Patents for C10G 11 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils (12,050)
08/2005
08/25/2005WO2005078051A1 Low temperature thermodynamic cracking and conversion for upgrading of heavy oils
08/25/2005WO2005077530A1 Structurally enhanced cracking catalysts
08/25/2005WO2005077527A1 Protective shroud for fcc feed nozzles and method for designing such shroud
08/25/2005WO2005058488A3 Process for the preparation of an oxidic catalyst composition comprising a divalent and a trivalent metal
08/25/2005US20050187410 Mesoporous material and use thereof for the selective oxidation of organic compounds
08/25/2005CA2555218A1 Protective shroud for fcc feed nozzles and method for designing such shroud
08/24/2005EP1169416B1 Production of low sulfur/low nitrogen hydrocrackates
08/24/2005CN1657150A Riser reactor for hydrocarbon fluidized catalytic conversion
08/23/2005US6932959 Macrostructures of porous inorganic material which can have controlled size, shape, and/or porosity and a process for preparing the macrostructures. The macrostructures comprise a three-dimension network of particles of porous inorganic
08/23/2005CA2244863C Hydrocarbon separation
08/18/2005US20050181933 In-situ ZSM-5 synthesis
08/17/2005EP1562852A2 Catalytic partial oxidation of hydrocarbons
08/17/2005EP1562702A1 Co oxidation promoters for use in fcc processes
08/17/2005CN2717959Y Improved secondary steam orifice structure for heavy oil catalytic cracking feeding spray nozzle
08/17/2005CN1655165A Modeling method for residual oil catalytic cracking reaction mechanism model
08/16/2005US6930219 Mesoporous material with active metals
08/16/2005US6930217 Catalyst containing microporous zeolite in mesoporous support and method for making same
08/16/2005US6929736 Compounds, compositions and methods to reduce SOx emissions from FCC units
08/11/2005WO2005073347A1 System and method for selective component cracking to maximize production of light olefins
08/11/2005WO2005072864A1 Nox reduction composition for use in fcc processes
08/11/2005US20050173558 Protective shroud for FCC feed nozzles and method for designing such shroud
08/11/2005US20050173303 Systems, methods, and catalysts for producing a crude product
08/11/2005US20050173302 Crude product is a liquid mixture at 25 degrees C. and 0.101 MPa; catalysts having a pore size distribution with a median pore diameter at least 180 A; Hydrotreating; specific micro-carbon-residue in the product
08/11/2005US20050173301 Systems, methods, and catalysts for producing a crude product
08/11/2005CA2553783A1 System and method for selective component cracking to maximize production of light olefins
08/10/2005CN2716269Y Coking resistant device for rapidly discharging oil gas for reaction settler
08/10/2005CN1653160A Process and apparatus for upgrading FCC product with additional reactor with catalyst recycle
08/10/2005CN1651363A Integrated catalytic cracking and steam pyrolysis process for olefins
08/10/2005CN1213971C Process for the production of olefins
08/09/2005US6926882 Porous inorganic macrostructure materials and process for their preparation
08/09/2005CA2250197C Apparatus and method for the separation and stripping of fluid catalyst cracking particles from gaseous hydrocarbons
08/04/2005US20050167332 in presence of a pore size catalyst; crude product is a liquid mixture at 25 degrees C. and 0.101 MPa; hydrotreating; specific micro-carbon-residue in the product; vacuum gas oil product; total acid number; producing a transportation fuel
08/04/2005US20050167331 Systems, methods, and catalysts for producing a crude product
08/04/2005US20050167330 Systems, methods, and catalysts for producing a crude product
08/04/2005US20050167329 Crude product is a liquid mixture at 25 degrees C. and 0.101 MPa; include sulfur, residue, Micro-Carbon Residue, C5 asphaltenes, or mixtures
08/04/2005US20050167328 Crude product is a liquid mixture at 25 degrees C. and 0.101 MPa; 180 A; Hydrotreating; total acid number (TAN) of 0.3 or more; first hydrogen uptake condition being different from the second hydrogen uptake condition
08/04/2005US20050167327 Systems, methods, and catalysts for producing a crude product
08/04/2005US20050167326 Systems, methods, and catalysts for producing a crude product
08/04/2005US20050167325 Systems, methods, and catalysts for producing a crude product
08/04/2005US20050167324 Systems, methods, and catalysts for producing a crude product
08/04/2005US20050167320 in presence of alumina pore size catalyst and catalyst support; crude product is a liquid mixture at 25 degrees C. and 0.101 MPa; hydrotreating; specific micro-carbon-residue in the product; vacuum gas oil product; total acid number; producing a transportation fuel
08/03/2005EP1558388A1 NO sb X /sb REDUCTION COMPOSITIONS FOR USE IN FCC PROCESSES
08/03/2005EP1558387A1 NO sb X /sb REDUCTION COMPOSITIONS FOR USE IN FCC PROCESSES
08/03/2005EP1558377A2 Highly homogeneous amorphous silica-alumina catalyst composition
08/03/2005EP1558372A1 Improved deep catalytic cracking process
08/03/2005CN2714570Y Access hole of thermal insulated plug
08/03/2005CN1648212A Method for cracking hydrocarbon oil
08/03/2005CN1648211A Hydrocarbon oil cracking method
08/03/2005CN1648210A Hydrocarbon cracking catalyst and its preparing method
08/03/2005CN1648209A High efficiency atomizing material feeding nozzle for heavy oil catalytic cracking
08/02/2005US6923903 Gasoline sulfur reduction in fluid catalytic cracking
08/02/2005CA2190844C Two-phase distributor system for downflow reactors
07/2005
07/28/2005US20050163691 NOx reduction composition for use in FCC processes
07/28/2005US20050163674 Improved selectivity to propene and butenes using riser reactor configured with two sections of different radii; revamping middle section of fluid cracking system
07/28/2005US20050161369 System and method for selective component cracking to maximize production of light olefins
07/28/2005US20050160666 Forming high quality oil from waste vegetable oils by compression and purification
07/27/2005EP1556462A1 Process for fluid catalytic cracking of hydrocarbon feedstocks with high levels of basic nitrogen
07/27/2005EP1556316A1 Fluid bed oxygenates to olefins reactor apparatus and process of controlling same
07/27/2005EP1220881B1 Reducing gasoline sulfur in fluid catalytic cracking
07/27/2005CN1646664A Process and apparatus for upgrading FCC product with additional reactor with thorough mixing
07/27/2005CN1646221A Molecular sieve compositions, catalyst thereof, their making and use in conversion processes
07/27/2005CN1644653A Catalyst and method for producing light fuel oil
07/27/2005CN1212372C Catalytic conversion method using C4 fraction to increase small molecule olefine hydrocarbon yield
07/27/2005CN1212371C Method of catalytic gasoline upgrading and lowering olefin hydrocarbon with high light oil yield and its device
07/27/2005CN1212370C Catalytic conversion method for reducing sulphur content of gasoline
07/27/2005CN1212194C Cracking catalyst for hydrocarbons and its preparation
07/21/2005US20050155908 Systems, methods, and catalysts for producing a crude product
07/21/2005DE10356245A1 Dieselöl aus Reststoffen durch katalytische Depolymerisation mit dem Energieeintrag in einem Pumpen-Rührwerkssystem Diesel oil from waste by catalytic depolymerization with the energy input in a pump-Rührwerkssystem
07/20/2005EP1555308A1 Integrated catalytic cracking and steam pyrolysis process for olefins
07/20/2005CN2711168Y Raw material oil spray nozzle of catalytic cracking installation
07/20/2005CN1643112A Method for jointly producing propylene and petrol from a heavy charge
07/20/2005CN1643111A Process for combusting coke in regeneration of catalyst
07/20/2005CN1642887A Multi-step method of converting a charge containing olefins with four, five or more carbon atoms in order to produce propylene
07/20/2005CN1642857A Crystalline aluminosilicate zeolitic composition: UZM-9
07/20/2005CN1642648A Catalyst compositions comprising molecular sieves, their preparation and use in conversion processes
07/20/2005CN1641307A Method for manufacturing oil slurry vapour generator
07/20/2005CN1211457C Silicate composition and preparation method and application thereof
07/19/2005CA2359779C Catalytic cracking process
07/14/2005US20050152814 Catalysis of oxygenate feed in multiple riser reactors producing a light olefin, separating and transporting the molecular seive to a regenerator for reuse; proper aspect ratio for a given riser reactor without the need for multiple, independent reactor systems
07/14/2005US20050150818 Systems, methods, and catalysts for producing a crude product
07/14/2005US20050150817 Integration of gas oil and light olefin catalytic cracking zones with a pyrolytic cracking zone to maximize efficient production of petrochemicals; allows production of product stream with maximum ethylene and/or propylene by routing various feedstreams and recycle streams to the appropriate zones
07/14/2005DE10357263A1 Recovery of liquid fuel components and precursors from waste containing hydrocarbons, e.g. polypropylene and polyethylene, uses mixture of plastics or coal and non-aromatic mineral oil and repeated heating and cooling with pause
07/13/2005EP1551940A1 A method for preparing a substitute for fresh fluid catalytic cracking catalyst
07/13/2005CN1639298A 催化裂化工艺 FCC Process
07/13/2005CN1638865A Molecular sieve compositions, catalyst thereof, their making and use in conversion processes
07/13/2005CN1636633A Prepn process of cracking catalyst
07/12/2005US6916762 Catalyst for fluidized catalytic cracking of heavy hydrocarbon oil and method of fluidized catalytic cracking
07/12/2005US6916459 Zeolite ITQ-16
07/12/2005US6916417 Catalytic cracking of a residuum feedstock to produce lower molecular weight gaseous products
07/12/2005US6916416 Fluid is mixed with an atomizing fluid in a plurality of locations and passed through a nozzle in an FCC feed injector comprising a plurality of mixing zones
07/07/2005WO2005061679A1 Process for reducing the pour point and viscosity of fischer-tropsch wax
07/07/2005WO2004105930A3 Fcc catalyst injection system having closed loop control
07/07/2005US20050145543 in presence of a pore size catalyst; crude product is a liquid mixture at 25 degrees C. and 0.101 MPa; hydrotreating; specific micro-carbon-residue in the product; vacuum gas oil product; nitrogen content; producing a transportation fuel
07/07/2005US20050145542 Process for small-scale testing of FCC catalysts
07/06/2005EP1073701B1 Reduction of sulphur content in fcc-naphtha
07/06/2005CN1635986A Production of olefins
07/06/2005CN1209445C Method for prepn. of catalytic emulsion
07/06/2005CN1209443C Prodn. of olefins
07/06/2005CN1209442C Catalytic cracking catalyst and its prepn
07/06/2005CN1209288C Modified octahedral zeolite
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