Siluria Technologies, Inc.

Lummus Technology Inc.

Siluria, LLC

Sam Weinberger

Erik C Scher

Alex Tkachenko

Justin Dwight Edwards

Julian Wolfenbarger

Joel M Cizeron

Fabio R Zurcher

Joel Gamoras

Wayne Paul Schammel

Greg Nyce

Srinivas R Vuddagiri

Dmitry Karshtedt

Rahul Iyer

Iraj Isaac Rahmim

Jarod McCormick

Guido Radaelli

Milind Ajinkya

Hatem Harraz

Jon McCarty

David Sheridan

Dave Sheridan

Jarod Mccormick

Jon Mccarty

Erik Scher

Ajay Madgavkar

Lawrence Peck

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

The present disclosure provides natural gas and petrochemical processing systems including oxidative coupling of methane reactor systems that integrate process inputs and outputs to cooperatively utilize different inputs and outputs of the various systems in the production of higher hydrocarbons from natural gas and other hydrocarbon feedstocks.

Natural gas processing and systems

Natural gas and petrochemical processing systems including oxidative coupling of methane reactor systems that integrate process inputs and outputs to cooperatively utilize different inputs and outputs of the various systems in the production of higher hydrocarbons from natural gas and other hydrocarbon feedstocks.

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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San Francisco, CA, United States of America

Sam Weinberger