초록 ▼

Integrated Combustion Reactors (ICRs) and methods of making ICRs are described in which combustion chambers (or channels) are in direct thermal contact to reaction chambers for an endothermic reaction. Particular reactor designs are also described. Processes of conducting reactions in integrated com

Integrated Combustion Reactors (ICRs) and methods of making ICRs are described in which combustion chambers (or channels) are in direct thermal contact to reaction chambers for an endothermic reaction. Particular reactor designs are also described. Processes of conducting reactions in integrated combustion reactors are described and results presented. Some of these processes are characterized by unexpected and superior results, and/or results that can not be achieved with any prior art devices.

대표청구항 ▼

1. An integrated reactor, comprising: an exothermic microchannel comprising an exothermic reaction catalyst; an endothermic reaction microchannel adjacent the exothermic microchannel and comprising an endothermic reaction catalyst, the endothermic reaction catalyst having a length, in the direction

1. An integrated reactor, comprising: an exothermic microchannel comprising an exothermic reaction catalyst; an endothermic reaction microchannel adjacent the exothermic microchannel and comprising an endothermic reaction catalyst, the endothermic reaction catalyst having a length, in the direction of flow, of at least 10 cm; and a wall separating the exothermic reaction catalyst and the endothermic reaction catalyst; wherein a gap of at least 0.2 mm exists between a wall of the endothermic reaction microchannel and a surface of the endothermic reaction catalyst; wherein the endothermic reaction catalyst has a length of at least 17 cm. 2. The integrated reactor of claim 1 wherein the endothermic reaction microchannel has a height (the dimension perpendicular to flow and defining the shortest distance from the center of the endothermic reaction microchannel to the exothermic microchannel) of 0.5 mm or less. 3. The integrated reactor of claim 1 wherein the endothermic reaction catalyst is a catalyst insert and wherein spacers press the catalyst against the wall separating the exothermic reaction catalyst and the endothermic reaction catalyst. 4. The integrated reactor of claim 1 wherein the wall separating the exothermic and endothermic reaction catalysts is comprised of a nickel-based alloy. 5. The integrated reactor of 1 wherein the endothermic reaction microchannel comprises an endothermic reaction chamber having a height and/or width of about 2 mm or less. 6. The integrated reactor of 1 wherein the endothermic reaction catalyst comprises a steam reforming catalyst. 7. The integrated reactor of claim 1 wherein the endothermic reaction catalyst comprises a steam reforming catalyst, and wherein the exothermic reaction catalyst comprises a combustion catalyst. 8. An integrated reactor, comprising: an exothermic microchannel comprising an exothermic reaction catalyst; an endothermic reaction microchannel adjacent the exothermic microchannel and comprising an endothermic reaction catalyst, the endothermic reaction catalyst having a length, in the direction of flow, of at least 10 cm; and a wall separating the exothermic reaction catalyst and the endothermic reaction catalyst; wherein at least one wall defining the exothermic microchannel contains apertures connecting gas flow between the exothermic microchannel and an adjacent oxidant channel. 9. The integrated reactor of claim 8 wherein the exothermic reaction catalyst is a combustion catalyst. 10. The integrated reactor of claim 8 wherein the exothermic microchannel comprises a combustion chamber. 11. The integrated reactor of claim 10 wherein an exhaust chamber is located downstream of the combustion chamber and wherein the exhaust chamber comprises a combustion catalyst; and wherein the endothermic reaction catalyst is a steam reforming catalyst and wherein the endothermic reaction microchannel does not have a catalyst downstream of the steam reforming catalyst. 12. The integrated reactor of claim 8 wherein the endothermic reaction catalyst is a catalyst insert. 13. The integrated reactor of claim 8 wherein the endothermic reaction catalyst has a length of at least 17 cm. 14. The integrated reactor of claim 8 wherein the exothermic microchannel comprises a partial oxidation reaction chamber comprising a partial oxidation catalyst followed by a combustion chamber. 15. The integrated reactor of claim 8 comprising two exothermic microchannels that each have a u-bend and that merge into a single exhaust channel after the u-bend. 16. The integrated reactor of claim 8 comprising a flow stabilization feature disposed upstream of the first of the apertures. 17. The integrated reactor of claim 16 wherein the flow stabilization feature comprises a porous insert. 18. The integrated reactor of claim 8 wherein the endothermic reaction catalyst comprises a steam reforming catalyst.