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WO/2021/030003A1 |
Methods for assessing the potential for converting lubricating oil, for example, used lubricating oil, by catalytic cracking include subjecting a potential catalytic cracking feedstock to a plurality of tests to generate a plurality of m...
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WO/2021/023700A1 |
The present invention provides a microcrystalline wax having a needle penetration according to ASTM D-1321 at 25°C of more than 1, a crystallinity according to XRD between 5 and 70%, an initial boiling point of less than 500°C, a conge...
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WO/2021/023172A1 |
The present invention relates to a full conversion method and device for producing light aromatic hydrocarbons from a catalytic diesel. The technical solution of the present invention comprises: subjecting a catalytic diesel material flo...
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WO/2021/024014A1 |
The present invention relates to a process and a reactor for carrying out the process for reducing the benzene content of a reformate refinery stream. The process according to the present invention for reducing the benzene content of a l...
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WO/2021/018600A1 |
Disclosed is a catalyst nickel, copper and an alumina support, said catalyst being characterized in that: - the nickel is distributed both in a shell at the periphery of the support and in the core of the support, the thickness of the sh...
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WO/2021/019344A1 |
Systems and methods for processing full range naphtha feeds to produce a light olefins stream and an aromatics stream concerns integration of catalytic cracking with steam cracking to maximize production of aromatics and olefins.
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WO/2021/018603A1 |
Disclosed is a catalyst comprising nickel and sulfur on an alumina support, said catalyst being characterized in that: - the nickel is distributed both in a shell at the periphery of the support and in the core of the support, the thickn...
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WO/2021/019343A1 |
Systems and methods for producing light olefins and BTX (benzene, toluene, and xylene). Crude oil is first separated to produce light naphtha and heavy naphtha. Light naphtha is fed to a steam cracking unit and heavy naphtha is fed to a ...
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WO/2021/018604A1 |
Disclosed is a catalyst comprising a nickel-based active phase and an alumina support, characterized in that: - the nickel is distributed both in a shell at the periphery of the support and in the core of the support, the thickness of sa...
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WO/2021/013527A1 |
The present invention concerns a method for processing a petrol containing sulfur and olefin compounds, comprising the following steps: a) a step of hydrodesulfurisation in the presence of a catalyst comprising an oxide support and an ac...
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WO/2021/013525A1 |
The present invention relates to a process for desulphurising a gasoline, comprising at least the following steps: a) fractionating the gasoline so as to recover a light gasoline cut LCN and a first heavy gasoline cut HCN, b) carrying ou...
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WO/2021/013528A1 |
The present application relates to a method for treating a gasoline containing sulfur-containing compounds and olefins, comprising the following steps: a) a step of hydrodesulfurization in the presence of a catalyst comprising an oxide s...
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WO/2021/016253A1 |
A system for processing a stream including fuel oil includes an atmospheric flash column for receiving the stream as feedstock and separate the stream into an atmospheric flash distillate stream and an atmospheric flash residue stream. T...
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WO/2021/013526A1 |
The present application relates to a method for treating a petrol containing sulphur compounds, olefins and diolefins, the method comprising the following steps: a) a step of hydrodesulphurisation in the presence of a catalyst comprising...
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WO/2021/009666A1 |
A system and method for processing pyrolysis gasoline is disclosed. The system and method involves separating a pyrolysis gasoline stream to produce a first stream comprising primarily un-hydrogenated C9+ compounds. The separating of the...
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WO/2021/008924A1 |
The present invention relates to a process for the preparation of olefins from a hydrocarbon feedstock (1) having a sulphur content of at least 0.1 wt.%, an initial boiling temperature of at least 180 °C and a final boiling temperature ...
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WO/2021/001474A1 |
A method for in-situ sulfidation of a hydroconversion catalyst, is provided, in which inactive hydroconversion catalyst is combined with a liquid hydrocarbon prior to sulfidation. Methods for hydroconversion of a liquid hydrocarbon feeds...
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WO/2021/002886A1 |
A method of making a multifunctional catalyst for upgrading pyrolysis oil includes contacting a zeolite support with a solution including at least a first metal catalyst precursor and a second metal catalyst precursor, the first metal ca...
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WO/2021/002889A1 |
A method of making a multifunctional catalyst for upgrading pyrolysis oil includes contacting a hierarchical mesoporous zeolite support with a solution including at least a first metal catalyst precursor and a second metal catalyst precu...
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WO/2020/262989A1 |
The present invention relates to a nickel-based catalyst for hydrogenation and a method for preparing same and, more specifically, provides a catalyst having improved activity by including copper or copper oxide as a cocatalyst when a hy...
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WO/2020/262078A1 |
Provided are a heavy oil hydrogenation processing catalyst combination demonstrating higher performance than prior art catalyst systems and a heavy oil processing method. This heavy oil hydrogenation processing method involves a demetall...
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WO/2020/263854A1 |
A desolidification process enables the isolation and extraction of solid additives from an unreacted petroleum residue stream. In a hydrocracking process that mixes a solid additive with a petroleum residue feedstock to convert the petro...
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WO/2020/262987A1 |
The present invention relates to a nickel catalyst for a hydrogenation reaction and a manufacturing method therefor, and relates to a nickel catalyst added in a hydrogenation reaction for improving the color of a petroleum resin. The cat...
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WO/2020/262985A1 |
The present invention relates to a catalyst for a hydrogenation reaction and a method for producing same and, more specifically, to a catalyst for a hydrogenation reaction, wherein the catalyst comprises nickel oxide as an active materia...
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WO/2020/262986A1 |
According to the present invention, when preparing a hydrogenation catalyst containing nickel as an active material, the reduction of nickel may be facilitated by using copper and sulfur as accelerators. In particular, the present invent...
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WO/2020/263545A1 |
A method for operating an acetylene hydrogenation unit in an integrated steam cracking-fluidized catalytic dehydrogenation (FCDh) system may include separating a cracked gas from a steam cracking system and an FCDh effluent from an FCDh ...
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WO/2020/264145A1 |
Increased paraxylene production through the use of a split feed reforming process, wherein hydrotreated naphtha is split into light, middle and heavy fractions. Each fraction is reformed separately to generate streams containing aromatic...
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WO/2020/254634A1 |
A broad aspect of the present disclosure relates to a process for conversion of a hydro- carbonaceous feed comprising at least 20 ppmw, 100 ppmw or 500 ppmw and less than 1000 ppmw, 5000 ppmw or 10000 ppmw halides, to a hydrocarbon produ...
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WO/2020/254629A1 |
The present disclosure relates to a process plant and process for conversion of a hy- drocarbonaceous feed, having a feed temperature, to a hydrocarbonaceous effluent, having an effluent temperature, by hydrotreatment, in the presence of...
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WO/2020/229892A1 |
A system and method for producing high-purity hexane that uses a deisohexanizer with a dividing wall within the separation section following the isomerization reactor section of an isomerization unit deisohexanizer column with a dividing...
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WO/2020/230630A1 |
[Problem to be Solved] To provide a catalyst having hydrotreatment (hydrogenation, desulfurization and denitrogenation) performance that is equal to or superior to the prior art, as a hydrotreating catalyst for hydrocarbon oils, and a hy...
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WO/2020/205850A1 |
Disclosed is a method for preparing a nanoparticle composition. The method includes hydrogenating a hydrocarbon oil comprising a hydrocarbon having a carbon-carbon multiple bond, to give a hydrogenated hydrocarbon oil. The method further...
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WO/2020/205210A1 |
Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the cmde to chemicals process very flexible in terms of crude. In embodiments herein, cmde is progressively...
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WO/2020/197952A1 |
An integrated process for maximizing recovery of hydrogen is provided. The process comprises: providing a hydrocarbonaceous feed comprising naphtha, and a hydrogen stream to a reforming zone, wherein the hydrogen stream is obtained from ...
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WO/2020/186633A1 |
Disclosed is a micro-interface enhanced reaction system, comprising: a reactor main body (1), which acts as a reaction chamber for the reaction of a gas-liquid, liquid-liquid, liquid-liquid-solid, liquid-solid or gas-liquid-solid multiph...
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WO/2020/190786A1 |
Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery' altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressiv...
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WO/2020/186640A1 |
A micro-interface reinforced lubricating oil hydrofining reaction system and method, comprising: a liquid feed unit (1), a gas feed unit (2), a micro-interface generator (3), a fixed bed reactor (4), and a separation tank (5). Microbubbl...
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WO/2020/186638A1 |
A heavy oil hydrogenation and micro-interface strengthened suspension bed reaction system, comprising: a liquid phase feeding unit (1), a gas phase feeding unit (2), a micro-interface reactor (3), a suspension bed reactor (4), and a sepa...
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WO/2020/186635A1 |
Disclosed is an enhanced emulsion reaction system on an oil-coal co-hydrogenation micro-interface, comprising: an emulsion reactor (1), used as a reaction chamber in oil-coal co-hydrogenation reaction process; a micro-interface generator...
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WO/2020/186639A1 |
A micro-interface enhanced diesel hydrorefining reaction system and method, the system comprising: a liquid feeding unit (1), a gas feeding unit (2), a micro-interface generator (3), a fixed bed reactor (4) and a separating tank (5). Gas...
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WO/2020/186637A1 |
A micro-interface strengthening fluidized bed hydrogenation system, comprising: a liquid phase feed unit (1), a gas phase feed unit (2), a micro-interface generator (3), a fluidized bed reactor (4), and a separation tank (5).
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WO/2020/186641A1 |
The present invention relates to a micro-interface enhanced wax oil hydrogenation reaction system and method, comprising: a liquid-phase feed unit, a gas-phase feed unit, a micro-interface generator, a fixed-bed reactor, and a separation...
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WO/2020/186636A1 |
Disclosed is a micro-interface emulsification bed enhanced reaction system for the hydrogenation of coal tar, wherein the system comprises: an emulsification bed reactor (1), which acts as a reaction chamber in a coal tar hydrogenation r...
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WO/2020/186634A1 |
A micro-interface enhanced hydrogenation reaction system, comprising: a reactor main body (1), used as a reaction chamber during a hydrogenation reaction process; a micro-interface generator (2), connected to the reactor main body (1) an...
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WO/2020/190787A1 |
Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressive...
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WO/2020/186644A1 |
A downward fixed-bed enhanced reaction system with an oil hydrogenation micro interface, comprising a fixed-bed reactor (4) and a micro interface generator, wherein the micro-interface generator is arranged on the upper part of the fixed...
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WO/2020/190784A1 |
Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, erode is progressive...
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WO/2020/186642A1 |
A micro-interface strengthening reaction system and method for preparing a ship fuel by means of heavy oil hydrogenation, comprising: a liquid phase feeding unit (1), a gas phase feeding unit (2), a micro-interface reactor (3), a fixed b...
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WO/2020/128161A9 |
A process for selective removal of hydroxyl groups from phenolic compounds is disclosed. The process uses a combination of catalytic hydrodeoxygenation and catalytic direct deoxygenation to convert alkylphenols into alkylbenzenes.
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WO/2020/183302A1 |
A method of producing a fuel additive includes passing a feed stream comprising C4 hydrocarbons through a first hydrogenation unit producing a first process stream; passing the first process stream through a distillation unit; withdrawin...
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