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WO/2008/017953A2 |
An apparatus for cracking organic substances, for making a mixture of solid and/or liquid and/or gaseous components. The device comprises a cracking chamber (5) with substantially tubular walls arranged between an inlet port (β) of said...
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WO/2008/017741A1 |
Method of producing liquid hydrocarbons from a heavy charge such as biomass, coal, lignite, or heavy petroleum residue comprising: - partial oxidation b) of the heavy charge, producing a synthetic gas SG1, with H2/CO ratio of < 1; - stea...
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WO/2008/014854A1 |
The present invention relates to a method for reprocessing the combustion products carbon dioxide and water into renewable synthetic- heating fuel and fuel for vehicles with the help of electrical energy, according to the invention by me...
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WO/2008/008076A1 |
A method for transforming at least a part of the catalyst precursor hematite into χ- carbide (Fe5C2) and ε'-carbide (FeC2-2) without a large amount of fines generation. This method slows the transformation of the hematite to iron carbi...
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WO/2008/006786A2 |
A method of supporting a hydrocarbon synthesis catalyst material comprising a catalytically active metal and a carrier material on a substrate comprising the steps of: (a) applying the catalyst material to the substrate; and (b) heating ...
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WO/2008/003731A1 |
A process for the preparation of a catalyst or catalyst precursor for use in a reactor, comprising the steps of: (a) admixing: (i) a catalytically active component or precursor therefor; (ii) one or more carrier materials; (iii) particle...
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WO/2008/000784A1 |
A method for the optimisation of a multi-stage Fischer-Tropsch process producing hydrocarbons from synthesis gas, which method comprises the steps of: (i) providing synthesis gas comprising in the range of from 1 to 7 vol% inerts, prefer...
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WO/2007/131082A2 |
An optimized Fischer-Tropsch process utilizing a diluted synthesis gas and one or more Fischer-Tropsch reactors having an overall CO conversion of at least 90%.
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WO/2007/125360A1 |
A process for converting methane to higher molecular weight hydrocarbons comprises (A) reforming (1) methane by catalytic reaction with steam at elevated temperature to generate carbon monoxide and hydrogen; (B) subjecting the mixture of...
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WO/2007/122498A2 |
This invention relates to a method of producing liquid hydrocarbons, preferably internal combustion engine fuels, using feedstocks of coal or methane. Depending on the nature of the feedstock it is subjected to a gasification and/or refo...
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WO/2007/122315A1 |
The present invention describes a new type of internal exchanger for a reactor intended to bring about the Fischer-Tropsch synthesis. Said exchanger is of modular design and includes a central tube with separations enabling both the modu...
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WO/2007/119455A1 |
Disclosed is a process for hydrorefining a fuel base material wherein a fuel base material containing an oxygen-containing compound, an olefin and a normal paraffin is brought into contact with a hydrorefining catalyst, which is composed...
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WO/2007/119474A1 |
Disclosed is a process for production of a hydrocarbon, which can reduce the content of a water-insoluble oxygen-containing hydrocarbon in a hydrocarbon oil. An alcohol having 4 or less carbon atoms is injected into a reaction product pr...
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WO/2007/119587A1 |
Disclosed is a liquid fuel synthesis system (1) comprising: a first reformer (12) for reforming a hydrocarbon raw material to produce a synthetic gas comprising mainly a carbon monoxide gas and a hydrogen gas; a bubble column reactor (30...
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WO/2007/114027A1 |
An unleaded gasoline composition in which an FT synthesized base material of low octane number can be used as a gasoline base material. There is provided an unleaded gasoline composition characterized by containing the whole or part of f...
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WO/2007/114250A1 |
A liquid fuel synthesis system (1) comprises: a reformer (12) for reforming a hydrocarbon raw material to produce a synthetic gas composed mainly of a carbon monoxide gas and a hydrogen gas; a bubble column reactor (30) for synthesizing ...
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WO/2007/114274A1 |
Disclosed is a liquid fuel synthesis system (1) comprising: a reformer (12) for reforming a hydrocarbon raw material to produce a synthetic gas comprising mainly a carbon monoxide gas and a hydrogen gas; a bubble column reactor (30) for ...
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WO/2007/114276A1 |
Disclosed is a liquid fuel synthesis system which comprises: a reformer (12) for reforming a hydrocarbon raw material to produce a synthetic gas composed mainly of a carbon monoxide gas and a hydrogen gas; a bubble column reactor (30) fo...
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WO/2007/114277A1 |
Disclosed is a liquid fuel synthesis system (1) which comprises: a reformer (12) for reforming a hydrocarbon raw material to produce a synthetic gas composed mainly of a carbon monoxide gas and a hydrogen gas; a bubble column-type reacto...
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WO/2007/114271A1 |
Bubble tower type hydrocarbon synthesis reactor (100) comprising reactor main frame (110) accommodating slurry (120) having solid catalyst particles (124) suspended in liquid hydrocarbon (122), and distributor (140) disposed at an inferi...
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WO/2007/114279A1 |
Disclosed is a liquid fuel synthesis system (1) which comprises: a reformer (12) for reforming a hydrocarbon raw material to produce a synthetic gas composed mainly of a carbon monoxide gas and a hydrogen gas; a waste heat boiler (14) fo...
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WO/2007/114025A1 |
This invention provides a gas oil composition for use in superchargers having a geometric compression ratio of not more than 16 and diesel engines with EGR. The gas oil composition is an FT synthetic base material-containing gas oil comp...
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WO/2007/113965A1 |
A process for producing middle distillate useful as a fuel base efficiently at a high conversion of carbon monoxide and a high chain propagation probability (α), namely, a process for producing hydrocarbons by conducting the reduction o...
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WO/2007/114028A1 |
This invention provides a gas oil composition for use in superchargers having a geometric compression ratio of more than 16 and diesel engines with EGR. The gas oil composition is an FT synthetic base material-containing gas oil composit...
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WO/2007/111152A1 |
A fuel composition for the winter season which has all of excellent low-temperature flowability, mileage performance, and environmental preservation performance. The fuel composition is obtained by subjecting a hydrocarbon mixture having...
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WO/2007/112314A2 |
A low-temperature catalytic process for converting biomass (preferably glycerol recovered from the fabrication of bio-diesel) to synthesis gas (i.e., H2/CO gas mixture) in an endothermic gasification reaction is described. The synthesis ...
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WO/2007/108196A1 |
A fuel composition for combustors which is reduced in the odor of the composition itself and thereby lowered in the uncomfortableness in handling such as oil feeding, characterized by an aromatic content of 7% by volume or below, an olef...
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WO/2007/108014A1 |
A process for producing high octane fuel from carbon dioxide and water is disclosed. The feedstock for the production line is industrial carbon dioxide and water, which may be of lower quality. Water is electrolysed into hydrogen and oxy...
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WO/2007/106775A1 |
The invention relates to a method of removing contaminants from a hydroprocessing feed stream. More specifically, the invention relates to a method of removing contaminants from a hydroprocessing feed stream which originates in a Fischer...
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WO/2007/103677A2 |
The invention provides a catalytic distillation system which combines two fundamental unit operations, chemical reaction and distillation in a single piece of equipment for hydrocracking and hydrotreating of Fischer-Tropsch liquids.
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WO/2007/101831A1 |
Process to prepare a Fischer-Tropsch synthesis product from a gaseous mixture of hydrocarbons comprising methane, ethane and optional higher carbon number hydrocarbons by performing the following steps (a) pre-reforming the hydrocarbon m...
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WO/2007/092733A1 |
The invention provides a process for desalting crude by combining water and raw crude oil in a mixer to produce a mixture. Desalted crude oil and a brine mixture are separated from the mixture. The water is obtained as a byproduct of a F...
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WO/2007/086612A1 |
A bubble column type hydrocarbon synthesis reactor synthesizes a hydrocarbons by a chemical reaction of a gas the main components of which are hydrogen and carbon monoxide, and a slurry having solid catalyst particles suspended in a liqu...
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WO/2007/086610A1 |
The bubble column type hydrocarbon synthesis reactor synthesizes hydrocarbons by a chemical reaction of a gas whose main components are hydrocarbon and carbon monoxide, and a slurry having solid catalyst particles suspended in a liquid, ...
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WO/2007/080247A1 |
The present invention describes a device allowing secondary filtration of catalyst particles contained in a process effluent comprising a reactor operated in three-phase mode.
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WO/2007/077139A2 |
A process for enhanced oil recovery in combination with the production of hydrocarbons from synthesis gas, the process comprising injecting a gaseous mixture comprising carbon dioxide into a subsurface reservoir to enhance the recovery o...
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WO/2007/077138A1 |
A process for the sequestration of carbon dioxide, the process comprising injecting a carbon dioxide containing stream into a subsurface formation, wherein the carbon dioxide containing stream has been obtained from a gaseous mixture by ...
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WO/2007/077137A1 |
The process comprises the step of injecting a gaseous mixture comprising carbon dioxide into a subsurface reservoir to enhance the recovery of hydrocarbons from the reservoir, wherein the carbon dioxide content in the gaseous mixture has...
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WO/2007/079031A1 |
A method for separating and filtering solid particles from a hydrocarbon slurry liquid includes two or more filter sections in fluid communication with the hydrocarbon slurry. At least one filter section is comprised of one or more filte...
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WO/2007/077139A1 |
A process for enhanced oil recovery in combination with the production of hydrocarbons from synthesis gas, the process comprising injecting a gaseous mixture comprising carbon dioxide into a subsurface reservoir to enhance the recovery o...
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WO/2007/074127A1 |
Process to make a sulphur containing hydrocarbon product from crude natural gas by performing the following steps: (a) separating a sulphur containing liquid field condensate fraction from the natural gas, (b) further separating a sulphu...
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WO/2007/071903A1 |
A process for producing at least one condensed-phase product from one or more gas- phase reactants in the presence of a solid catalyst having one or more catalyst components, wherein the solid catalyst has two or more regions in which th...
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WO/2007/068732A1 |
The invention relates to a catalyst body comprising a Fischer-Tropsch catalyst or catalyst precursor and a porous body, said porous body being between 1-50 mm, preferably 1-30 mm in size, the catalyst body having an internal voidage betw...
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WO/2007/069197A2 |
A process (10) for producing hydrocarbons from natural gas includes, in a cryogenic separation stage (16), cryogenically separating the natural gas to produce at least a methane stream and natural gas liquids, in a reforming stage (20), ...
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WO/2007/069317A1 |
A Fischer-Tropsch (FT) synthesis system, characterized in that the FT synthesis process of bringing synthesis gas continuously fed from the bottom of a bubble column type slurry-bed reactor into contact with suspended catalyst particles ...
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WO/2007/068682A1 |
A process for the sequestration of carbon dioxide, the process comprising injecting carbon dioxide into a reservoir, the carbon dioxide derived from flue gas from a reformer, particularly from a steam methane reformer (SMR). The injected...
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WO/2007/065902A1 |
The present invention provides a method to start a steady state process for producing normally gaseous, normally liquid and optionally normally solid hydrocarbons from synthesis gas, which method comprises the steps of: (i) providing an ...
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WO/2007/065904A1 |
Method to start a steady state process for producing normally gaseous, normally liquid and optionally normally solid hydrocarbons from synthesis gas, which process comprises the steps of: (i) providing the synthesis gas; (ii) catalytical...
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WO/2007/065905A1 |
Method to start a steady state process for producing normally gaseous, normally liquid and optionally normally solid hydrocarbons from synthesis gas, which process comprises the steps of : (i) providing the synthesis gas; and (ii) cataly...
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WO/2007/060186A1 |
Method for synthesis of olefins from synthesis gas in the presence of at least one Fischer-Tropsch catalyst in a reaction column, wherein the synthesis gas is introduced into the reaction column below a zone A of the reaction column and ...
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