Catalyst and process for the production of olefins
View Patent ↗A catalyst system capable of supporting combustion beyond the fuel rich limit of flammability comprising a catalytic component, a first support and a second support and wherein the catalytic component is present on both the first and the second support, and a process for the production of an olefin, said process comprising passing a mixture of a hydrocarbon and an oxygen-containing gas over said catalyst system to produce said olefin. The first support and the second support must differ in at least one of the following aspects: support material, support type and/or structural dimension.
1. A process for the production of an olefin, said process comprising passing a mixture of a hydrocarbon and an oxygen-containing gas over a catalyst system capable of supporting combustion beyond the fuel rich limit of flammability, which catalyst system comprises a catalytic component, a first support and a second support, wherein the catalytic component is present on both the first and the second support, wherein the first support and second support differ in at least one of support material, support type and/or support structural dimension and wherein the first and/or second supports are in the form of ceramic foam or ceramic monolith and comprise a series of blocks or layers which are arranged such that they tessellate together to leave no gaps, the blocks or layers being tiled within a reactor in different directions in a manner such that tiles of a layer either above or below do not exactly overlap with any neighboring layer.
2. A process as claimed in claim 1 , wherein hydrogen is co-fed with the hydrocarbon and oxygen-containing gas into the reactor.
3. A process as claimed in claim 1 , wherein the catalytic component comprises a Group VIIIB metal.
4. A process as claimed in claim 1 , wherein the first support and the second support have different structural dimensions.
5. A process as claimed in claim 1 , wherein the first support is formed from the same material and has the same structural dimensions as the second support, but the supports are of different support types.
6. A process as claimed in claim 1 , wherein one support is located upstream of the other with respect to the directional flow of reactants.
7. A process as claimed in claim 6 , wherein the first support is located in a reactor upstream of the second support with respect to the directional flow of the reactants, and the first support provides a higher pressure drop per unit length (in the direction of flow of the reactants) than the second support.
8. A process as claimed in claim 6 , wherein the first support is located in a reactor upstream of the second support with respect to the directional flow of the reactants and down the sides of the second support.
9. A process as claimed in claim 7 , wherein the first support is a foam and the second support is a monolith, and the first support is located in a reactor upstream of the second support with respect to the directional flow of reactants.
10. A process as claimed in claim 7 , wherein the first support is a porous foam comprising small pores and the second support is a foam comprising larger pores, and the first support is located in a reactor upstream of the second support with respect to the directional flow of reactants.
11. A process as claimed in claim 1 , wherein a non catalytic resistance zone is located upstream of the catalyst system.
12. A process as claimed in claim 1 , wherein the ratio of hydrocarbon to oxygen-containing gas is 5 to 16 times the stoichiometric ratio of hydrocarbon to oxygen-containing gas required for complete combustion of the hydrocarbon to carbon dioxide and water.
13. A catalyst system capable of supporting combustion beyond the fuel rich limit of flammability comprising a catalytic component, a first support and a second support, wherein the catalytic component is present on both the first support and the second support, wherein the first support and second support differ in at least one of support material, support type and/or support structural dimension and further wherein the first and/or second supports are in the form of a ceramic foam or ceramic monolith and comprise a series of blocks or layers which are arranged such that they tessellate together to leave no gaps and the blocks or layers are tiled within a reactor in different directions in a manner such that tiles of a layer either above or below do not exactly overlap with any neighboring layer.
14. A catalyst system as claimed in claim 13 , wherein first support and the second support have different structural dimensions.
15. A process as claimed in claim 4 , wherein the first support is formed from the same material and is of the same support type as the second support.
16. A catalyst system as claimed in claim 15 , wherein the first support is formed from the same material and is of the same support type as the second support.