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:
Jan. 06, 2009
Filed:
Jun. 04, 2003
Jean-marie Basset, Caluire, FR;
Philippe Bres, Marq en Bareul, FR;
Christophe Coperet, Lyons, FR;
Barry Martin Maunders, Surrey, GB;
Daravong Soulivong, Lyons, FR;
Mostafa Taoufik, Rillieux-la-Pape, FR;
Jean Thivolle-cazat, Fontaines-sur-Saone, FR;
Jean-Marie Basset, Caluire, FR;
Philippe Bres, Marq en Bareul, FR;
Christophe Coperet, Lyons, FR;
Barry Martin Maunders, Surrey, GB;
Daravong Soulivong, Lyons, FR;
Mostafa Taoufik, Rillieux-la-Pape, FR;
Jean Thivolle-Cazat, Fontaines-sur-Saone, FR;
BP Chemicals Limited, Middlesex, GB;
Abstract
The invention relates to a process for producing ethane comprising contacting methane with a metal catalyst selected from metal hydrides, metal organic compounds and mixtures thereof. It also relates to a process for the conversion of methane to carbon-containing products comprising contacting methane with a metal catalyst comprising at least one metal, Me, chosen from the lanthanides, the actinides and the metals from Groups 2 to 12 of the Periodic Table of the Elements, so as to produce ethane in a proportion of at least 65%, especially at least 98% or 99% by weight with respect to carbon-containing products formed in the process. The process can be a single-step process, preferably carried out under conditions involving a non-oxidative catalytic coupling of methane, in particular under operating conditions maintained substantially constant, preferably continuously, during the ethane production, e.g. at a temperature ranging from −30° C. to +80° C., preferably from 20° C. to 500° C., under a total absolute pressure ranging from 10to 100 MPa, preferably from 0.1 to 50 MPa. The metal catalyst may be chosen from metal catalysts supported on and preferably grafted to a solid support. One of the main advantages of the present invention is to produce ethane with a very high selectivity.