Uop Lcc

Phillips 66 Company

Mark Rumel Cragun

Keith W Hovis

Khalid Iqbal

Bruce B Randolph

Kristi A Fjare

Uchenna Prince Paul

Richard D Sadok

Jon M Nelson

Danielle Kristin Smith

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 system for alkylating hydrocarbons which includes an improved method of safely handling alkylation catalyst is disclosed. The process includes passing the alkylation catalyst from a settler vessel to a catalyst receiving vessel, via a catalyst cooler, for containment therein in the presence of a condensible gas. Also disclosed is a method for controlling the pressure in the catalyst receiving vessel by controlling the rate of removal of vapors.

Alkylation system with catalyst transfer

A system and/or process for alkylating hydrocarbons which includes an improved method of safely handling alkylation catalyst is disclosed. The process includes passing the alkylation catalyst from a settler vessel to a catalyst receiving vessel, via a catalyst cooler, for containment therein in the presence of a condensible gas. Also disclosed is a method for controlling the pressure in the catalyst receiving vessel by controlling the rate of removal of vapors.

Alkylation process with catalyst transfer

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Bartlesville, OK, United States of America

Mark Rumel Cragun