초록 ▼

A compact integrated combustion reactor is described. In a preferred embodiment, the combustion catalyst is disposed in a staggered configuration such that the hot spot in an adjacent endothermic reaction chamber is substantially less than would occur with a conventional, unstaggered configuration.

A compact integrated combustion reactor is described. In a preferred embodiment, the combustion catalyst is disposed in a staggered configuration such that the hot spot in an adjacent endothermic reaction chamber is substantially less than would occur with a conventional, unstaggered configuration. The integrated reactor may also include a methanation chamber for methanation of a reformate product. Systems containing reactant and product streams, and methods of conducting integrated combustion reactions are also described. A staggered catalyst conformation can be used more broadly for thermal chemical reactions requiring heat transfer in a layered device.

대표청구항 ▼

1. A compact steam reformer, comprising: a reactant preheat section;a steam reforming reaction chamber comprising a steam reforming catalyst; wherein the steam reforming reaction chamber is in conductive thermal contact with the reactant preheat section such that, during operation, heat from the ste

1. A compact steam reformer, comprising: a reactant preheat section;a steam reforming reaction chamber comprising a steam reforming catalyst; wherein the steam reforming reaction chamber is in conductive thermal contact with the reactant preheat section such that, during operation, heat from the steam reforming reaction chamber can be conducted directly across a reaction chamber wall into the reactant preheat section;wherein the reactant preheat section comprises an inlet and an outlet, and wherein the reactant preheat section outlet is disposed such that, during operation, flow from the reactant preheat section outlet flows into the steam reforming reaction chamber;a combustion chamber adjacent to the steam reforming reaction chamber and separated from the steam reforming reaction chamber by a chamber wall; wherein the combustion chamber comprises a combustion catalyst and wherein the combustion chamber has a length and wherein the combustion chamber length is defined in the direction of flow through the combustion chamber, and begins at a point where flow first encounters catalyst and ends where flow last encounters catalyst; anda combustion preheat chamber; wherein the combustion chamber is in conductive thermal contact with the combustion preheat section such that, during operation, heat from the combustion chamber can be conducted through a combustion chamber wall into the combustion preheat section;wherein the combustion chamber comprises an inlet and an outlet, and wherein the combustion chamber outlet is disposed such that, during operation, flow from the combustion chamber outlet flows into the combustion preheat section. 2. The compact steam reformer of claim 1 further comprising a methanation catalyst disposed in the reactant preheat section. 3. The compact steam reformer of claim 1 wherein the reactant preheat section comprises methanator, vaporizer and superheat subsections. 4. The compact steam reformer of claim 1 comprising a stack of layers, comprising the following layers in sequential order: a methanation layer comprising a methanation catalyst;a vaporizer layer;a superheat layer;the steam reforming reaction chamber;the combustion chamber; anda preheater layer. 5. The compact steam reformer of claim 4 comprising at least 3 preheat layers in the combustion preheat chamber. 6. A compact steam reformer, comprising: a reactant preheat section;a steam reforming reaction chamber comprising a steam reforming catalyst; wherein the steam reforming reaction chamber is in conductive thermal contact with the reactant preheat section such that, during operation, heat from the steam reforming reaction chamber can be conducted directly across a reaction chamber wall into the reactant preheat section;wherein the reactant preheat section comprises an inlet and an outlet, and wherein the reactant preheat section outlet is disposed such that, during operation, flow from the reactant preheat section outlet flows into the steam reforming reaction chamber;a combustion chamber adjacent to the steam reforming reaction chamber and separated from the steam reforming reaction chamber by a chamber wall; wherein the combustion chamber comprises a combustion catalyst; anda combustion preheat chamber; wherein the combustion chamber is in conductive thermal contact with the combustion preheat section such that, during operation, heat from the combustion chamber can be conducted through a combustion chamber wall into the combustion preheat section;wherein the combustion chamber comprises an inlet and an outlet, and wherein the combustion chamber outlet is disposed such that, during operation, flow from the combustion chamber outlet flows into the combustion preheat sectionwherein the combustion channel has a height of 10 mm or less and wherein the combustion comprises a combustion catalyst staggered over the width of the combustion chamber, such that, at the beginning of the combustion chamber's length, catalyst is present in no more than 70% of the combustion chamber's width. 7. The compact steam reformer of claim 1 wherein the steam reforming reaction chamber comprises a catalyst comprising CuZnAl, Pd/ZnO, Ru, Pt, Rh, or combinations of these. 8. The compact steam reformer of claim 2 wherein a preheat layer is disposed between the steam reforming reaction chamber and a methanation layer that comprises the methanation catalyst. 9. The compact steam reformer of claim 8 wherein the methanation catalyst comprises Ru on an alumina support. 10. The compact steam reformer of claim 9 wherein the steam reforming reaction chamber comprises a catalyst having a porosity of at least 80%. 11. A prebonded assembly having the structure of the compact steam reformer of claim 1. 12. A compact steam reformer system, comprising the compact steam reformer of claim 1 comprising alcohol and steam flowing through the reactant preheat section and hydrogen flowing through the reactant preheat section. 13. The compact steam reformer system of claim 12 comprising alcohol and steam flowing through the reactant preheat section and hydrogen flowing through the reactant preheat section. 14. A method of producing H2 comprising passing CO and H2O into the compact steam reformer of claim 1. 15. The method of claim 14 wherein the combustion chamber has a volume/power ratio of 0.017 ml/We or less. 16. The method of claim 14 wherein the integrated steam reformer has a volume/power ratio of 0.82 ml/We or less. 17. The method of claim 14, comprising: passing a reactant stream comprising a hydrogen source and water into the reactant preheat section and through a preheat layer in the reactant preheat section and then into the steam reforming reaction section where the hydrogen source and water react to form a product stream comprising H2;passing the product stream comprising H2 through a layer parallel to the preheat layer and transferring heat through a wall from the product stream to the reactant stream;passing a combustant stream comprising a fuel and an oxidant into the combustion preheat section and through a preheat layer in the combustion preheat section and then into the combustion chamber where the fuel and oxidant combust to form an exhaust stream;wherein heat from the combustion passes through a wall into the steam reforming reaction section; andpassing the exhaust stream through a layer parallel to the preheat layer and transferring heat through a wall from the exhaust stream to the combustant stream. 18. Laminated apparatus for integrated thermal reaction, comprising the following layers in stacked in sequential order: an endothermic preheat layer;an endothermic reaction chamber;an exothermic reaction chamber; andan exothermic preheat layer;wherein a reaction chamber wall separates the endothermic reaction chamber and the exothermic reaction chamber;wherein a first fluid flow path connects the endothermic preheat layer with the endothermic reaction chamber; andwherein a second fluid flow path connects the exothermic preheat layer with the exothermic reaction chamberwherein the endothermic reaction chamber comprises a steam reformer and includes a steam reforming catalyst, andwherein the exothermic reaction chamber comprises a combustion chamber and includes a combustion catalyst. 19. The laminated apparatus of claim 18 further comprising a methanator connected to the first fluid path. 20. The laminated apparatus of claim 18 further comprising a preferential oxidation chamber connected to the first fluid path. 21. A method of conducting thermal chemical reactions in the apparatus of claim 18, comprising: passing a first reactant stream into and through the endothermic preheat layer and then into the endothermic reaction chamber wherein the reactant reacts endothermically to form an endothermic product stream;passing the endothermic product stream into a heat transfer layer that is adjacent to the endothermic preheat layer and passing heat from the endothermic product stream into the reactant stream through a wall that separates the heat transfer layer from the endothermic preheat layer; and simultaneously,passing a second reactant stream into and through the exothermic preheat layer and then into the exothermic reaction chamber wherein the reactant reacts exothermically to form an exothermic product stream;passing the exothermic product stream into a heat transfer layer that is adjacent to the exothermic preheat layer and passing heat from the exothermic product stream into the second reactant stream through a wall that separates the heat transfer layer from the endothermic preheat layer; andwherein heat from the exothermic reaction is conducted into the endothermic reaction chamber through a reaction chamber wall that separates the enothermic reaction chamber and the exothermic reaction chamber. 22. The method of claim 21 wherein the endothermic reaction comprises steam reforming; wherein the exothermic reaction comprises combustion; wherein the laminated apparatus comprises a preferential reaction chamber in the first fluid flow path; wherein the endothermic product stream comprises CO and flows into the preferential reaction chamber wherein at least a portion of the CO is converted to CO2. 23. The method of claim 17 wherein the product stream comprising H2 has an H2:CO ratio of at least 70. 24. The method of claim 17 wherein the product stream comprising H2 has an H2:CO ratio in the range of 100 to 100,000. 25. The method of claim 14 wherein the combustion chamber has a volume/power ratio of 0.011 ml/We or less. 26. The method of claim 14 wherein the combustion chamber has a volume/power ratio in the range of 0.007 and 0.004 ml/We. 27. The method of claim 14 wherein the integrated steam reformer has a volume/power ratio of 0.55 ml/We or less. 28. The method of claim 17 wherein the reforming chamber has a volume/power ratio of 0.03 ml/We or less.