Siluria Technologies, Inc.

Other

Eaton Corporation

Jon McCarty

Erik C Scher

Joel M Cizeron

Fabio R Zurcher

Jarod McCormick

Ralph Albert Dalla Betta

Joel Gamoras

Wayne Paul Schammel

Greg Nyce

Dmitry Karshtedt

Alex Tkachenko

Sam Weinberger

Justin Dwight Edwards

Milind Ajinkya

Julian Wolfenbarger

David Sheridan

Sarento George Nickolas

Damodara M Poojary

Robert Anthony Corr, Ii

Mark A Spencer

Timothy J Caron

Dave Sheridan

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

A power generation system and method of operating a power generation system which comprises a diesel engine which produces lean exhaust which passed to an exhaust after treatment system comprising an exhaust line which is in communication with a controller, reformer, lean NOx trap and SCR has been taught wherein the reformer comprises oxidation and reforming catalyst is a composition which comprises a catalyst wash coat comprising a ZrOrefractory metal oxide support, a LnOdistributed on the surface of the refractory metal oxide in an amount to form a monolayer over the refractory metal oxide support wherein Ln is selected from the group consisting of La, Nd and mixtures thereof and Rh distributed over the catalyst surface in an effective amount to catalyze steam reforming at 650&#xb0; C.

Catalyst composition and structure for a diesel-fueled autothermal reformer placed in and exhaust stream

Methods and apparatus for control of NO in catalytic combustion systems, and more particularly to control of thermal or/and prompt NO produced during combustion of liquid or gaseous fuels in the combustor sections of catalytic combustor-type gas turbines, by controlled injection of water in liquid or vapor form at selected locations, orientations, amounts, rates, temperatures, phases, forms and manners in the compressor and combustor sections of gas turbines. The ratio of thermal NO ppm reduction to water addition, in weight %, is on the order of 4-20, with % NO reduction on the order of up to about 50-80% and NO of below 2 ppm. Liquid water, steam or superheated steam can be used to reduce NO in combustion systems operating at reaction zone temperatures above 900&deg; C., preferably 1400&deg; C. to 1700&deg; C. The amount of water added is sufficient to provide a concentration of water in the range of from about 0.1% to about 20% by weight of the total air and fuel mixture flowing into the post catalyst reaction zone. Water is introduced simultaneously or sequentially in a plurality of locations, at selected rates, amounts, temperatures, forms, and purity, preferably in accord with a suitable control algorithm.

Process and apparatus for control of NOx in catalytic combustion systems

Growing community of inventors

Menlo Park, CA, United States of America

Jon McCarty