Velocys Technologies Limited

Velocys Corp.

Andre Peter Steynberg

Roger Allen Harris

John W Dolan

Jasmeer Jaichland Ramlal

Dennis Parker

Ivan Phillip Greager

Steven T Perry

Robert Dwayne Litt

Paul Edwin Kennedy

Steven Claude LeViness

Lucas D Schrader

Soumitra R Deshmukh

Roy Lipski

Sean P Fitzgerald

Laura J Silva

Bin Yang

Ravi Arora

Paul William Neagle

Ivan Philip Greager

Heinz J Robota

Stephen Claude LeViness

Jason Robinson

Deshmukh R Soumitra

Paul Schubert

Steven Perry

Steven Claude Levinness

The disclosed invention relates to a method for restarting a synthesis gas conversion process which has stopped. The synthesis gas conversion process may be conducted in a conventional reactor or a microchannel reactor. The synthesis gas conversion process may comprise a process for converting synthesis gas to methane, methanol or dimethyl ether. The synthesis gas conversion process may be a Fischer-Tropsch process.

Synthesis gas conversion process

The present invention provides an improved process for removing heat from an exothermic reaction. In particular, the present invention provides a process wherein heat can be removed from multiple reaction trains using a common coolant system.

Process of removing heat

The present technology is directed to processes for conversion of synthesis gas in a tubular reactor to produce a synthetic product that utilizes high activity carbon monoxide hydrogenation catalysts and a heat transfer structure that surprisingly provides for higher per pass conversion with high selectivity for the desired synthetic product without thermal runaway.

Process for operating a highly productive tubular reactor

Method for stopping and restarting a Fischer-Tropsch process

The present technology is directed to processes involving formation of hydrocarbons and oxygenated hydrocarbons through use of oxygen supplied by ion transport membranes. More particularly, the present technology relates in part to a process involving steam reforming and subsequent production of a synthetic product where carbon dioxide and/or hydrogen downstream of the process is reclaimed to generate the synthetic product. The present technology also relates in part to an ethylene formation process involving a viral-templated coupling catalyst in the presence of an ion transport membrane.

Process for operating an integrated gas-to-liquids facility

Growing community of inventors

Dublin, OH, United States of America

Andre Peter Steynberg