초록 ▼

Methods have been developed to form catalysts having active metals disposed on a carbon nanotube coated porous substrate. Catalysts and reactions over nanotube-containing catalysts are also disclosed. Results are presented showing enhanced performance resulting from use of the inventive catalyst. M

Methods have been developed to form catalysts having active metals disposed on a carbon nanotube coated porous substrate. Catalysts and reactions over nanotube-containing catalysts are also disclosed. Results are presented showing enhanced performance resulting from use of the inventive catalyst. Mesoporous oxide layers can be utilized to improve catalyst properties.

대표청구항 ▼

We claim: 1. A method of conducting a catalyzed chemical reaction, comprising: passing at least one reactant into an engineered catalyst wherein the catalyst comprises a support material having through-porosity; a layer comprising carbon nanotubes disposed over the support material; an oxide layer

We claim: 1. A method of conducting a catalyzed chemical reaction, comprising: passing at least one reactant into an engineered catalyst wherein the catalyst comprises a support material having through-porosity; a layer comprising carbon nanotubes disposed over the support material; an oxide layer disposed between the support and the layer comprising carbon nanotubes; and a surface-exposed catalyst composition; and wherein the support material has an average pore size, as measured by microscopy, of at least 1 micrometer (μm); and reacting the at least one reactant within the catalyst to form a product. 2. A method of converting a chemical reactant, comprising: passing at least one reactant into a reaction chamber; wherein an engineered catalyst is disposed within the reaction chamber; wherein the engineered catalyst comprises a support material having through-porosity; a layer comprising carbon nanotube disposed over the support material; an oxide layer disposed between the support and the layer comprising carbon nanotubes; and a surface-exposed catalyst composition; and reacting the at least one reactant in the reaction chamber to produce at least one product. 3. The method of claim 2 wherein the reaction chamber has an interior with a cross-sectional area and the engineered catalyst occupies at least 80% of said cross-sectional area. 4. The method of claim 3 wherein the reaction chamber is a microcharmel and the engineered catalyst comprises a monolith. 5. The method of claim 2 wherein the reaction chamber comprises an array of microchannels wherein each of the microchannels in said array comprises the engineered catalyst. 6. The method of claim 5 wherein the array of microchannels is in thermal contact with at least one microchannel heat exchanger. 7. The method of claim 2, wherein the engineered catalyst has a volume of at least 5 mm3. 8. The method of claim 2 wherein the catalyst contains 0.1 to 20 weight % carbon. 9. A method of converting a chemical reactant, comprising: passing at least one reactant into a reaction chamber; wherein an engineered catalyst is disposed within the reaction chamber, wherein the engineered catalyst comprises: a support, carbon nanotubes disposed over said support, an oxide layer disposed over the nanotubes, and a catalyst composition disposed over the oxide layer; and reacting the at least one reactant in the a reaction chamber to produce at least one product. 10. The method of claim 9 wherein the at least one reactant is in liquid solution. 11. The process of claim 1 wherein the gaseous composition contacts the catalyst for 250 ms or less. 12. The process of claim 1 wherein the support comprises a honeycomb, foam or felt. 13. The method of claim 9 wherein the support comprises a honeycomb, foam or felt. 14. The method of claim 1 wherein the support material is a metal. 15. The method of claim 2 wherein the support material comprises cordierite, silica, alumina, rutile, mullite, zirconia, silicon carbide, aluminosilicate, stabilized zirconia, steel or alumina-zirconia blend. 16. The method of claim 1 wherein at least 80% of the carbon in the catalyst is in the form of carbon nanotubes having a length of 5 to 200 μm. 17. The method of claim 1 wherein the carbon nanotubes comprise clumps of aligned carbon nanotubes. 18. The method of claim 9 wherein the carbon nanotubes comprise clumps of aligned carbon nanotubes. 19. The method of claim 5 wherein the method of converting a chemical reactant, comprises a reaction selected from the group consisting of: acetylation, addition reactions, alkylation, dealkylation, hydrodealkylation, reductive alkylation, amination, aromatization, arylation, carbonylation, decarbonylation, reductive carbonylation, carboxylation, reductive carboxylation, reductive coupling, condensation, cracking, hydrocracking, cyclization, cyclooligomerization, dehalogenation, dimerization, epoxidation, esterification, exchange, halogenation, hydrohalogenation, homologation, hydration, dehydration, hydrogenation, dehydrogenation, hydrocarboxylation, hydroformylation, hydrogenolysis, hydrometallation, hydrosilation, hydrolysis, hydrotreating, hydrodesulferization/hydrodenitrogenation (HDS/HDN), isomerization, methanol synthesis, methylation, demethylation, metathesis, nitration, partial oxidation, polymerization, reduction, steam and carbon dioxide reforming, sulfonation, telomerization, transesterification, trimerization, water gas shift (WGS), and reverse water gas shift (RWGS). 20. The method of claim 9 wherein the method of converting a chemical reactant, comprises a reaction selected from the group consisting of: acetylation, addition reactions, alkylation, dealkylation, hydrodealkylation, reductive alkylation, amination, aromatization, arylation, carbonylation, decarbonylation, reductive carbonylation, carboxylation, reductive carboxylation, reductive coupling, condensation, cracking, hydrocracking, cyclization, cyclooligomerization, dehalogenation, dimerization, epoxidation, esterification, exchange, halogenation, hydrohalogenation, hornologation, hydration, dehydration, hydrogenation, dehydrogenation, hydrocarboxylation, hydroformylation, hydrogenolysis, hydrometallation, hydrosilation, hydrolysis, hydrotreating, hydrodesulferization/hydrodenitrogenation (HDS/HDN), isomerization, methanol synthesis, methylation, demethylation, metathesis, nitration, partial oxidation, polymerization, reduction, steam and carbon dioxide reforming, sulfonation, telomerization, transesterification, trimerization, water gas shift (WGS), and reverse water gas shift (RWGS). 21. The method of claim 1 wherein a mesoporous thin silica film is disposed between the support and the layer of nanotubes. 22. The method of claim 9 wherein the engineered catalyst comprises an oxide layer disposed between the support and the carbon nanotubes. 23. The method of claim 3 wherein the catalyst has a pore volume of 30 to 95%, and at least 50% of the catalyst's pore volume is comprised of pores in the size range of 0.3 to 200 microns. 24. The method of claim 9 wherein the reaction chamber has an interior with a cross-sectional area and the engineered catalyst occupies at least 80% of said cross-sectional area. 25. The method of claim 2, comprising: passing the at least one reactant into at least 10 reaction chambers in an integrated chemical reactor; wherein the at least 10 reaction chambers comprise the engineered catalyst. 26. The method of claim 25 wherein the integrated chemical reactor further comprises microchannel heat exchangers. 27. The method of claim 25 wherein the at least 10 reaction chambers are connected in parallel and wherein each of the at least 10 reaction chambers has a height and/or width of 2 mm or less. 28. The method of claim 25 wherein the integrated chemical reactor further comprises second reaction chambers that are adjacent to the at least 10 reaction chambers such that heat from an exothermic reaction in one reaction chamber is transferred to an endothermic reaction in an adjacent reaction chamber. 29. The method of claim 9, comprising: passing the at least one reactant into at least 10 reaction chambers in an integrated chemical reactor; wherein the at least 10 reaction chambers comprise the engineered catalyst.