The University of Texas System

Wen-Long Jang

Richard B Timmons

Yigong He

David J Houpt, Jr

A novel catalytic process involving complete hydrodehalogenation of halogenated aliphatic hydrocarbons in the presence of a hydrogen donor and a modified zeolite catalyst has been developed. The process is operated in a continuous flow mode and reaction products consist exclusively of hydrogen halide and hydrocarbons. The relative ratio of paraffins to olefins to aromatics obtained in the product distribution is a strong function of the ratio of hydrogen to reactant and the space velocity and temperature employed. The catalyst employed is a nickel metal modified shape selective zeolite that takes advantage of the hydrogenolysis ability of nickel and the acidic-shape selective properties of the zeolite.

Catalytic hydrodehalogenation of polyhalogenated hydrocarbons

The invention relates to an efficient process for the production of higher hydrocarbon from the catalyzed conversion of acetylene. This invention describes the use of a nickel or cobalt-containing zeolite catalyst, coupled with the addition of a hydrogen donor co-reactant to the acetylene feed, to obtain continuous and complete conversion of acetylene to other hydrocarbons. The catalyst/reactant feed process described eliminates rapid catalyst deactivation.

Growing community of inventors

Arlington, TX, United States of America

Wen-Long Jang