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WO/2014/099325A1 |
A new family of crystalline aluminosilicate zeolites has been synthesized that has been designated UZM-43. These zeolites are similar to previously known ERS-10, SSZ-47 and RUB-35 zeolites but are characterized by unique x-ray diffractio...
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WO/2014/097350A1 |
As a technique for increasing the yield of an aromatic hydrocarbon and/or an olefin having 4 or less carbon atoms by improving the steam resistance of a catalyst for hydrocarbon catalytic cracking, there is provided a method for producin...
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WO/2014/092896A1 |
A process of catalytically cracking a feedstock based on a biocomponent contacts the feedstock with a catalytic cracking catalyst comprising a basic metal oxide on a porous oxide support at an elevated cracking temperature to eliminate o...
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WO/2014/093564A1 |
A process and apparatus are disclosed for recovering a product stream by fractionation perhaps with compression of a C5? hydrocarbon stream. The C5? hydrocarbon stream may be taken from an overhead of a fractionation column. Fractionatio...
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WO/2014/093016A1 |
Method and apparatuses for producing ethylene and propylene from naphtha feedstock are provided. The naphtha feedstock includes a first component consisting of hydrocarbons that have less than or equal to five carbon atoms and a second c...
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WO/2014/085279A1 |
A new family of crystalline microporous metallophosphates designated AlPO-67 has been synthesized. These metallophosphates are represented by the empirical formula R+ rMm 2+EPxSiyOz where R is an organoammonium cation such as the ETMA+ o...
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WO/2014/085281A1 |
A new family of crystalline microporous metallophosphates designated MAPSO-64 has been synthesized. These metallophosphates are represented by the empirical formula R+rMmn+EPxSiyOz where R is an organoammonium cation such as ETMA+ or DED...
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WO/2014/074856A1 |
Distillate cracks to propylene more readily than VGO. Additionally, less branched hydrocarbons crack to propylene more readily than more branched hydrocarbons. Oligomerization to diesel range oligomers followed by catalytic cracking with...
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WO/2014/074975A1 |
One exemplary embodiment can be a process for fluid catalytic cracking. The process can include providing a first feed including one or more heavy hydrocarbons to a riser of a riser-reactor, and obtaining a second feed from an oligomeriz...
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WO/2014/074980A1 |
A process provides oligomerization feed stream comprising C5 hydrocarbons and olefins along with C4 olefins to an oligomerization zone. The oligomerization feed stream may be obtained from cracked FCC products. Unreacted C5 hydrocarbons ...
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WO/2014/071842A1 |
A process and an apparatus used in the catalytic reaction process with feed of petroleum hydrocarbons or alcohols for controlling catalyst in reaction zones, purifying, heat transferring and cooling regenerant are provided. The apparatus...
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WO/2014/070857A2 |
A system and method for improving the quality of a raw gas or raw syngas passes the raw gas or raw syngas past a catalytic element comprising catalyst with an optional sorbent. A downstream measurement of one or more parameters of the im...
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WO/2014/068498A1 |
The thermal conversion and/or catalytic plants, which can be found in the productive cycle of a refinery, are aimed at the utilization of the residues of the distillation of petroleum, otherwise destined for bitumen or combustible oil (p...
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WO/2014/065420A1 |
This olefin and single-ring aromatic hydrocarbon production method involves: a cracking reforming reaction step for obtaining a product containing olefins and single-ring aromatic hydrocarbons by bringing into contact with a catalyst and...
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WO/2014/064109A1 |
Reactor vessel and a feed nozzle assembly (1) for feeding a gas and a liquid into such reactor vessel. The feed nozzle assembly comprises an outer tube (3) supplying a first liquid feed, such as oil, an inner tube (2) supplying a dispers...
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WO/2014/064008A1 |
A process for converting a biomass, comprising contacting the biomass with a catalytic cracking catalyst at a temperature of more than 400°C in a catalytic cracking reactor to produce a product stream containing one or more cracked prod...
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WO/2014/065419A1 |
This single-ring aromatic hydrocarbon production method involves a cracking reforming reaction step for obtaining products including 6-8C single-ring aromatic hydrocarbons by 1-3C saturated hydrocarbons and a raw oil having a 10 vol% dis...
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WO/2014/064261A1 |
A process for catalytic cracking of a pyrolysis oil derived from material comprising biomass, comprising the steps of a) subjecting a feed comprising the pyrolysis oil to a hydrodeoxygenation step to prepare an at least partially deoxyge...
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WO/2014/065421A1 |
This olefin and single-ring aromatic hydrocarbon production method involves: a dicyclopentadiene removal step for removing dicyclopentadienes having a dicyclopentadiene skeleton from a raw oil having the distillation characteristic of a ...
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WO/2014/062465A1 |
In an FCC process and system, a whole crude oil feedstock is directly converted into light olefins and other products. The feed is separated into a high boiling fraction and a low boiling fraction, and each fraction is processed in separ...
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WO/2014/057931A1 |
A catalyst for the catalytic cracking of a hydrocarbon oil is provided with which it is possible to produce a gasoline fraction with a high octane number in high yield while inhibiting the yield of heavy fractions from increasing, in par...
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WO/2014/054234A1 |
[Problem] To provide: a method for treating a hydrocarbon oil, whereby it becomes possible to reduce the content of a diene or an olefin in the hydrocarbon oil even when hydrogen is unavailable; and an apparatus for treating a hydrocarbo...
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WO/2014/046866A1 |
A process for producing coke that may include: heating a coker feedstock to a coking temperature to produce a heated coker feedstock; feeding the heated coker feedstock to a coking drum; feeding a coking additive, such as at least one hy...
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WO/2014/043049A1 |
Methods are provided for qualifying jet fuel fractions that are derived at least in part from pre-refined crude oil sources. The methods allow for determination of the stability of a jet fuel product over time by using an accelerated agi...
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WO/2014/027537A1 |
This catalyst for hydrocarbon catalytic cracking is obtained by mixing a catalyst (a) comprising a faujasite-type zeolite (A) having a lattice constant within the range of 2.435-2.455 nm, a matrix component, and a rare earth, and a catal...
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WO/2014/021975A1 |
Methods and apparatuses for upgrading a pyrolysis oil stream and a hydrocarbon stream are provided herein. In an embodiment, a method for upgrading a pyrolysis oil stream and a hydrocarbon stream includes separately introducing the pyrol...
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WO/2014/021974A1 |
Methods and apparatuses for upgrading a pyrolysis oil stream and a hydrocarbon stream are provided. In an embodiment, a method for upgrading a pyrolysis oil stream and a hydrocarbon stream includes providing the pyrolysis oil stream and ...
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WO/2014/018484A1 |
A rare earth free, ultra low soda, particulate fluid catalytic cracking catalyst which comprises a reduced soda zeolite having fluid catalytic cracking ability under fluid catalytic cracking conditions, a magnesium salt, an inorganic bin...
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WO/2014/016764A1 |
The present invention provides a catalyst composition for use in a catalytic cracking process, said catalyst composition comprises 3.5 to 15.5 % of pentasil zeolite, 9 to 40 % of ultra-stable Y (USY) or rare earth exchanged USY (REUSY) z...
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WO/2014/001587A1 |
The invention relates to a method, in the absence of hydrogen, for the catalytic cracking of organic compounds using a zeolitic material, modified Y zeolite. In said cracking method, the modified zeolitic material can be the sole zeoliti...
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WO/2014/003890A1 |
A process and apparatus described is for distributing hydrocarbon feed to catalyst in a riser. Hydrocarbon feed is delivered to a plenum in the riser. Nozzles from the plenum inject feed into the riser to contact the catalyst. Streams of...
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WO/2014/003891A1 |
An apparatus for mixing streams of regenerated and carbonized catalyst utilizes bend provided on only one of the catalyst conduits to provide mixing advantages. A pair of horizontally aligned openings with a band between the pair of open...
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WO/2014/000423A1 |
Disclosed are a catalytic cracking catalyst and the preparation method therefor. The catalytic cracking catalyst comprises a cracking active component, 10 weight％-70 weight％ of clay in dry weight, and 10 weight％-40 weight％ of an ...
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WO/2013/188729A1 |
A direct catalytic cracking system for converting undistilled and imfractionated hydrocarbon material into hydrocarbon products, which include light olefins and C6-8 aromatics. The direct catalytic cracking system includes a moving catal...
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WO/2013/087480A9 |
A process and catalyst system for thermal catalytic cracking of pyrolysis derived organic molecules comprising at least a first inorganic catalytic material and a second inorganic catalytic material. The first inorganic catalytic materia...
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WO/2013/188577A1 |
An access system (100) for a pressure controlled environment is disclosed and described. The system (100) can include a pressurized region (110) having a first fluid (104). The pressurized region (110) can be defined, at least partially,...
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WO/2013/184282A1 |
One exemplary embodiment may be a process for fluid catalytic cracking. The process can include providing a stream through a plurality of distributors to a riser terminating in a reaction vessel. Often, the plurality of distributors incl...
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WO/2013/177707A1 |
A fuel processor with a floating catalyst has a reactant gas passage and a product gas passage separated by a separating wall which is fixed at one end and free at the other end, to permit differential thermal expansion. The catalyst is ...
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WO/2013/177728A1 |
The invention discloses a catalytic cracking catalyst for heavy oil and a preparation method thereof. The catalyst contains 2-50 wt% of a phosphorus-containing ultrastable rare earth Y-type molecular sieve, 0.5-30 wt% of one or more othe...
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WO/2013/177388A1 |
A fluid catalytic cracking catalyst for increased production of propylene and gasoline from heavy hydrocarbon feedstock, the catalyst comprising between 10 and 20% by weight of an ultra-stable Y-type zeolite, between 10 and 20% by weight...
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WO/2013/173164A1 |
One exemplary embodiment can be a process for mixing catalyst in a regenerator. The process can include providing a first stream of catalyst, a second stream of catalyst mixed with the first stream of catalyst, and an oxygen-containing g...
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WO/2013/028454A9 |
A process and apparatus are disclosed for recovering hydroprocessing effluent from a hydroprocessing unit utilizing a hot stripper and a cold stripper. A net overhead stream from the hot stripper is forwarded to the cold stripper for fur...
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WO/2013/169463A1 |
In a hydrocarbon upgrading process, a hydrocarbon feed is treated in at least one of a steam cracker, catalytic cracker, coker, hydrocracker, and reformer under suitable conditions to produce a first stream comprising olefinic and aromat...
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WO/2013/165960A1 |
Systems and methods for gasifying a feedstock are provided. A feedstock can be introduced to a riser. A first oxidant can be introduced to a first mixing zone within the riser, thereby generating a first high temperature zone within the ...
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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/2013/161333A1 |
The mixing device of the present invention for mixing a raw material and a catalyst used in a fluid catalytic cracking device is provided with a cylindrical reaction container (5) for supplying a catalyst (S) in the vertical direction, a...
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WO/2013/158488A2 |
A method of improving the uniformity of the contacting of a heavy oil feed with FCC cracking catalyst in the feed zone of an FCC cracking riser in which the heavy oil feed is injected into the catalyst in the riser by means of feed injec...
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WO/2013/158235A1 |
Fluid catalytic cracking units having risers with improved hydrodynamics through the use of baffles are described. The baffles break up the high concentration of catalyst in the slower moving outer annulus and redistribute it into the fa...
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WO/2013/144689A1 |
An apparatus which is an integral hardware consisting of an annular downer reactor and a concentric upflow riser regenerator for catalytic cracking of hydrocarbon feed to is disclosed. The annular downer reactor terminates in annular str...
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WO/2013/142026A1 |
One exemplary embodiment can be a process for fluid catalytic cracking. The process can include sending a first catalyst from a first riser reactor and a second catalyst from a second riser reactor to a regeneration vessel having a first...
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