Siluria Technologies, Inc.

Lummus Technology Inc.

Siluria, LLC

Justin Dwight Edwards

Joel M Cizeron

Jarod McCormick

Sam Weinberger

Julian Wolfenbarger

David Sheridan

Guido Radaelli

Roberto O Pellizzari

Srinivas R Vuddagiri

Jin Ki Hong

Satish Lakhapatri

Erik Freer

Samuel Weinberger

Iraj Isaac Rahmim

Charles Reid

Erik C Scher

Fabio R Zurcher

Joel Gamoras

Wayne Paul Schammel

Greg Nyce

Dmitry Karshtedt

Alex Tkachenko

Milind Ajinkya

Jon McCarty

Dave Sheridan

Jarod Mccormick

Jon Mccarty

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

Disclosed herein are processes for producing and separating ethane and ethylene. In some embodiments, an oxidative coupling of methane (OCM) product gas comprising ethane and ethylene is introduced to a separation unit comprising two separators. Within the separation unit, the OCM product gas is separated to provide a C-rich effluent, a methane-rich effluent, and a nitrogen-rich effluent. Advantageously, in some embodiments the separation is achieved with little or no external refrigeration requirement.

Process for separating hydrocarbon compounds

Systems and methods conducive to the formation of one or more alkene hydrocarbons using a methane source and an oxidant in an oxidative coupling of methane (OCM) reaction are provided. One or more vessels each containing one or more catalyst beds containing one or more catalysts each having similar or differing chemical composition or physical form may be used. The one or more catalyst beds may be operated under a variety of conditions. At least a portion of the catalyst beds may be operated under substantially adiabatic conditions. At least a portion of the catalyst beds may be operated under substantially isothermal conditions.

Oxidative coupling of methane systems and methods

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Pacifica, CA, United States of America

Justin Dwight Edwards