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WO/2017/151845A1 |
A new family of crystalline microporous high charge density silicometallophosphates has been synthesized. These silicometallophosphate are represented by the empirical formula of: Rp+ rMm +ExPSiyOz where M is an alkali metal such as pota...
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WO/2017/151875A1 |
A new family of high charge density crystalline microporous silicometallophosphate designated SAPO-79 has been synthesized. These silicometallophosphate are represented by the empirical formula of: Rp+ rMm +ExPSiyOz where M is an alkali ...
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WO/2017/149728A1 |
This petroleum processing apparatus is characterized by including a direct crude fluid catalytic cracking reaction device through which crude oil or a mixture of crude oil and atmospheric residue oil is run, and reaction product distilla...
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WO/2017/151278A1 |
A method is disclosed for fluidizing a spent catalyst in a regenerator during a combustion process. The combustor includes a vessel and an air distributor. The air distributor includes an air grid and a plurality of first nozzles extendi...
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WO/2017/137866A1 |
Methods and systems for generating light olefins using a cyclic reactor configuration are provided. Methods can include heating a feedstream including hydrocarbons in a first heating unit and introducing the feedstream to a first reactor...
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WO/2017/127288A1 |
Systems and methods are provided for upgrading refinery fuel gas and/or production of naphtha from refinery fuel gas. Initially, an olefin-containing feed can be exposed to conventional conditions for removing a portion of C3+ compounds ...
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WO/2017/118301A1 |
A method and an apparatus for a catalytic cracking reaction and regeneration. The method consists of two reaction parts, a raw material reaction and a catalyst regeneration. The regenerator is divided from top to bottom into a gas-solid ...
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WO/2017/116750A1 |
Clean, safe and efficient methods, systems, and processes for utilizing thermolysis methods to processes to convert various e-waste sources into Clean Fuel Gas and Char source are disclosed. The invention processes e-waste sources, such ...
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WO/2017/114715A1 |
This invention relates generally to a process for producing gasoline component. More particularly, the invention relates to a process for producing high octane gasoline component using renewable raw material as an additional feedstock. F...
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WO/2017/116756A1 |
Methods are provided for upgrading disadvantaged feeds for use in lubricant base stock production. A disadvantaged feed can be upgraded by hydroprocessing the feed to form a hydroprocessed bottoms fraction. The hvdroprocessed bottoms fra...
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WO/2017/109640A1 |
The presently disclosed subject matter relates to methods of producing ethylene and propylene by the catalytic steam cracking of naphtha using an HZSM-5 catalyst. An example method can include providing a naphtha feedstock, providing ste...
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WO/2017/105580A1 |
Methods and processes for moving towards optimizing one or more parameters in a parallel train comprising two hydrocarbon cracking facilities where the two facilities either have non-identical process unit configurations or are operating...
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WO/2017/103021A1 |
The present invention relates to a process for continuously converting mixed waste plastic into waxes and liquid fuels by cracking. The process comprises the steps of feeding a mixed waste plastic stream to a cracking reactor where the m...
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WO/2017/105871A1 |
Methods are provided for FCC processing of atmospheric resid boiling range feedstocks derived from tight oils. Due to low contents of metals, sulfur, and/or coke-forming compounds, an atmospheric resid boiling range fraction derived from...
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WO/2017/087187A1 |
Multiphase separators, processes and systems for converting an oxygenate and/or olefin feedstock to a hydrocarbon product are described herein.
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WO/2017/081595A1 |
The presently disclosed subject matter provides methods for producing olefins and/or aromatics from coker naphtha. In a non-limiting embodiment, a method for producing aromatics includes hydrogenating the coker naphtha stream in the pres...
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WO/2017/082345A1 |
[Problem] To provide an additive for a fluid catalytic cracking (FCC) catalyst used with an FCC catalyst in FCC, the additive making it possible to increase the yield of lower olefins. [Solution] An additive for an FCC catalyst used in m...
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WO/2017/076855A1 |
The invention relates to a process for the positioning of a corrosion resistant coating on an internal or external metal wall (20) of a fluid catalytic cracking unit chamber, comprising: • (i) the shaping of a metal anchoring structure...
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WO/2017/071792A1 |
The invention relates to a method (100) for producing hydrogen and further reaction products by converting hydrocarbons. According to the invention, a first gas mixture containing hydrogen, carbon monoxide, and methane is produced by a s...
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WO/2017/072786A1 |
The present disclosure relates to an assembly implementing the process disclosed for atomizing a hydrocarbon feedstock. The method includes receiving the hydrocarbon feedstock (2) and a diluent mixed steam (3) from a first inlet (5) and ...
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WO/2017/068599A1 |
Methods and apparatus for fluid catalytic cracking (FCC) of a hydrocarbon feedstock is described. The apparatus (100) comprises a first reactor (1), a second reactor (2), and a regenerator assembly (3) shared and connected with the two r...
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WO/2017/053796A1 |
Biomass is converted into a bio-oil containing stream in a riser reactor containing a cooling media. The cooling media quenches the rapid heat transfer to the biomass during cracking of the biomass in the mixing zone of the riser. By low...
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WO/2017/051260A1 |
The present disclosure relates to an additive and a catalyst composition for a catalytic cracking process of vacuum gas oil for preparing cracked run naphtha having reduced liquid olefin content, and increased propylene and butylene yiel...
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WO/2017/051262A1 |
The present disclosure relates to an additive and a catalyst composition for a catalytic cracking process of vacuum gas oil for preparing cracked run naphtha having reduced liquid olefin content, and increased propylene and butylene yiel...
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WO/2017/051261A1 |
The present disclosure relates to an additive and a catalyst composition for a catalytic cracking process of vacuum gas oil for preparing cracked run naphtha having reduced liquid olefin content, and increased propylene and butylene yiel...
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WO/2017/044748A1 |
An interconnected set of two or more stages of reactors to form a bio-reforming reactor that generates syngas for a number of different liquid fuel or chemical processes is discussed. A first stage includes a circulating fluidized bed re...
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WO/2017/034914A1 |
A process for the laboratory deactivation of a porous solid comprising subjecting the porous solid to a cyclic treatment, the treatment being selected from a hydration/dehydration cyclic treatment, a thermal cyclic treatment, or combinat...
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WO/2017/020847A1 |
A preparation method for modified molecular sieve and a modified molecular sieve-containing catalytic cracking catalyst. The preparation method comprises: mixing molecular sieve slurry, a compound solution containing ions of group IIIB m...
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WO/2017/021977A1 |
A spray nozzle assembly 10 to use multi-stages atomization of liquid feed for fluidized catalytic cracking process is described. The assembly comprises an inner conduit 50 comprising a liquid inlet 22 to let liquid feed flow to enter the...
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WO/2017/021317A1 |
A gas oil composition comprising at least 20.0% by volume total aromatic content, at least 1.0% by volume bicyclic aromatic content, at least 0.2% by volume trior higher cyclic aromatic content, no more than 18.0% by mass naphthenobenzen...
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WO/2017/015597A1 |
Provided is a process for manufacturing a Fluid Catalytic Cracking catalyst additive composition with a novel binder. The steps involve mixing an alumina source with water to make a slurry; adding to the alumina slurry an amount of P2O5 ...
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WO2017009109A1 |
The present invention relates to a method for catalytic cracking of a naphtha cut in which the heat budget is provided by the combustion of a fraction of the C5 cut of the feedstock, said fraction only containing normals and isoparaffins...
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WO/2017/007603A1 |
A sulfur-contaminated ionic liquid catalyst is provided comprising 300 to 20,000 wppm of sulfur from a contaminant, wherein the catalyst is a chloroaluminate and it alkylates olefin and isoparaffin to make an alkylate gasoline blending c...
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WO/2017/001446A1 |
The present invention relates to a process for conversion of a hydrocarbon feed comprising saturated hydrocarbon compounds to olefin products comprising contacting a hydrocarbon feed stream with a catalyst in an oxidic form of the formul...
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WO/2017/003991A1 |
A catalyst standpipe comprising a horizontal section, a sloped section, and vertical section, wherein the vertical section comprises one or more ring portions and associated methods and systems.
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WO/2016/209074A1 |
The invention is directed to a process to prepare propylene from a mixture of hydrocarbons by performing the following steps. (a) extracting aromatics from the mixture of hydrocarbons thereby obtaining a mixture of hydrocarbons poor in a...
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WO/2016/209073A1 |
The invention is directed to a process to prepare propylene from a hydrocarbon feedstock comprising olefin hydrocarbon compounds by contacting the feedstock with a mixture of a heterogeneous cracking catalyst and a heterogeneous dehydrog...
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WO/2016/200566A1 |
An FCC unit enables the normal regenerator to be eliminated by carrying out catalyst regeneration in the reactor section of the unit using air, oxygen-enriched air or even relatively pure oxygen as the stripping medium in the stripping s...
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WO/2016/200565A1 |
A potentially heat-deficient fluid catalytic cracking process for effecting a bulk boiling point conversion of a high boiling point petroleum feed to lower boiling products in which the overall enthalpy balance between the endothermic cr...
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WO/2016/186761A1 |
Uses for a new crystalline molecular sieve designated SSZ-27 are disclosed. SSZ-27 is synthesized using a hexamethyl [4.3.3.0] propellane-8,11-diammonium cation as a structure directing agent.
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WO/2016/182786A1 |
A solids distributor (100) comprising: a solids standpipe (110); a gas line (120); a solids transfer line (130) in fluid communication with the solids standpipe (110) and the gas line (120); and a distributor (140) in fluid communication...
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WO/2016/179410A1 |
A method for optimizing a cracking efficiency with which a pyrolysis tube of a deposition apparatus cracks a precursor material into reactive species is disclosed, including measuring an input pressure at an entrance to the pyrolysis tub...
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WO/2016/171936A1 |
Process for minimizing the amount of catalyst fines in a flue gas from a catalyst regenerator. Pyrolysis oil is injected into the reaction zone, preferably downstream from the feed stream inlet. The catalyst fines will be passed along wi...
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WO/2016/157014A1 |
The present disclosure relates to a catalytic cracking process of vacuum gas oil for preparing cracked run naphtha with low olefin content. The process makes use of a catalyst composition which is a mixture of an FCC equilibrated catalys...
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WO/2016/156938A1 |
The present disclosure relates to an FCC catalyst additive composition, including at least one zeolite in an amount ranging from 30 to 50% of the total weight of the composition; at least one Group V element in an amount ranging from 0.1...
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WO/2016/160081A1 |
Processes are provided for conversion of oxygenated hydrocarbon, such as methanol and/or dimethyl ether, to aromatics, such as a para-xylene, and olefins, such as ethylene and propylene. The processes entail using a reactor having multip...
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WO/2016/157015A1 |
The present disclosure relates to a fluid catalytic cracking process. The process of the present disclosure includes contacting a feedstock containing vacuum gas oil (VGO) with a catalyst composition in an FCC reactor, at pre-determined ...
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WO/2016/141610A1 |
Provided are a heavy oil processing technology and a processing apparatus. The processing technology comprises the following steps: A) under air isolation conditions, performing a dry distillation reaction between the heavy oil and a cat...
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WO/2016/141189A1 |
A withdrawal system for withdrawing particulate matter from a high-temperature industrial process or withdrawing material from a cryogenic process such as a pharmaceutical manufacturing process is disclosed. The withdrawal system compris...
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WO/2016/137831A1 |
Apparatuses and methods are provided for fluid catalytic cracking. A fluid catalytic cracking apparatus includes a riser with a first inlet. A first distributor pipe is coupled to the riser at the riser inlet. A heat transfer device is c...
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