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Catalyst compositions suitable for use in the exhaust gas recycle stream of an internal combustion engine are provided. Such catalyst compositions typically provide significant amounts of methane in addition to syngas. A reformer incorporating such a catalyst for use in an exhaust gas recycle portio

Catalyst compositions suitable for use in the exhaust gas recycle stream of an internal combustion engine are provided. Such catalyst compositions typically provide significant amounts of methane in addition to syngas. A reformer incorporating such a catalyst for use in an exhaust gas recycle portion of an internal combustion engine powertrain is described. A powertrain incorporating such a reformer, a method of increasing the octane rating of an exhaust gas recycle stream, and a method of operating an internal combustion engine using methane-assisted combustion are also described.

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1. A method of operating an internal combustion engine using methane-assisted combustion, comprising: (a) providing an exhaust gas-containing mixture to an exhaust gas recycle reformer; the exhaust gas-containing mixture comprising recycled exhaust gas and a first hydrocarbon-containing fuel;(b) con

1. A method of operating an internal combustion engine using methane-assisted combustion, comprising: (a) providing an exhaust gas-containing mixture to an exhaust gas recycle reformer; the exhaust gas-containing mixture comprising recycled exhaust gas and a first hydrocarbon-containing fuel;(b) converting at least a portion of the exhaust gas-containing mixture in the presence of heat and a catalyst composition to a reformed gaseous mixture comprising CH4, CO, CO2, H2O, N2, and H2, said CH4 being present at a concentration greater than about 1.0 mol % CH4, based on the total moles of gas in the reformed gaseous mixture, said catalyst composition comprises a hydrocarbon-reforming catalyst, the catalyst composition having a hydrocarbon-reforming catalyst loading from 1.0 wt % to 10.0 wt %, based on the total weight of the catalyst composition, the metal of the hydrocarbon-reforming catalyst being rhodium or a combination of rhodium and platinum or a combination of rhodium and ruthenium;(c) introducing at least a portion of the reformed gaseous mixture and a second hydrocarbon-containing fuel into the engine, wherein said second hydrocarbon-containing fuel may be the same or different from the first hydrocarbon-containing fuel;(d) combusting the at least a portion of the reformed gaseous mixture and second hydrocarbon-containing fuel in the engine to form an exhaust gas, the exhaust gas comprising a first portion of the exhaust gas and a second portion of the exhaust gas; and(e) passing a first portion of the exhaust gas through a first heat exchanger to extract heat from the first portion of the exhaust gas, the recycled exhaust gas comprising the second portion of the exhaust gas. 2. The method of claim 1, wherein the first hydrocarbon-containing fuel comprises about 2.0 mol % or less of CH4. 3. The method of claim 1, further including prior to introducing the reformed gaseous mixture into the internal combustion engine, cooling the gaseous mixture by passing the gaseous mixture through the first heat exchanger or a second heat exchanger. 4. The method of claim 1, wherein providing the exhaust gas-containing mixture to the reformer does not substantially include providing an oxygen-containing gas other than engine exhaust gas and a first hydrocarbon-containing fuel. 5. The method of claim 1, wherein the catalyst composition further comprises a metal oxide composition, the metal oxide composition being selected from aluminum oxides, silicon oxides, rare-earth metal oxides, Group IV metal oxides, and mixtures thereof. 6. The method of claim 5, wherein the metal oxide composition comprises a mixture of an aluminum-containing oxide and a cerium-containing oxide. 7. The method of claim 1, wherein the catalyst composition further comprises at least one medium pore molecular sieve or large pore molecular sieve. 8. The method of claim 1, wherein the catalyst composition further comprises ZSM-5, phosphorus-modified ZSM-5, MCM-68, or a combination thereof. 9. The method of claim 1, wherein providing an exhaust gas-containing mixture to an exhaust gas recycle reformer comprises: passing at least a portion of the first hydrocarbon-containing fuel into a cylinder of the engine after the combusting of the reformed gaseous mixture and second hydrocarbon-containing fuel to form a portion of the exhaust gas;cracking the at least a portion of the first hydrocarbon-containing fuel in the cylinder to form a cracked hydrocarbon-containing fuel; andproviding the portion of the exhaust gas and the cracked hydrocarbon-containing fuel to the exhaust gas recycle reformer. 10. The method of claim 1, further comprising pre-combusting a portion of exhaust gas-containing mixture prior to providing the exhaust gas-containing mixture to the exhaust gas recycle reformer, the exhaust gas recycle reformer having a reformer inlet temperature of about 525° C. to about 625° C. 11. A method of increasing the octane rating of an internal combustion engine exhaust gas stream, said method comprising: (a) providing an exhaust gas-containing mixture to an exhaust gas recycle reformer; the exhaust gas-containing mixture comprising recycled exhaust gas and a first hydrocarbon-containing fuel, said exhaust gas-containing mixture containing about 3.0 mol % of CH4 or less and having an initial octane rating of less than 93 RON; and(b) in the presence of a catalyst composition comprising a hydrocarbon-reforming catalyst, the catalyst composition having a hydrocarbon-reforming catalyst loading from 1.0 wt % to 10.0 wt %, based on the total weight of the catalyst composition, the metal of the hydrocarbon-reforming catalyst being rhodium or a combination of rhodium and platinum or a combination of rhodium and ruthenium, converting under reforming conditions at least a portion of the exhaust gas-containing mixture to a reformed gaseous mixture having a second octane rating (RON) from 100 to 125, the reformed gaseous mixture comprising H2, CO, CO2, H2O, N2, and greater than about 1.0 mol % CH4 based on the total moles of gas in the reformed gaseous mixture. 12. The method of claim 11, wherein said converting supplies heat sufficient to maintain the reformer at an average reformer temperature above about 450° C. 13. The method of claim 11, wherein the catalyst composition further comprises a metal oxide composition, the metal oxide composition being selected from aluminum oxides, silicon oxides, rare-earth metal oxides, Group IV metal oxides, mixtures of an aluminum-containing oxide and a cerium-containing oxide, and mixtures thereof. 14. The method of claim 11, wherein the catalyst composition further comprises at least one medium pore molecular sieve or large pore molecular sieve, the at least one medium pore molecular sieve or large pore molecular sieve preferably being ZSM-5, phosphorus-modified ZSM-5, MCM-68, or a combination thereof. 15. The method of claim 11, wherein providing an exhaust gas-containing mixture to an exhaust gas recycle reformer comprises: passing at least a portion of the first hydrocarbon-containing fuel into a cylinder of the engine after the combusting of the reformed gaseous mixture and second hydrocarbon-containing fuel to form a portion of the exhaust gas;cracking the at least a portion of the first hydrocarbon-containing fuel in the cylinder to form a cracked hydrocarbon-containing fuel; andproviding the portion of the exhaust gas and the cracked hydrocarbon-containing fuel to the exhaust gas recycle reformer. 16. The method of claim 11, further comprising pre-combusting a portion of exhaust gas-containing mixture prior to providing the exhaust gas-containing mixture to the exhaust gas recycle reformer, the exhaust gas recycle reformer having a reformer inlet temperature of about 525° C. to about 625° C.