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WO/2013/066029 |
This invention relates to a method of producing aromatic hydrocarbons and olefin from hydrocarbonaceous oils including large amounts of polycyclic aromatic compounds having two or more rings via partial hydrogenation in the presence of a...
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WO/2013/058997 |
The invention directed to a method of reducing the increase in viscosity and the drop in the heat transfer coefficient that commonly occurs with quenching media which is repeatedly circulated through a hot reaction vessel. The method com...
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WO/2013/055450 |
Methods and apparatuses for the isomerization and deisohexanizing of a feed are provided. In a method for the isomerization of a feed in an isomerization zone to form an isomerized stream and the deisohexanizing of the isomerized stream ...
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WO/2013/053740 |
The invention relates to a process for preparing jet fuel or jet fuel precursors which comprises the treatment of a charge derived from biomass, the said charge comprising at least one compound chosen from terpenes of formula [CH2=C(CH3)...
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WO/2013/052232 |
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/2013/052228 |
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/2013/043314 |
One exemplary embodiment can be a process for oligomerizing one or more hydrocarbons. The process can include oligomerizing a feed including one or more C3-C5 hydrocarbons to produce an effluent, and recycling at least a portion of the e...
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WO/2013/043287 |
The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing ...
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WO/2013/034677 |
The present invention provides aprocess for preparing ethylene and/or propylene, comprising the steps of a)contacting a stream comprising C4+ olefins with a zeolite-comprising catalyst at a temperature in the range of from 350 to 1000 °...
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WO/2013/034678 |
The present invention provides a process for preparing ethylene and propylene, comprising the step of: a) contacting a feed comprising methanol, ethanol and C4+ olefins with a catalyst, comprising ZSM-5 having a silica to alumina ratio i...
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WO/2013/034683 |
The present invention provides a process for preparing ethylene and/or propylene and an iso-olefin-depleted C4 olefinic product, comprising the steps of: a) providing a C4 hydrocarbon stream, comprising normal olefins and iso-olefins; b)...
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WO/2013/029457 |
Disclosed is a multi-stage plasma reactor for cracking carbonaceous material comprising: first stage of reaction tube mainly for mixing of the carbonaceous material, carrier gas with first heating gas and pyrolysis of the carbonaceous ma...
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WO/2013/025642 |
Techniques, systems, apparatus and material are disclosed for generating renewable energy from biomass waste while sequestering carbon. In one aspect, a method performed by a reactor to dissociate raw biomass waste into a renewable sourc...
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WO/2013/015676 |
The present invention relates to a process for producing liquid transportation fuel (15) based on plastic waste materials (10), comprising the step of: providing (S101) plastic waste materials (10) in molten form; de-polymerizing (S103) ...
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WO/2013/015676 |
The present invention relates to a process for producing liquid transportation fuel (15) based on plastic waste materials (10), comprising the step of: providing (S101) plastic waste materials (10) in molten form; de-polymerizing (S103) ...
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WO/2013/013344 |
An ethylene cracking furnace is provided, comprising: at least one radiation region where a bottom burner and/or side wall burner is installed; and at least one set of radiation furnace tubes arranged along the longitudinal direction of ...
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WO/2013/015895 |
Processes are disclosed that achieve a high conversion of lignin to aromatic hydrocarbons, and that may be carried out without the addition of a base. Depolymerization and deoxygenation, the desired lignin convention steps to yield aroma...
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WO/2013/015895 |
Processes are disclosed that achieve a high conversion of lignin to aromatic hydrocarbons, and that may be carried out without the addition of a base. Depolymerization and deoxygenation, the desired lignin convention steps to yield aroma...
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WO/2012/170082 |
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/2012/161872 |
The present techniques provide a pyrolysis process that is reduced in coke and/or tar formation relative to comparable processes. A flushing fluid is applied or injected directly into a pyrolysis reactor to reduce high levels of coke and...
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WO/2012/161281 |
This method for producing monocyclic aromatic hydrocarbons comprises: a decomposition reforming reaction step in which oil feedstock is brought into contact with a catalyst for producing monocyclic aromatic hydrocarbons to produce a reac...
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WO/2012/161261 |
The present invention is a method for producing a monocyclic aromatic hydrocarbon whereby oil feedstock, which has a 10% distillation temperature of at least 140°C and a 90% distillation temperature of not more than 380°C, is brought i...
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WO/2012/161264 |
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/2012/139181 |
A process is described for FCC middle distillate maximization comprising the use of two distinct converters, which are operably coupled, said process aiming to maximize the production of LCO for diesel, generate a specific gasoline and d...
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WO/2012/142491 |
This invention provides processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to gene...
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WO/2012/139181 |
A process is described for FCC middle distillate maximization comprising the use of two distinct converters, which are operably coupled, said process aiming to maximize the production of LCO for diesel, generate a specific gasoline and d...
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WO/2012/133180 |
This method for producing single-ring aromatic hydrocarbons by contacting a starting material oil having a 10 vol% distillation temperature of at least 140°C and a 90 vol% distillation temperature of no greater than 380°C to a catalyst...
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WO/2012/133170 |
The method for producing an aromatic hydrocarbon of the present invention is a method for producing an aromatic hydrocarbon wherein a catalyst for the production of a monocyclic aromatic hydrocarbon containing crystalline aluminosilicate...
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WO/2012/133138 |
This method that is for producing single-ring aromatic hydrocarbons and that produces single-ring aromatic hydrocarbons having 6-8 carbon atoms has: a breakdown/modification reaction step for obtaining a product containing single-ring ar...
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WO/2012/133168 |
This method for producing single-ring aromatic hydrocarbons has: a breakdown/modification reaction step for obtaining a product by introducing into a breakdown/modification reaction vessel a starting material oil, contacting the starting...
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WO/2012/133197 |
This method for producing single-ring aromatic hydrocarbons has: a breakdown/modification reaction step for obtaining a product containing single-ring aromatic hydrocarbons having 6-8 carbon atoms by contacting a starting material oil to...
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WO/2012/126670 |
In the preparation of low molecular weight olefins, especially of ethylene and propylene, a reactant stream (O) comprising at least one oxygenate and a reactant stream (C) comprising at least one C4+ olefin are converted simultaneously i...
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WO/2012/121985 |
A method comprises forming a reaction mixture comprising a terephthalate polyester, a glycol comprising 2 to 5 carbons, and an amidine organocatalyst; and heating the reaction mixture at a temperature of about 120° C or more to depolyme...
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WO/2012/121985 |
A method comprises forming a reaction mixture comprising a terephthalate polyester, a glycol comprising 2 to 5 carbons, and an amidine organocatalyst; and heating the reaction mixture at a temperature of about 120° C or more to depolyme...
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WO/2012/099678 |
An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques combine a firs...
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WO/2012/099672 |
The invention relates to processes for converting a mixture of hydrocarbon and sulfur- containing molecules such as mercaptan into products comprising acetylene, ethylene, and hydrogen sulfide, to processes utilizing the acetylene and et...
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WO/2012/099675 |
An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into ethylene. In particular, the present techniques expose feed containing hydrocarbons to high-severity oper...
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WO/2012/099679 |
An apparatus and method are provided for processing hydrocarbon feeds. The method may pass a pyrolysis feed to a thermal pyrolysis reactor and expose at least a portion of the pyrolysis feed to high-severity operating conditions in a the...
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WO/2012/099672 |
The invention relates to processes for converting a mixture of hydrocarbon and sulfur- containing molecules such as mercaptan into products comprising acetylene, ethylene, and hydrogen sulfide, to processes utilizing the acetylene and et...
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WO/2012/099671 |
An apparatus and method are provided for processing hydrocarbon feeds. The method may contact hydrogen (H2) and a hydrocarbon feed containing ≥ 10 wt% resid in the hydrocarbon feed with a catalyst to form a hydroprocessed product. Then...
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WO/2012/099677 |
An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques utilize a high...
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WO/2012/099676 |
An apparatus and process are provided for processing hydrocarbon feeds. The process enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques utilize two ...
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WO/2012/099676 |
An apparatus and process are provided for processing hydrocarbon feeds. The process enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques utilize two ...
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WO/2012/099677 |
An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques utilize a high...
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WO/2012/099675 |
An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into ethylene. In particular, the present techniques expose feed containing hydrocarbons to high-severity oper...
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WO/2012/091119 |
This catalyst for producing a monocylic aromatic hydrocarbon: is a catalyst for producing a monocyclic aromatic hydrocarbon with 6 to 8 carbons from raw oil, of which 10% by volume has been distilled at 140°C or higher and 90% by volume...
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WO/2012/091100 |
This catalyst for producing a monocylic aromatic hydrocarbon: is a catalyst for producing a monocyclic aromatic hydrocarbon with 6 to 8 carbons from raw oil, of which 10% by volume has been distilled at 140°C or higher and 90% by volume...
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WO/2012/091099 |
In this method for producing a monocylic aromatic hydrocarbon, raw oil, of which 10% by volume has been distilled at 140°C or higher and 90% by volume has been distilled at 380°C or lower, is brought into contact with a catalyst for pr...
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WO/2012/088852 |
Provided is a process for catalytic cracking naphtha coupled with methanol using a modified ZSM-5 molecular sieve catalyst. Said process includes co-feeding methanol with naphtha to react on the modified ZSM-5 molecular sieve catalyst fo...
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WO/2012/091092 |
This catalyst for producing a monocylic aromatic hydrocarbon: is a catalyst for producing a monocyclic aromatic hydrocarbon with 6 to 8 carbons from raw oil, of which 10% by volume has been distilled at 140°C or higher and 90% by volume...
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