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WO/2013/166235A2 |
A gasoline blending components production system useful for producing both aromatics and gasoline blending components from naphtha. The production system includes a light hydrocracked naphtha splitter, a medium hydrocracked naphtha split...
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WO/2013/160253A1 |
A process for converting a solid biomass material, comprising contacting the solid biomass material and a hydrocarbon co-feed with a catalytic cracking catalyst at a temperature of more than 400°C in a riser reactor to produce one or mo...
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WO/2013/153287A1 |
The invention relates to a method of deoxygenation of tall oil as well as methods for the production of aliphatic hydrocarbons and polymerizable monomers from tall oil. Sulphurous crude tall oil (5) together with hydrogen gas (6) is fed ...
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WO/2013/149365A1 |
The present invention relates to a method for producing a gasoline blended component with a high octane number, comprising: raw materials of mixed C4-C8 alkane and C4 alkene entering an isomerization reaction device, and conducting an is...
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WO/2013/148194A1 |
A process and apparatus are disclosed for hydrotreating a hydrocarbon feed in a hydrotreating unit and hydrocracking a second hydrocarbon stream in a hydrocracking unit. The hydrocracking unit and the hydrotreating unit may share the sam...
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WO/2013/148907A1 |
Feeds containing triglycerides are processed to produce an olefinic diesel fuel product. The olefinic diesel can optionally be oiigomerized to form a lubricant base oil product. The olefinic diesel is generated by deoxygenating the trigl...
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WO/2013/148906A1 |
Feeds containing triglycerides are processed to produce an olefinic diesel fuel product and propyiene. The olefinic diesel can optionally be oligomerized to form a lubricant base oil product. The olefinic diesel and propylene are generat...
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WO/2013/141978A1 |
A method for producing a linear paraffin product from natural oil and kerosene includes providing a first feed stream comprising kerosene, pre-fractionating the first feed stream to produce a heart cut paraffin stream comprising paraffin...
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WO/2013/142609A1 |
An integrated hydrotreating, steam pyrolysis and catalytic cracking process for the production of olefins and aromatic petrochemicals from a crude oil feedstock is provided. Crude oil and hydrogen are charged to a hydroprocessing zone un...
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WO/2013/142620A1 |
An integrated slurry hydroprocessing and steam pyrolosyis process for the production of olefins and aromatic petrochemicals from a crude oil feedstock is provided. Crude oil, a steam pyrolysis residual liquid fraction and slurry reside a...
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WO/2013/142617A1 |
Crude oil is charged to a hydroprocessing zone in the presence of hydrogen operating under conditions effective to produce a hydroprocessed effluent, which is thermally cracked in the presence of steam in a steam pyrolysis zone to produc...
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WO/2013/142605A1 |
An integrated hydrotreating, steam pyrolysis and coker process for the direct processing of a crude oil is provided to produce olefinic and aromatic petrochemicals, and petroleum coke. Crude oil and recycled coker liquid product are char...
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WO/2013/138001A1 |
One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon ...
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WO/2013/112967A1 |
A process is provided that is directed to a steam pyrolysis zone integrated with a solvent deasphalting zone and a hydrotreating zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aro...
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WO/2013/112968A1 |
A process is provided that is directed to a steam pyrolysis zone integrated with a hydrotreating zone and a solvent deasphalting zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aro...
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WO/2013/112969A2 |
A process is provided that is directed to a steam pyrolysis zone integrated with a hydroprocessing zone including hydrogen redistribution to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and...
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WO/2013/112970A1 |
A process is provided that is directed to a steam pyrolysis zone integrated with a hydroprocessing zone including residual bypass to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromati...
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WO/2013/112965A1 |
An integrated hydrotreating and steam pyrolysis process for the direct processing of a crude oil is provided to produce olefinic and aromatic petrochemicals. Crude oil and hydrogen are charged to a hydroprocessing zone operating under co...
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WO/2013/104614A1 |
The invention relates to a method for the treatment of an olefin containing hydrocarbon feedstock (110), wherein said feedstock (110) successively undergoes the following steps: (i) selective catalytic hydrogenation, (ii) a fractionation...
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WO/2013/098523A1 |
The invention relates to a method for producing an aromatic petroleum fraction comprising at least 95% by weight of benzene (31), from at least one naphtha fraction (2) comprising paraffins, aromatic compounds and precursors of said arom...
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WO/2013/093227A1 |
The present invention describes an improved process for converting a heavy feedstock that makes it possible to improve the selectivity for middle distillates. The invention consists in the implementation of a hydrotreatment or hydroconve...
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WO/2013/096066A1 |
This invention relates to methods and processes for increasing the production of FCC (Fluid Catalytic Cracking) gasoline products, and optionally distillate products, from refinery feedstocks. In particular, the processes include hydrotr...
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WO/2013/095815A1 |
A reforming process includes an endpoint reduction zone for converting C11+ components via selective hydrogenation and hydrodealkylation to lower boiling point aromatics, such as benzene, toluene, and xylene, or their single ring aromati...
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WO/2013/093299A1 |
A method for optimising the production of middle distillate within a refinery comprising at least one catalytic cracking unit (3) and at least one vacuum distillation unit (2, 4), the optimising operation consisting: a) of recycling (14)...
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WO/2013/089856A1 |
A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will...
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WO/2013/089857A1 |
A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will...
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WO/2013/089854A1 |
A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and partially processing each feedstream in separate reactors. The processing includes passing the...
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WO/2013/089849A1 |
A process for the production of aromatics through the reforming of a hydrocarbon stream is presented. The process utilizes the differences in properties of components within the hydrocarbon stream to increase the energy efficiency. The d...
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WO/2013/066660A2 |
This invention provides methods for multi-stage hydroprocessing treatment of FCC naphthas for improving the overall production quantity of naphtha boiling-range materials during naphtha production for low sulfur gasolines. Of particular ...
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WO/2013/057389A1 |
A method of converting petroleum feedstocks for the production of fuels with a low sulphur content comprising the following steps; a step of ebullated-bed hydroconversion of the feedstock in the presence of a supported catalyst, a separa...
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WO/2013/052228A1 |
A process for maximizing p-xylene production begins by producing a naphtha fraction and a light cycle oil fraction from a fluid catalytic cracking zone. The gasoline and light cycle oil fractions are combined and hydrotreated to produce ...
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WO/2013/052233A1 |
A reforming process includes integrating catalytic cracking product naphtha dehydrogenation and naphtha from a hydrocracking zone and feeding them to a dehydrogenation zone. The dehydrogenation zone includes a first portion of reforming ...
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WO/2013/052232A1 |
A process for maximizing p-xylene production includes producing a naphtha fraction and a light cycle oil fraction from a fluid catalytic cracking zone. These fractions are combined and hydrotreated. Fractionation of the hydrotreated prod...
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WO/2013/043294A1 |
Embodiments of methods for co-production of linear alkylbenzene and biofuel from a natural oil are provided. A method comprises the step of deoxygenating the natural oils to form paraffins. A first portion of the paraffins is hydrocracke...
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WO/2013/033582A1 |
The invention relates to processes for upgrading products obtained from hydrocarbon pyrolysis, equipment useful for such processes, and the use of upgraded pyrolysis products. A tar-containing stream recovered from the pyrolysis effluent...
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WO/2013/033590A2 |
The invention relates to processes for upgrading products obtained from hydrocarbon pyrolysis, equipment useful for such processes, and the use of upgraded pyrolysis products.
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WO/2013/033577A1 |
The invention relates to upgraded pyrolysis products, processes for upgrading products obtained from hydrocarbon pyrolysis, equipment useful for such processes, and the use of upgraded pyrolysis products. A tar-containing stream recovere...
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WO/2013/028379A2 |
A process and apparatus are disclosed for recovering hydroprocessing effluent from a hydroprocessing unit utilizing a hot stripper and a cold stripper. Only the hot hydroprocessing effluent is heated in a fired heater prior to product fr...
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WO/2013/019585A2 |
Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by flashing the feed at a target cut point t...
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WO/2013/019587A2 |
Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by hydrotreating the feed under mild conditi...
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WO/2013/019586A2 |
Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by first subjecting the entire feed to an ex...
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WO/2013/019512A1 |
An integrated process and system for conversion of a heavy crude oil to produce transportation fuels is provided. The process includes separating the hydrocarbon feed into an aromatic-lean fraction and an aromatic-rich fraction. The arom...
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WO/2012/177180A1 |
The present invention relates to the field of petroleum processing and can be used in the production of a low-sulfur diesel fuel. The method comprises removing the salts from and distilling the petroleum, recovering diesel fractions, mix...
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WO/2012/174860A1 |
A device for the low-cost production of low-sulphur, high-octane gasoline, comprising an extraction device (1), a first splitting tower (2), an etherification device (3), a hydrodesulphurization device (4), a reforming preprocessing devi...
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WO/2012/170153A2 |
The present invention is directed to methods for processing fatty acids to provide for base oil and transportation fuels, wherein decarboxylation-coupling dimerization of fatty acids provides dimer ketones from which the base oils and tr...
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WO/2012/170082A1 |
A process for the production of high yields of high quality products from heavy hydrocarbonaceous feedstock comprising a two-stage, close-coupled process, wherein the first stage comprises a thermal-catalytic zone into which is introduce...
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WO/2012/161263A1 |
This method for producing xylene involves producing xylene from an oil feedstock, which has a 10% distillation temperature of at least 135°C and a 90% distillation temperature of not more than 380°C, and comprises: a decomposition refo...
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WO/2012/161264A1 |
This method for producing monocyclic aromatic hydrocarbons involves producing monocylic aromatic hydrocarbons with 6 to 8 carbon atoms, and comprises: a decomposition reforming reaction step in which oil feedstock is brought into contact...
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WO/2012/153011A2 |
The invention relates to a method for the production of a diesel and middle distillate cut from an olefin feed having between 4 and 6 carbon atoms, said method including a first purification step performed on a resin, followed by an olig...
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WO/2012/153010A2 |
The invention relates to a method for the production of a diesel and middle distillate cut from an olefin feed having between 4 and 6 carbon atoms, said method including: a first purification step performed on a trapping mass formed by a...
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