Siluria Technologies, Inc.

Lummus Technology Inc.

Kainos Tech Incorporated

Xerox Corporation

Silura Technologies, Inc.

Oh Pharmaceuticals Co. Ltd

Jin Ki Hong

Joel M Cizeron

Erik Freer

Erik C Scher

Jarod McCormick

Guido Radaelli

Wayne Paul Schammel

Fabio R Zurcher

Joel Gamoras

Roberto O Pellizzari

Daniel Rosenberg

Anja Rumplecker

David Sheridan

Satish Lakhapatri

Justin Dwight Edwards

Samuel Weinberger

Sam Maurer

Charles Reid

Humera A Rafique

Bradley Rupp

Hatem Harraz

Mary Louie

Dane Andrew Boysen

Jarod Mccormick

Srinivas Vuddagiri

Ajay M Madgavkar

Greg Nyce

Srinivas R Vuddagiri

Aihua Zhang

Bipinkumar Patel

Ron Runnebaum

Tim A Rappold

Suchia Duggal

William Michalak

Rahul Iyer

Peter Czerpak

Carlos Faz

Richard Black

Jessica De Paula Tadeu Medrado

Hassan Taheri

Erik M Freer

Systems for hydrocarbon pyrolysis are provided, which may comprise a reactor configured to contain a liquid metal; a heater operably coupled to the reactor to form a heating zone; a cooler operably coupled to the reactor to form a cooling zone; a gas delivery assembly comprising an inlet and configured to deliver a feed gas comprising a hydrocarbon as a plurality of bubbles through the liquid metal; an outlet configured to deliver a product gas to a separation assembly, the product gas formed from pyrolysis of the hydrocarbon in the liquid metal, the product gas comprising Hand carbon; and the separation assembly configured to separate the carbon from other components of the product gas. The reactor is configured to entrain the carbon from pyrolysis of the hydrocarbon in the liquid metal into the product gas without accumulating the carbon in the interior chamber during pyrolysis.

Systems and methods for hydrocarbon pyrolysis

A method of producing hydrogen may include: providing a catalyst-carbon gel; and flowing a hydrocarbon through a catalyst, wherein catalyst is a metal or mixture of metals that is non-wetting to solid carbon at 1 bar absolute and 10° C. above a melting point of the metal or mixture of metals.

Hydrogen production methods and related systems and compositions

In an aspect, the present disclosure provides a method for the oxidative coupling of methane to generate hydrocarbon compounds containing at least two carbon atoms (Ccompounds). The method can include mixing a first gas stream comprising methane with a second gas stream comprising oxygen to form a third gas stream comprising methane and oxygen and performing an oxidative coupling of methane (OCM) reaction using the third gas stream to produce a product stream comprising one or more Ccompounds.

Reactors and systems for oxidative coupling of methane

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Catalysts for natural gas processes

Provided is a method for producing aromatic hydrocarbons from light alkanes. A light alkane is contacted with catalyst particles in each of reactors, wherein each of the reactors is a fluidized bed reactor arranged in parallel with each other in a furnace. At least a portion of the alkane feed is converted to aromatic hydrocarbons using the catalyst particles, wherein the aromatic hydrocarbons form a part of a reactor effluent stream. The reactor effluent streams from each of the reactors are merged to form a first merged effluent stream. Catalysts particles deactivated through the light alkane conversion are either regenerated inside the reactors or withdrawn from the reactors for regeneration outside the reactors. The furnace comprises multiple furnaces, and the first merged effluent stream from each of the furnaces is further merged with each other to form a second merged effluent stream.

Production of aromatic hydrocarbons from light alkanes

A process and an apparatus for producing olefins from light alkanes. A light alkane feed is contacted with catalyst particles in each of reactors, wherein each of the reactors is a fluidized bed reactor. At least a portion of the alkane feed is converted to olefins using the catalyst particles, wherein the olefins form a part of a reactor effluent stream. The reactor effluent streams from each of the reactors are merged to form a merged effluent stream. The merged effluent stream is separated into an olefin stream and the other streams. The other streams may comprise a recycle stream and light gases.

Process and apparatus for producing olefins from light alkanes

Provided is a method for producing aromatic hydrocarbons from light alkanes. A light alkane feed is contacted with catalyst particles in each of reactors, wherein each of the reactors is a fluidized bed reactor and arranged in parallel with each other in a furnace. At least a portion of the alkane feed is converted to aromatic hydrocarbons using the catalyst particles, wherein the aromatic hydrocarbons form a part of a reactor effluent stream. The reactor effluent streams from each of the reactors are merged to form a first merged effluent stream. The first merged effluent stream is separated into the aromatic hydrocarbons, light hydrocarbons, and a fuel gas.

Integrated systems are provided for the production of higher hydrocarbon compositions, for example liquid hydrocarbon compositions, from methane using an oxidative coupling of methane system to convert methane to ethylene, followed by conversion of ethylene to selectable higher hydrocarbon products. Integrated systems and processes are provided that process methane through to these higher hydrocarbon products.

Ethylene-to-liquids systems and methods

A process for producing aromatic hydrocarbons from a light alkane feedstock such as an ethane-containing hydrocarbon stream is disclosed. The process comprises: contacting a light alkane feedstock comprising at least 50% ethane with a bi-functional aromatization catalyst in a fluidized bed reactor of bubbling or turbulent fluidization regime. The fluidized bed reactor comprise a catalyst bed, catalytic combustor and internal heat exchanger tubes embedded in the catalyst bed to provide the heat supply necessary for production of aromatic hydrocarbons. Continuous and uninterrupted production of aromatic hydrocarbons is realized by fluidly connecting multiple reactors in parallel and cycling operation of individual reactors between aromatics production mode and catalyst regeneration mode.

Production of aromatic hydrocarbons

The present disclosure provides oxidative coupling of methane (OCM) systems for small scale and world scale production of olefins. An OCM system may comprise an OCM subsystem that generates a product stream comprising Ccompounds and non-Cimpurities from methane and an oxidizing agent. At least one separations subsystem downstream of, and fluidically coupled to, the OCM subsystem can be used to separate the non-Cimpurities from the Ccompounds. A methanation subsystem downstream and fluidically coupled to the OCM subsystem can be used to react Hwith CO and/or COin the non-Cimpurities to generate methane, which can be recycled to the OCM subsystem. The OCM system can be integrated in a non-OCM system, such as a natural gas liquids system or an existing ethylene cracker.

Oxidative coupling of methane implementations for olefin production

Growing community of inventors

Moraga, CA, United States of America

Jin Ki Hong