초록 ▼

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 metha

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 10-3 to 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.

대표청구항 ▼

The invention claimed is: 1. A process for producing ethane comprising bringing a stream consisting essentially of methane into contact with a metal catalyst selected from the group consisting of metal hydrides, metal organic compounds and mixtures thereof at the operating conditions for methane co

The invention claimed is: 1. A process for producing ethane comprising bringing a stream consisting essentially of methane into contact with a metal catalyst selected from the group consisting of metal hydrides, metal organic compounds and mixtures thereof at the operating conditions for methane conversion. 2. The process according to claim 1, wherein the metal catalyst comprises at least one metal selected from the group consisting of lanthanides, the actinides and the metals from Groups 2 to 12 of the Periodic Table of the Elements. 3. A process for the conversion of methane to carbon-containing products comprising bringing a stream consisting essentially of methane into contact with a metal catalyst comprising at least one metal selected from the group consisting of 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% by weight with respect to carbon-containing products formed in the process. 4. The process according to claim 3, wherein the ethane is produced in a proportion of at least 70% by weight with respect to carbon-containing products formed in the process. 5. The process according to claim 3 or 4, wherein the metal catalyst is selected from the group consisting of metal hydrides, metal organic compounds and mixtures thereof. 6. The process according claim 1 or 3, wherein the process is carried out under conditions involving a non-oxidative coupling of methane. 7. The process according to claim 1 or 3, wherein the process is a single-stage process. 8. The process according to claim 1 or 3, wherein the process is carried out with operating conditions maintained substantially constant during the ethane production. 9. The process according to claim 1 or 3, wherein the process is carried out under a total absolute pressure ranging from 10-3 to 100 MPa. 10. The process according to claim 1 or 3, wherein the process is carried out at a temperature ranging from-30° C. to +800° C. 11. The process according to claim 1 or 3, wherein the process is carried out in the presence of one or more inert agents. 12. The process according to claim 1 or 3, wherein the metal catalyst is supported on a solid support. 13. The process according to claim 12, wherein the solid support is selected from the group consisting of metal oxides, refractory oxides, molecular sieves, sulphated metal oxides, sulphated refractory oxides, metal sulphides, refractory sulphides, sulphided metal oxides, sulphided refractory oxides and azides. 14. The process according to claim 1 or 3, wherein the metal of the metal catalyst is at least one metal selected from the group consisting of yttrium, scandium, lanthanum, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, rhenium, iron, ruthenium, cobalt, rhodium, iridium, nickel, palladium, platinum, cerium and neodymium. 15. The process according to claim 14, wherein the metal is at least one metal selected from the group consisting of yttrium, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, ruthenium, rhodium and platinum. 16. The process according to claim 15, wherein the metal is at least one metal selected from the group consisting of yttrium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, ruthenium, rhodium and platinum. 17. The process according to claim 1 or 3, wherein the process is carried out in the gas phase in a reactor. 18. The process according to claim 17, wherein the metal catalyst is used in a solid form, essentially forming the bed of the reactor. 19. The process according to claim 1 or 3, wherein the process comprises adding the methane to the metal catalyst, or adding the metal catalyst to the methane, or simultaneously mixing the methane and the metal catalyst.