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WO/2010/075222A2 |
In the present invention, a fuel composition and a process for making the same are disclosed. Specifically, in the present invention, triglycerides useful for distillate fuels are described along with their method for preparation from Fi...
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WO/2010/071989A1 |
A Fischer-Tϊopsch process for producing diesel fuel or diesel blending stock with a high cetane number, in a concentration of 65-90wt% at pressures below 200 psia, using a cobalt catalyst with a rhenium and/or ruthenium promoter. The ca...
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WO/2010/074762A1 |
The present invention provides methods and means for separating slurry liquid from catalyst in a three-phase slurry process. The embodiments of the invention are characterized by conducting the three-phase process under conditions to pro...
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WO/2010/075516A2 |
A method for forming a catalyst for synthesis gas conversion comprises impregnating a zeolite extrudate using a solution, for example, a substantially non-aqueous solution, comprising a cobalt salt to provide an impregnated zeolite extru...
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WO/2010/069978A1 |
A process for regenerating one or more deactivated cobalt comprising Fischer-Tropsch catalyst particle (s) in situ in a reactor tube, said process comprising the steps of : (i) oxidising the catalyst particle(s) at a temperature between ...
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WO/2010/069925A1 |
The present invention pertains to a process for carrying out a high-speed stop in a Fischer-Tropsch process which comprises providing a feed to a fixed bed reactor comprising a Fischer-Tropsch catalyst, the reactor being at reaction temp...
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WO/2010/069927A1 |
The present invention pertains to a Process for carrying out a high-speed stop in a Fischer-Tropsch process which comprises providing a feed comprising CO and H2 to the inlet section of a fixed bed reactor comprising a Fischer-Tropsch ca...
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WO/2010/069486A2 |
The present invention relates to a multi-stage adiabatic method for performing the Fischer-Tropsch synthesis at low temperatures, wherein the synthesis is performed in 5 to 40 sequentially connected reaction zones under adiabatic conditi...
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WO/2010/070475A1 |
A process for regenerating a spent particulate wax-containing cobalt-based Fischer-Tropsch synthesis catalyst is provided. The process includes subjecting the spent wax-containing catalyst sequentially to a dewaxing treatment, an oxidati...
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WO/2010/068364A2 |
A process is described for converting synthesis gas containing carbon monoxide and hydrogen to hydrocarbons via methanol as an intermediate, by contacting the synthesis gas with a catalyst system containing a mixture of gallium silicate ...
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WO/2010/066386A1 |
The present invention relates to a hydrocarbon synthesis catalyst comprising in its unreduced form a) Fe as catalytically active metal, b) an alkali metal and/or alkaline-earth metal in an alkali metal- and/or alkaline-earth metal-contai...
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WO/2010/067077A1 |
The present invention relates to an integrated synthesis gas refinery plant and a process for the simultaneous production from a single synthesis gas stream X of a hydrogen stream useful for the production of ammonia, a hydrogen rich syn...
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WO/2010/063850A1 |
Process for carrying out a high-speed stop in a Fischer-Tropsch process which comprises providing a feed comprising CO and H2 to a fixed bed reactor comprising a Fischer-Tropsch catalyst, the reactor being at reaction temperature and pre...
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WO/2010/065132A1 |
A method and system for collecting a plurality of slurries containing solid particles of varying particle size distribution and amount and performing a classification and separation on the slurries is provided whereby a fines-rich stream...
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WO/2010/061623A1 |
Provided is a method for producing a catalyst for hydrocarbon production wherein a hydrocarbon is produced from a mixed gas comprising carbon monoxide and hydrogen. By means of the method for producing a catalyst for hydrocarbon product...
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WO/2010/058164A1 |
A slurry bubble column reactor (11) with a gas distribution arrangement comprising an upper sparger (12), a lower sparger (13) and an open-ended tube (14). Gas from the lower sparger (13) enters the tube (14) and lowers the density of sl...
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WO/2010/056692A2 |
A method of producing synthesis gas via gasification in a Fischer-Tropsch plant, the method including providing a number of gasifiers, the number of gasifiers provided being at least one more than the base number required to provide 100%...
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WO/2010/057222A2 |
An integrated CTL/IGCC facility that is more efficient than separate conventional CTL and IGCC processes, and can readily be designed for ultra-low emissions, and yet is economical to construct. For an incremental increase in cost and fu...
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WO/2010/049715A1 |
A catalyst precursor is described comprising 5 to 50 % by weight of one or more oxidic cobalt compounds selected from CoO, CoO(OH) and Co3O4 and 0.05 to 10 % by weight of one or more reduction promoter selected from metals or compounds o...
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WO/2010/049592A1 |
The invention relates to producing liquid hydro carbonaceous product (1) from solid biomass (2). In the invention solid biomass (2) is gasified in a gasifier (6) to produce raw synthesis gas (3). The raw synthesis gas (3) is conditioned ...
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WO/2010/049714A1 |
A catalyst suitable for the Fischer-Tropsch synthesis of hydrocarbons is described comprising cobalt nanocrystallites containing a precious metal promoter, dispersed over the surface of a porous transition alumina powder wherein the coba...
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WO/2010/038399A1 |
A hydrocarbon synthesis reactor in which a hydrocarbon compound is synthesized by the chemical reaction of synthesis gas comprising hydrogen and carbon monoxide as major components with a slurry obtained by suspending solid catalyst part...
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WO/2010/038395A1 |
A method for synthesizing a liquid fuel, which comprises a synthesizing step wherein a liquid fuel is synthesized by reacting, in a reactor, a synthesis gas mainly composed of a carbon monoxide gas and a hydrogen gas with a slurry which ...
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WO/2010/038392A1 |
A reactor comprising a reactor main body which holds therein a slurry obtained by suspending solid catalyst particles in a liquid. The reactor has, formed in a bottom part of the reactor main body, an inlet through which synthesis gas c...
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WO/2010/038400A1 |
A system for catalyst separation in which solid catalyst particles are separated from a hydrocarbon synthesized by the chemical reaction of synthesis gas comprising hydrogen and carbon monoxide as major components with a slurry obtained ...
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WO/2010/038391A1 |
A hydrocarbon synthesis reactor in which a hydrocarbon compound is synthesized by the chemical reaction of synthesis gas comprising hydrogen and carbon monoxide as major components with a slurry obtained by suspending solid catalyst part...
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WO/2010/038389A1 |
A method of starting up a rectifier for fractionating Fisher-Tropsch synthesis hydrocarbons produced by FT synthesis. The method comprises: a step in which light FT synthesis hydrocarbons present as a gas in an FT reactor where the Fish...
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WO/2010/038396A1 |
A unit for hydrocarbon synthesis reaction in which hydrocarbon compounds are synthesized by the chemical reaction of synthesis gas comprising hydrogen and carbon monoxide as major components with a slurry obtained by suspending a solid c...
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WO/2010/038394A1 |
A method of starting up a reactor for hydrotreating a naphtha fraction which has been fractionated with a rectifier from hydrocarbon compounds yielded by Fisher-Tropsch synthesis. The method comprises: a step in which a gas/liquid separ...
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WO/2010/025525A1 |
A method for producing hydrocarbons or oxygenates for use as a synthetic fuel source from suitable material, the method including: providing a feedstock stream comprising solid and/or liquid and/or gaseous material under pressure to a mi...
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WO/2010/021123A1 |
Provided are a gasification device, a fuel generation system, a gasification method, and a fuel generation method that have a simple and compact configuration overall and that can improve processing efficiency. The gasification device (1...
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WO/2010/015737A1 |
The invention relates to a process for producing middle distillates from a paraffinic feedstock produced by Fischer-Tropsch synthesis, using a hydrocracking/hydroisomerization catalyst that comprises at least one hydro-dehydrogenating me...
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WO/2010/011332A1 |
A method is provided for preparing a supported cobalt-containing catalyst having substantially homogenously dispersed, small cobalt crystallites. The method comprises depositing cobalt nitrate on a support and then heating the support in...
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WO/2010/007602A1 |
This invention relates to a process and apparatus for the production of hydrogen, oxygen and hydrocarbons from carbon dioxide and water. Carbon dioxide in the liquid phase with water in the liquid phase to provide and maintain a liquid e...
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WO/2009/157260A1 |
Disclosed are: a catalyst for FT synthesis, which has a high CO conversion rate, can reduce the production of a gaseous component, enables a stable FT synthesis reaction, and can improve the productivity of a hydrocarbon in FT method; an...
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WO/2009/154099A1 |
Disclosed is an FT synthesis catalyst which exhibits higher activity and high CO conversion rate in an FT process, thereby enabling a stable FT synthesis reaction. The FT synthesis catalyst can improve productivity of hydrocarbons. A m...
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WO/2009/152895A1 |
The invention relates to a method and a system for operating a Fischer-Tropsch synthesis, wherein a feed gas comprising CO and H2 from coal gasification (1) is desulfurized and subsequently fed into a Fischer-Tropsch synthesis as an inpu...
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WO/2009/154094A1 |
The objective is to provide a synthetic oil manufacturing apparatus and a synthetic oil manufacturing method that can manufacture synthetic oil by using Fischer‑Tropsch synthesis with which simplification, miniaturization, and easier o...
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WO/2009/152873A1 |
The present invention relates to an integrated process for producing diesel fuel or fuel additive from biological material by producing paraffins by a Fischer-Tropsch reaction on one hand and by a catalytic hydrodeoxygenation of bio oils...
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WO/2009/144411A2 |
The invention relates to a method for producing medium distillates from a paraffinic charge produced by Fischer-Tropsch synthesis, implementing a hydrocracking/hydroisomerization catalyst including: at least one substrate formed from at ...
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WO/2009/145807A1 |
A method of tracking production from an NG source that includes the steps of providing one or more micro-scale GTL units, feeding NG from the source to the micro-scale GTL units, operating the micro-scale GTL units and adjusting the numb...
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WO/2009/144412A2 |
The invention relates to a method for producing medium distillates from a paraffinic charge produced by Fischer-Tropsch synthesis, implementing a hydrocracking/hydroisomerization catalyst containing at least one hydro-dehydrogenating met...
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WO/2009/141375A2 |
Use of a Fischer-Tropsch derived fuel component in a fuel composition, to reduce the rate of accumulation of acidic components in a lubricant fluid present in an internal combustion engine which is running, or is intended to be run, on t...
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WO/2009/140317A1 |
The present invention provides a method for recovering a natural gas contaminated with high levels of carbon dioxide. A gas containing methane and carbon dioxide is extracted from a reservoir containing natural gas, where carbon dioxide ...
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WO/2009/129610A1 |
A process to efficiently convert organic feedstock material into liquid non-oxygenated hydrocarbons in the C5 to C12 carbon skeleton range is disclosed. The process can utilize gaseous, liquid or solid organic feedstocks containing carbo...
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WO/2009/127990A1 |
A process for preparing a cobalt based Fischer-Tropsch synthesis catalyst precursor includes introducing a multi-functional carboxylic acid having the general formula (1 ) HOOC -C*R1C*R2- COOH (1 ) or a precursor thereof, where C* in eac...
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WO/2009/128865A1 |
A mobile system for providing start-up electrical power to a micro scale liquid hydrocarbon and/or oxygenate synthesis plant is provided including a portable gas or liquid fueled electrical generator, a steam turbine, a plant generator m...
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WO/2009/123095A1 |
Disclosed is a method for operating a synthesis gas reformer in a GTL plant. In the method, operation conditions for the synthesis gas reformer are set, and flow rate control target values respectively for a light hydrocarbon gas, steam,...
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WO/2009/123247A1 |
In a so-called GTL process comprising producing synthesis gas from natural gas, producing a Fischer-Tropsch oil from the resultant synthesis gas by Fischer-Tropsch synthesis, and upgrading the oil to produce liquid hydrocarbons containin...
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WO/2009/114416A1 |
A process for producing an API Group I base oil, comprising: blending a lower quality base oil that does not meet API Group I specifications with a Fischer-Tropsch derived distillate fraction having defined pour point, viscosity index an...
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