초록

Novel methods of electroless plating are described. Catalyst coatings can be applied within microchannel apparatus. Various reactions, including combustion and steam reforming, can be conducted over electroless catalyst coatings.

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1. A method of partially oxidizing a hydrocarbon, comprising: passing a process stream comprising a hydrocarbon and oxygen through a flow path at a temperature of at least 750° C. and a contact time of 10 ms or less;wherein the flow path is defined by channel walls;wherein at least one of the channe

1. A method of partially oxidizing a hydrocarbon, comprising: passing a process stream comprising a hydrocarbon and oxygen through a flow path at a temperature of at least 750° C. and a contact time of 10 ms or less;wherein the flow path is defined by channel walls;wherein at least one of the channel walls comprises a wall catalyst coating;wherein the wall catalyst coating comprises at least 3 mg/in2 Rh and at least 3 mg/in2 Pt; andconverting at least 80% of the oxygen and at least 10% of the hydrocarbon in the process stream and forming CO and water. 2. The method of claim 1 comprising operating the reaction for at least 500 continuous hours without regeneration, and further wherein the catalyst maintains essentially constant activity over the at least 500 hours of operation without regeneration. 3. The method of claim 2 wherein the wall catalyst coating comprises at least 5 mg/in2 Rh and at least 5 mg/in2 Pt and more than 15 mg/in2 (Pt+Rh). 4. The method of claim 1 wherein the hydrocarbon comprises methane, and methane conversion is at least about 75%. 5. The method of claim 4 wherein the temperature is 800° C. or less and the partial pressure of hydrocarbon is at least 0.071 atm. 6. The method of claim 1 wherein the wall catalyst coating comprises at least 5 mg/in2 Rh and at least 5 mg/in2 Pt and more than 15 mg/in2 (Pt+Rh). 7. The method of claim 1 wherein the wall catalyst coating comprises at least 0.6 mg/cm2 Rh. 8. The method of claim 1 wherein the wall catalyst coating is disposed on a metallic insertable substrate. 9. The method of claim 8 wherein the substrate has a height of less than 5 mm. 10. The method of claim 1 wherein the wall catalyst coating is disposed on a metallic substrate; wherein the metallic substrate comprises a layer of a metal aluminide. 11. The method of claim 10 further comprising a thermally grown oxide layer disposed on the metal aluminide. 12. The method of claim 1 wherein the process stream comprises 50-100 parts hydrocarbon, 35-60 parts CO, 120-150 parts H2, and 80-140 parts O2 . 13. The method of claim 1 wherein the channel is a microchannel and wherein the catalyst coating is contiguous over at least 5 cm of the microchannel. 14. The method of claim 1 where the oxygen selectivity of hydrocarbon to CO is the same or greater than the oxygen selectivity of CO to CO2. 15. The method of claim 1 wherein the wall catalyst coating comprises more than 10 mg/in2 (Pt+Rh). 16. The method of claim 15 wherein a hydrocarbon fuel is added at one end of a fuel subchannel and oxygen is added from an adjacent subchannel through holes along the length of the fuel subchannel, and further wherein the wall catalyst coating was formed by electroless plating. 17. A method of combusting a hydrocarbon comprising conducting the partial oxidation of claim 1 in a fuel rich zone followed by combustion in a fuel lean zone. 18. The method of claim 17 wherein contact time of hydrocarbon in the fuel rich zone is in the range of 2 to 5 msec. 19. The method of claim 17 wherein the fuel rich zone comprises H2 and wherein the partial pressure of H2 is in the range of 0.11 to 0.27 atm.