Phillips 66 Company

Danielle Kristin Smith

Bruce B Randolph

Uchenna Prince Paul

Jon M Nelson

Neal Donald McDaniel

Kristi A Fjare

Richard D Sadok

Mark Rumel Cragun

Dennis Schultz

Mahaprasad Kar

Jimmy A Faria

A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200&#xb0; C. to about 375&#xb0; C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.

Process scheme for catalytic production of renewable hydrogen from oxygenate feedstocks

A method of steam reforming where a reaction occurs in which an oxygenated feed contacts a catalyst to produce hydrogen. The catalyst of the reaction comprises a metal/metal promoter on a nickel/transition metal blend catalyst supported on a high-energy lattice metal oxide.

Catalysts for renewable hydrogen production from oxygenated feedstocks

A method is taught of introducing an alternating voltage between a first electrode and a second electrode in a mixture comprising a depolarizing agent. The method then alternates between forming hydrogen gas at the first electrode while simultaneously oxidizing a depolarizing agent at the second electrode and forming hydrogen gas at the second electrode while simultaneously oxidizing the depolarizing agent at the first electrode.

Alternating voltage electrochemical reforming

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Bartlesville, OK, United States of America

Danielle Kristin Smith