| Document |
Document Title |
|
WO/2015/112399A1 |
A metal contaminated spent catalyst or regenerated catalyst from a biomass conversion unit may be subjected to an ammonium wash in order to remove potassium. The ammonium wash may include ammonium sulfate, ammonium nitrate, ammonium hydr...
|
|
WO/2015/075565A9 |
The present invention relates to a novel catalyst composition for catalytic cracking of hydrocarbon streams to enhance the yield of light olefins. The catalyst composition for the cracking of hydrocarbon feed streams to light olefins, co...
|
|
WO/2015/102002A1 |
The invention provides a process for preparing SAPO-11, that comprises combining in an aqueous solution alumina source, P 2 O source and a silica source in the presence of a crystallization template and a surfactant to form a gel, which ...
|
|
WO/2015/094657A1 |
The present invention discloses a process optimizing the yield of propylene from a fluid catalytic cracking unit. The method combines a first catalytic reactor, a fractionation zone, a separation unit and a second catalytic reactor. The ...
|
|
WO/2015/094916A1 |
Fluid catalytic cracking (FCC) processes are described, the processes utilizing one or more boron oxide components. Also described are FCC compositions and methods of manufacture. One or more boron oxide components on FCC compatible inor...
|
|
WO/2015/094920A1 |
Described are fluid catalytic cracking (FCC) compositions, methods of manufacture and use. FCC catalyst compositions comprise particles first particle type comprising one or more boron oxide components and a first matrix component and a ...
|
|
WO/2015/094908A1 |
Described are fluid catalytic cracking (FCC) compositions, methods of manufacture and use. FCC catalyst compositions comprise particles containing a non-zeolitic component and one or more boron oxide components. In embodiments, the FCC c...
|
|
WO/2015/094654A1 |
A process for catalytic cracking includes the steps of: (a) contacting a hydrocarbon feed with a catalyst at catalytic cracking conditions; (b) adsorbing hydrogen on the catalyst during cracking; and (c) producing a cracked product, pref...
|
|
WO/2015/088616A1 |
Methods and apparatuses for processing hydrocarbons are provided. In one embodiment, a method for processing hydrocarbons includes providing a stream of olefins including normal olefins and non-normal olefins. The method includes separat...
|
|
WO/2015/082313A1 |
The invention concerns a method for refining a heavy hydrocarbon feedstock comprising a) at least two steps of deasphalting in series carried out on said feedstock, making it possible to separate at least one asphalt fraction, at least o...
|
|
WO/2015/084779A1 |
The process described herein broadly comprehends an integrated process that permits the use of straight run residual fractions as a feedstock to produce lighter olefins including propylene. A blend of natural gas condensate and/or naphth...
|
|
WO/2015/073179A1 |
Embodiments of apparatuses and methods for hydrotreating coker kerosene or other thermally or catalytically cracked hydrocarbon stream are provided. In one example, a method comprises splitting a feed comprising coker kerosene into first...
|
|
WO/2015/071773A1 |
The present invention provides a catalyst product comprising of (a) porous acidic clay material and (b) binder and matrix to shape the catalyst to either microspheres, pellet, tablet, extrudate and ring and suitable for enhancing the cra...
|
|
WO/2015/065690A1 |
A fluid catalytic cracking reactor including a vessel, a chamber housed within the vessel, and a plurality of cyclones housed within the vessel, but externally of the chamber. The plurality of cyclones are arranged in a plurality of cycl...
|
|
WO/2015/054757A1 |
The present invention relates to a fluid catalytic cracking (FCC) method intended to maximise medium distillates of low aromaticity. This aim is achieved by the injection of air and, alternatively, gaseous oxygen in the contact region be...
|
|
WO/2015/053821A1 |
The present disclosure is directed to processes using a new crystalline molecular sieve designated SSZ-96, which is synthesized using a 1-butyl-1-methyl-octahydroindolium cation as a structure directing agent.
|
|
WO/2015/051266A1 |
A process for reactivating an iron-contaminated FCC catalyst is disclosed. The process comprises contacting the iron-contaminated FCC catalyst with an iron transfer agent. The iron transfer agent comprises a magnesia-alumina hydrotalcite...
|
|
WO/2015/048649A1 |
Disclosed are processes for extracting deasphalted crude oil from oil sand. Deasphalted crude oil can be extracted using a hydrocarbon recycle solvent stream having specified Hansen blend parameters, with the oil sand being contacted wit...
|
|
WO/2015/048588A1 |
Disclosed are processes for producing a transportation fuel from a high quality oil sands-derived crude oil. The oil sands-derived crude oil is provided as a feed source for a catalytic conversion reaction, which produces the product use...
|
|
WO/2015/035077A1 |
Methods and apparatus for producing bio-oil that include providing a catalyst that includes red mud in a catalyst bed in a fluid state, the catalyst being maintained at a temperature suitable for pyrolysis; providing a flow of a non-reac...
|
|
WO/2015/031050A1 |
A heat transfer unit includes an inlet manifold; an outlet manifold spaced from the inlet manifold; and a plurality of conduits coupling the inlet manifold to the outlet manifold, wherein at least on the conduits is coupled to the outlet...
|
|
WO/2015/026945A1 |
A method of operating a hydrocarbon material processing system includes feeding a hydrocarbon feedstock from a hydrocarbon feedstock source into a reaction tube positioned within an opening of a waveguide, feeding a process gas from a pr...
|
|
WO/2015/026938A1 |
A system for processing hydrocarbon materials includes a waveguide having a lateral portion comprising housing having a first end portion configured to be connected to an energy generator, a closed opposite end portion, a primary axis ex...
|
|
WO/2015/019313A2 |
A method and retort vessel for enabling continuous thermal or thermo-catalytic degradation of mixed waste plastic feedstock. The method includes receiving the feedstock into a rotary retort vessel. The feedstock is heated in the retort v...
|
|
WO/2015/020827A1 |
Disclosed are catalyst compositions including zeolite and silica components, methods of making, and processes of using in the thermo-catalytic conversion of biomass. Such disclosed methods of making include treating the zeolite with phos...
|
|
WO/2015/001214A1 |
The present invention describes a process for heating the reboiler of the propane/propylene separation column located downstream of an FCC unit and fed with the C3 fraction from said FCC unit, said process consisting in heating the water...
|
|
WO/2015/001004A1 |
Catalyst compositions comprising an inorganic porous material with pore diameters of at least 2 nm and of crystals of molecular sieve, characterized in that the crystals of molecular sieve have an average diameter, measured by scanning e...
|
|
WO/2015/000850A1 |
The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, reforming, dearomatization, fluid catalytic cracking and aromatic ring opening, which process comp...
|
|
WO/2014/207756A1 |
A process for testing a zeolite based FCC catalyst and a ZSM-5 zeolite based FCC catalyst additive for simulating commercial plant yields is disclosed in, the present disclosure wherein the catalyst and the additive are subjected separat...
|
|
WO/2014/210150A1 |
The present application generally relates to the introduction of a renewable fuel oil as a feedstock into refinery systems or field upgrading equipment. For example, the present application is directed to methods of introducing a liquid ...
|
|
WO/2014/204720A1 |
FCC catalysts having improved attrition resistance are provided by mixing a cationic polyelectrolyte with either zeolite crystals or a zeolite-forming nutrient and/or a matrix material, prior to or during formation of a catalyst microsph...
|
|
WO/2014/199389A1 |
The present subject matter provides a process for hydrocarbon residue upgradation. The combination of the hydrocarbon residue along with aromatic rich hydrocarbons, catalysts and surfactants allow the operation of visbreaking unit at hig...
|
|
WO/2014/200633A1 |
The invention relates to a process for preparing molecular sieves, such as ZSM-57, using one or more structure directing agents selected from the group consisting of N 1,N 1,N 5,N 5-tetraethyl-N 1,N 5-dimethylpentane-1,5-diamininum, 1-et...
|
|
WO/2014/193537A1 |
A method of hydrocarbon conversion is described. The hydrocarbon feed is decontaminated using an ionic liquid and introduced into a conversion zone. The conversion of the decontaminated feed is increased compared to the conversion of the...
|
|
WO/2014/181293A1 |
The invention pertains to a zeolite catalyst, methods of making same, and its use in the catalytic cracking of naphtha for the production of lower molecular weight olefins and alkanes, while minimizing production less desirable products....
|
|
WO/2014/177988A1 |
The inventions described herein relate to catalysts comprising a zeolite comprising at least one metal or ion thereof, wherein the at least one metal or ion thereof comprises barium, strontium, titanium, tungsten, or a mixture thereof, a...
|
|
WO/2014/175941A1 |
Disclosed in one embodiment is a method for the catalytic pyrolysis of a carbonaceous material that includes contacting the carbonaceous material with a plurality of catalyst particles to produce a gas phase product and a solid phase pro...
|
|
WO/2014/148416A1 |
Provided is a method for easily manufacturing a catalytic cracking catalyst for hydrocarbon oil having high cracking activity when used on heavy hydrocarbon oil and allowing production with a high yield ratio of a gasoline fraction with ...
|
|
WO/2014/150874A1 |
Systems and methods for the external processing flash zone gas oil by recycling it through a vacuum residuum hydroprocessing unit before reentering the delayed coking process.
|
|
WO/2014/140175A1 |
The present invention relates to gravitational collision enhanced upgrading of heavy oils, It thus describes a thermodynamic cracking process for heavy oil, extra heavy oil and bituem as well as a thermodynamic cracking unit for carrying...
|
|
WO/2014/142874A1 |
A process for slurry-phase hydrocracking of a heavy hydrocarbon feedstock in a reactor, such as an upflow bubble column reactor, includes separately introducing additive in two size ranges into the feedstock. A fine size particle additiv...
|
|
WO/2014/129585A1 |
This method for producing single-ring aromatic hydrocarbons has a decomposition reformation reaction step for filling a fixed-bed reactor with a single-ring aromatic hydrocarbon production catalyst containing a crystalline aluminosilicat...
|
|
WO/2014/125345A1 |
A method of producing olefins and aromatic compounds from a feedstock is accomplished by introducing a hydrocarbon feedstock and a catalyst composition within a reactor. At least a portion of the reactor is at a reactor temperature of fr...
|
|
WO/2014/125344A1 |
A catalyst composition useful for producing olefins and aromatic compounds from a feedstock is formed from a fluidized catalytic cracking (FCC) catalyst and a ZSM-5 zeolite catalyst, wherein the amount of ZSM-5 zeolite catalyst makes up ...
|
|
WO/2014/125346A1 |
A method of producing olefins and aromatic compounds from a plastic feedstock includes introducing a plastic feedstock and a catalyst composition that is suitable for converting the plastic feedstock to at least one of olefins and aromat...
|
|
WO/2014/123610A1 |
This disclosure is directed to uses for a new cobalt aluminophosphate molecular sieve designated SSZ-85 prepared using a 1,3-diisopropylimidazolium ionic liquid.
|
|
WO/2014/116269A1 |
Herein disclosed is a method for catalytic cracking or reforming of hydrocarbons comprising: supersaturating a hydrocarbonaceous liquid or slurry stream in a high shear device with a gas stream comprising one or more C1-C6 hydrocarbons a...
|
|
WO/2014/116271A1 |
Herein disclosed is a method for thermal cracking or steam cracking of hydrocarbons comprising: supersaturating a hydrocarbonaceous liquid or slurry stream in a high shear device with a gas stream comprising steam or hydrogen and optiona...
|
|
WO/2014/099235A1 |
A cost effective method for reutilizing exiting refinery equipment associated with either a Reformer Unit or Isomerization Unit by converting such units into units and associated processes for hydrodesulfurizing and cracking naphtha feed...
|
|
WO/2014/096267A1 |
Provided is a Fluid Catalytic Cracking catalyst composition having increased propylene production with respect to other Fluid Catalytic Cracking catalysts (measured at constant conversion). The catalyst composition comprises a particulat...
|
