Document |
Document Title |
WO/2011/045483A1 |
The invention relates to a method for the hydrocracking and/or hydroprocessing of hydrocarbon feeds, using a catalyst comprising at least one hydro-dehydrogenating metal selected from the group containing metals from group VIB and non-no...
|
WO/2011/045484A1 |
The invention relates to a method for producing middle distillates from a paraffin feedstock produced by means of Fischer-Tropsch synthesis, implementing a hydrocracking/hydroisomerization catalyst that includes at least one hydro-dehydr...
|
WO/2011/044549A1 |
This invention relates to a process for hydroprocessing heavy oil under process intensification conditions to form an upgraded hydrocarbon product.
|
WO/2011/043936A2 |
Processes are provided for using employing lower activity hydrodesulfurization catalysts while achieving a desired product sulfur content. After determining effective reaction conditions for hydrodesulfurization using a reference catalys...
|
WO/2011/042617A2 |
The invention relates to a method for hydroconverting heavy carbonaceous loads comprising a step (1) for hydroconverting the load in at least one reactor containing a bubbling bed catalyst, and then a step (2) for hydroconverting at leas...
|
WO/2011/038027A1 |
A hydrocarbon synthesizer system for the production of petroleum fractions from a feedstock. Methods of synthesizing hydrocarbons from a feedstock.
|
WO/2011/037901A2 |
This invention relates to processes for the production of a fuel composition from a feedstock that comprises lipid material (e.g., bio- material) and mineral oil. The processes can be carried out without producing a significant mount of ...
|
WO/2011/034064A1 |
Disclosed is a method of hydrocracking which comprises: a wax-fraction hydrocracking step in which a wax fraction separated from a Fischer-Tropsch synthesis oil is hydrocracked to obtain a hydrocracking product; a gas-liquid separation s...
|
WO/2011/025002A1 |
Disclosed is a method for producing an aviation fuel oil base, which comprises: a first step wherein a raw material oil containing an oxygen-containing hydrocarbon compound that is derived from an animal/plant oil or fat is brought into ...
|
WO/2011/021459A1 |
Disclosed are a carrier capable of supplying a zeolite hydrocracking catalyst that has a stable catalyst life and exhibits long-term high cracking activity, a hydrocracking catalyst using the same, and a hydrocracking method for aromatic...
|
WO/2011/017720A1 |
The invention provides a fully synthetic aviation fuel or aviation fuel component having : " a total naphthenic content of more than 30 mass % " a mass ratio of naphthenic to iso-paraffinic hydrocarbon species of more than 1 and less tha...
|
WO/2011/016413A1 |
Disclosed is a hydrocracking catalyst for heavy oil, which has cracking and desulfurization activities for heavy oil and has excellent cracking and desulfurization functions. The hydrocracking catalyst for heavy oil comprises a carrier c...
|
WO/2011/014612A2 |
A wax fraction from a hydrocarbon synthesis process is fractionated in a vacuum distillation column prior to any hydrocracking steps. A straight-run distillation fraction is isolated from the vacuum distillation. A heavy wax fraction fro...
|
WO/2011/013272A1 |
Disclosed is a catalyst for the production of a monocyclic aromatic hydrocarbon, which can be used for the production of a monocyclic aromatic hydrocarbon having 6 to 8 carbon atoms from a crude oil having a 10-vol% distillation temperat...
|
WO/2011/011200A2 |
A hydroconversion process is disclosed, including contacting of hydrogen and a residuum hydrocarbon with a pre-conditioned and at least partially sulfided hydroconversion catalyst for converting at least a portion of the residuum hydroca...
|
WO/2011/007046A2 |
In the process of the invention, an aliphatic C2 -C 14 hydrocarbon product is prepared from natural fats or derivatives thereof. The process comprises the steps of: (i) providing a natural fat or derivative thereof, (ii) deoxygenating a ...
|
WO/2011/002782A2 |
The present invention is directed to a hydroprocessing catalyst containing at least one catalyst support, one or more metals, optionally one or more molecular sieves, optionally one or more promoters, wherein deposition of at least one o...
|
WO/2010/151463A2 |
A process and apparatus are disclosed for converting heavy hydrocarbon feed into lighter hydrocarbon products. The heavy hydrocarbon feed is slurried with a particulate solid material to form a heavy hydrocarbon slurry and hydrocracked i...
|
WO/2010/151462A2 |
A composition is produced from converting heavy hydrocarbon feed into lighter hydrocarbon products. The heavy hydrocarbon feed is slurried with a particulate solid material to form a heavy hydrocarbon slurry and hydrocracked in a slurry ...
|
WO/2010/151300A1 |
Processes for upgrading resid hydrocarbon feeds are disclosed. The upgrading processes may include: hydrocracking a resid in a first reaction stage to form a first stage effluent; hydrocracking a deasphalted oil fraction in a second reac...
|
WO/2010/143980A1 |
The invention relates to a system for integrating methanol production and hydroprocessing of oil feedstock comprising: a first feedstock comprising hydrocarbons that is fed to a steam reformer to produce synthesis gas comprising carbon m...
|
WO/2010/142397A2 |
A process for recovering metals from a stream rich in hydrocarbons and carbonaceous residues by means of a treatment section, characterized in that it comprises the following steps: sending said stream to a primary treatment, effected in...
|
WO/2010/144191A2 |
A method is provided to reduce carbon dioxide emissions and increase the output of more valuable hydrocarbon products in a fluid catalytic cracking unit.
|
WO/2010/124935A1 |
Process of preparing a hydrocracking catalyst carrier comprising amorphous binder and zeolite Y, which process comprises subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 7...
|
WO/2010/116603A1 |
Disclosed is an efficient production method for alkyl benzenes with high added value, and a catalyst used in same, wherein said production method suppresses a decrease in activity accompanying carbon deposition on the catalyst resulting ...
|
WO/2010/117614A2 |
One exemplary embodiment of the present invention can be a fired heater for a hydrocarbon conversion process. The fired heater includes inlet and outlet headers or manifolds, a set of heater tubes with each heater tube having an inlet an...
|
WO/2010/112691A1 |
The invention relates to a method for the production of middle distillates from a paraffin feed produced by means of Fischer-Tropsch synthesis and divided into two fractions, namely a light fraction, called cold condensate, and a heavy f...
|
WO/2010/112690A1 |
The invention relates to a method for the production of middle distillates from a liquid paraffin feed C5+, known as a heavy fraction, having an initial boiling point of between 15 and 40°C and produced by means of Fischer-Tropsch synth...
|
WO/2010/113174A1 |
The present invention relates to a fluidized catalytic cracking process for cracking hydrocarbon feed having organo-sulfur compound as an impurity, said process comprising: adding a heavy metal poisoned spent catalyst to an equilibrium c...
|
WO2010109817A1 |
Disclosed is a method for producing a liquid fuel, wherein hydrocarbon is synthesized from a synthesis gas by Fischer-Tropsch synthesis and then a fuel liquid is producing using the hydrocarbon. The method for producing a liquid fuel is ...
|
WO/2010/103245A2 |
The invention relates to a hydrocarbon fluid that is useful in the composition of materials for industrial, agricultural, or domestic use, having a pour point that is less than -15°C according to the ASTM D97 standard, having initial an...
|
WO/2010/103244A1 |
The invention relates to a hydrocarbon diluent for diluting a polymer having a pour point that is less than -15°C according to the ASTM D97 standard and a boiling temperature of 280 to 450°C, including more than 50 wt % of isoparaffins...
|
WO/2010/093732A2 |
This invention is directed to a high conversion hydrocracking (HCR) unit to produce premium middle distillate fuel. Unconverted oil which is low in sulfur is fed to a Fluid Catalytic Cracking (FCC) unit. The process results in reduced hy...
|
WO/2010/090811A1 |
Herein disclosed is a method for hydrodesulfurization, hydrodenitrogenation, hydrofinishing, amine production or a combination thereof. The method comprises forming a dispersion comprising hydrogen-containing gas bubbles dispersed in a l...
|
WO/2010/085168A1 |
The invention relates to the oil-refining, petrochemical, chemical and fuel-and-energy industries, more specifically, to the preparation and deep conversion of oil, including heavy oil, natural bitumen, residues of oil-refining and petro...
|
WO/2010/077513A2 |
Methods are disclosed for hydrocracking processes that convert a significant portion of a heavy hydrocarbon feedstock such as vacuum gas oil (VGO) to lower molecular weight, lower boiling hydrocarbons. In addition to molecular weight red...
|
WO/2010/077352A1 |
An integrated process for producing naphtha fuel, diesel fuel and/or lubricant base oils from feedstocks under sour conditions is provided. The ability to process feedstocks under higher sulfur and/or nitrogen conditions allows for reduc...
|
WO/2010/077476A2 |
A process for improving cold flow properties of diesel range hydrocarbons produced from renewable feedstocks such as plant oils and animal oils. A renewable feedstock is treated by hydrogenating and deoxygenating to provide an effluent c...
|
WO/2010/074923A2 |
A process for producing a fuel or fuel blending component from co-processing at least two different classes of renewable feedstocks, is presented. One feedstock comprises glycerides and free fatty acids in feedstocks such as plant and an...
|
WO/2010/068203A1 |
Paraffin compositions including mainly even carbon number paraffins, and a method for manufacturing the same, is disclosed herein. In one embodiment, the method involves contacting naturally occurring fatty acid/glycerides with hydrogen ...
|
WO/2010/065128A1 |
A porous material comprises oxides of silicon and aluminum and is substantially free of X-ray diffraction peaks in its calcined form. The material is characterized by the following properties: (a) a Bronsted acid site density as measured...
|
WO/2010/064947A1 |
The invention relates to oil processing, in particular to a method for thermally cracking heavy oil raw material, can be used for the targeted processing of heavy oils, atmospheric and vacuum distillation residues and refinery waste such...
|
WO/2010/062932A1 |
Methods are provided for producing a jet fuel composition from a feedstock comprising a natural oil. The methods comprise reacting the feedstock with oxygen under conditions sufficient to form an oxygen-cleaved product. The methods furth...
|
WO/2010/060281A1 |
A metal loaded catalyst comprises a support and main active metal components and optional auxiliary active metal components, wherein the main active metal components are elementary substances and obtained by ionizing radiation reducing p...
|
WO/2010/056154A1 |
The present matter relates to the petroleum industry and, specifically, to the processes of converting heavy petroleum products (HPR) into fuel distillates by thermal catalytic cracking. The process comprises mixing of HPR with solvent-r...
|
WO/2010/056153A1 |
The present matter relates to the petroleum industry and, more particularly, to a process of converting the heavy petroleum residues into fuel distillates by thermal cracking with use of the donor solvent processes.
|
WO/2010/053896A2 |
A method of producing a hydrocarbon product by hydrotreating a feedstock comprising triacylglyceride (TAG) in the presence of a nonsulfided hydrotreating catalyst to produce a first product comprising hydrocarbons. A method of producing ...
|
WO/2010/046562A2 |
The invention relates to a method for preparing synthetic crude oil from a heavy crude oil field, said method including: (a) extracting the heavy crude oil using a steam technology; (b) separating the extracted crude oil from the water; ...
|
WO/2010/046590A2 |
The invention relates to a process comprising the steps consisting in: - carrying out a hydrotreatment or a hydrocracking operated under a pressure of 20 to 120 bar and at a temperature between 250 and 500°C, preferably between 350 and ...
|
WO/2010/039776A2 |
This invention is directed to a synthesis process for preparing magnesium aluminosilicate clays and to the products of said process. Briefly, a silicon component, an aluminum component, and a magnesium component are combined, under aqueo...
|