steps of: a) contacting the carbon-based energy carrier material with a particulate catalyst material b) converting the carbon-based energy carrier material at a reaction temperature between 200° C. and 450° C., preferably between 250° C. and 350° C., thereby forming reaction products in the vapor phase. In a preferred embodiment the process comprises the additional step of: c) separating the vapor phase reaction products from the particulate catalyst material within 10 seconds after said reaction products are formed. In a further preferred embodiment step c) is followed by: d) quenching the reaction products to a temperature below 200° C. | 08-18-2011 |
20120323057 | Process for Converting Cellulose and/or Hemicellulose in a Liquid Fuel Comprising Dissolution in Ionic Liquid - A process is disclosed for converting cellulose to liquid fuels. In the process the cellulose is dissolved in an ionic Liquid medium. The conversion process may comprise pyrolysis, thermal cracking, hydrocracking, catalytic cracking, hydrotreatment, or a combination thereof. The Ionic Liquid medium preferably is an inorganic molten salt hydrate. | 12-20-2012 |
20120330074 | Simultaneous Catalytic Conversion of Cellulose and Lignin to a Liquid Fuel in an Ionic Liquid - A process is disclosed for converting lignocellulosic material to liquid fuels. In the process the cellulose is dissolved in an Ionic Liquid medium. The conversion process may comprise pyrolysis, thermal cracking, hydrocracking, catalytic cracking, hydrotreatment, or a combination thereof. The conversion reaction is carried out in the presence of lignin. The lignin is at least partially converted in the process. The Ionic Liquid medium preferably is an inorganic molten salt hydrate. | 12-27-2012 |
20130245252 | SIMULTANEOUS HYDROLYSIS AND HYDROGENATION OF CELLULOSE - A process is disclosed for conversion of cellulose in an Ionic Liquid medium. The process is characterized in that a cellulose-containing feedstock and an Ionic Liquid are mixed at a temperature below 80 ° C. The mixture is heated to a conversion temperature in the range of 80 ° C. to 220 ° C. under a hydrogen atmosphere. The presence of hydrogen during the heating step significantly reduces the formation of degradation products. | 09-19-2013 |
20130245346 | Improved Process for Converting Carbon-Based Energy Carrier Material - A process is disclosed process for converting a solid or highly viscous carbon-based energy carrier material to liquid and gaseous reaction products, said process comprising the steps of: a) contacting the carbon-based energy carrier material with a particulate catalyst material b) converting the carbon-based energy carrier material at a reaction temperature between 200° C. and 450° C., preferably between 250° C. and 350° C., thereby forming reaction products in the vapor phase. In a preferred embodiment the process comprises the additional step of: c) separating the vapor phase reaction products from the particulate catalyst material within 10 seconds after said reaction products are formed. In a further preferred embodiment step c) is followed by: d) quenching the reaction products to a temperature below 200° C. | 09-19-2013 |
20140039208 | PROCESS FOR CONVERTING POLYSACCHARIDES IN AN INORGANIC MOLTEN SALT HYDRATE - A process is disclosed for converting polysaccharides to platform chemicals. The process comprises dissolving the polysaccharides in a inorganic molten salt hydrate, converting the polysaccharides to monosaccharides, and converting the monosaccharides to platform chemicals that are easily separable from the inorganic molten salt hydrate. | 02-06-2014 |
20140323746 | ISOLATION OF ANHYDRO SUGAR ALCOHOLS BY SELECTIVE ADSORBENTS - A method is disclosed for recovering anhydrosugar alcohols from a mixture comprising closely related compounds, such as sugar alcohols. In the method the mixture is contacted with an adsorbent, whereby the anhydrosugar alcohols are selectively adsorbed. The anhydrosugar alcohols can be recovered by desorption from the adsorbent, using a desorbing solvent. | 10-30-2014 |
20140331992 | PROCESS FOR RECOVERING SACCHARIDES FROM CELLULOSE HYDROLYSIS REACTION MIXTURE - A method is disclosed for recovering saccharide monomers and/or oligomers from a reaction mixture. The reaction mixture may further comprise water and a molten salt hydrate. | 11-13-2014 |