The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.
The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.
Patent No.:
Date of Patent:
May. 27, 1980
Filed:
Dec. 18, 1978
Howard L Mitchell, III, Baton Rouge, LA (US);
Robert H Waghorne, Baton Rouge, LA (US);
Exxon Research & Engineering Co., Florham Park, NJ (US);
Abstract
Novel regenerable catalyst-reagents, and a new and improved process utilizing said regenerable catalyst-reagents, for the conversion, and oligomerization of hydrocarbons, notably methane, at relatively low temperatures to produce products rich in ethylene or benzene, or both, usually in admixture with other hydrocarbons; and process for the regeneration of said catalyst-reagents. (a) The catalyst-reagents are multi-functional and are comprised of (1) a Group VIII noble metal having an atomic number of 45 or greater, nickel, or a Group 1-B noble metal having an atomic number of 47 or greater; (2) a Group VI-B metal oxide which is capable of being reduced to a lower oxide, or admixture of metal oxides which includes one or more of such metal oxides; and, (3) a Group II-A metal or alkaline-earth metal, composited with a suitably passivated, spinel-coated refractory support, notably an inorganic oxide support, preferably alumina. (b) The process is one wherein a hydrocarbon feed, notably methane, is contacted and reacted with a catalyst-reagent as characterized in (a), supra, at temperature ranging from about 1150.degree. F. to about 1600.degree. F.; and also embodies (c) a process for regeneration of said catalyst-reagent which has become inactivated as by use in the process characterized in (b), supra, by contact thereof in an exothermic reaction with water, oxygen or an oxygen-containing gas, preferably air, at temperatures sufficient to reoxidize the Group VI-B metal oxide, and preferably also sufficient to provide the required sensible heat for the operation of said novel hydrocarbon conversion process (b), supra, on recycle of the catalyst-reagent.