Sabic Global Technologies B.v.

Krishnan Sankaranarayanan

Ravichander Narayanaswamy

Krishna Kumar Ramamurthy

Alexander Stanislaus

Istvan Lengyel

Hatem Belfadhel

Girish Koripelly

David H West

Dick Alan Nagaki

Aghaddin Mamedov

Sreekanth Pannala

Lei Chen

Vladimir Shtern

Zhun Zhao

Byeongjin Baek

Derek Falcone

C William Gundlach, Iv

Myat Noe Zin Myint

C William Gundlach Iv

Systems and methods for producing olefins and/or aromatics are disclosed. Methods disclosed includes thermal hydro-processing of crude oils and/or heavy oils and/or residues, in a thermal hydro-processing unit, to produce intermediate products, which can then be used to make valuable chemicals such as olefins and aromatics.

Conversion of heavy ends of crude oil or whole crude oil to high value chemicals using a combination of thermal hydroprocessing, hydrotreating with steam crackers under high severity conditions to maximize ethylene, propylene, butenes and benzene

Systems and methods for producing olefins and/or aromatics are disclosed. Methods disclosed includes aqua-processing hydro-processing of crude oils and/or heavy oils and/or residue, in an aqua-processing hydro-processing unit, to produce intermediate products, which can then be used to make valuable chemicals such as olefins and aromatics.

Methods and systems for upgrading crude oils, heavy oils, and residues

A reactor () and method for the conversion of hydrocarbon gases utilizes a reactor () having a unique feed assembly () with an original vortex disk-like inlet flow spaces (), a converging-diverging vortex mixing chamber (), and a cylindrical reactor chamber (). This design creates a small combustion zone and an inwardly swirling fluid flow pattern of the feed gases that passes through a converging conduit () with a constricted neck portion (). This provides conditions suitable for efficient cracking of hydrocarbons, such as ethane, to form olefins.

Method and reactor for conversion of hydrocarbons

A method for producing Chydrocarbons and Hcomprising (a) introducing to a reactor a reactant mixture comprising methane, (b) heating the reactant mixture to a preheating temperature to yield a heated mixture, (c) generating free radicals in the heated mixture to form a primary effluent mixture comprising free radicals, Chydrocarbons, H, and unreacted methane, (d) reacting the primary effluent mixture in a secondary reaction zone to form a secondary effluent mixture comprising Chydrocarbons, H, free radicals, and unreacted methane, at a secondary reaction zone temperature that is greater than the preheating temperature, wherein a free radicals amount in the primary effluent mixture is greater than a free radicals amount in the secondary effluent mixture, (e) cooling the secondary effluent mixture to a quench temperature lower than the secondary reaction zone temperature to yield a product mixture comprising Chydrocarbons and H, and (f) recovering the product mixture.

Method for producing hydrocarbons by non-oxidative coupling of methane

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Missouri City, TX, United States of America

Krishnan Sankaranarayanan