Steam reforming
A process is described for steam reforming a hydrocarbon feedstock, comprising passing a mixture of the hydrocarbon feedstock and steam through a catalyst bed comprising a particulate nickel steam reforming catalyst and a structured nickel steam reforming catalyst disposed within a plurality of externally heated tubes in a tubular steam reformer, wherein each tube has an inlet to which the mixture of hydrocarbon and steam is fed, an outlet from which a reformed gas containing hydrogen, carbon monoxide, carbon dioxide, steam and methane is recovered, and the steam reforming catalyst at the outlet of the tubes is the structured steam reforming catalyst, wherein the particulate steam reforming catalyst comprises 5 to 30% by weight nickel, and the structured steam reforming catalyst comprises nickel dispersed over the surface of a porous metal oxide present as a coating on a non-porous metal or ceramic structure.
1 . A process for steam reforming a hydrocarbon feedstock, comprising passing a mixture of the hydrocarbon feedstock and steam through a catalyst bed comprising a particulate steam reforming catalyst and a structured steam reforming catalyst disposed within a plurality of externally heated tubes in a tubular steam reformer, wherein each tube has an inlet to which the mixture of the hydrocarbon feedstock and the steam is fed, an outlet from which a reformed gas containing hydrogen, carbon monoxide, carbon dioxide, steam and methane is recovered, and the steam reforming catalyst at the outlet of the tubes is the structured steam reforming catalyst, wherein the particulate steam reforming catalyst comprises 5 to 30% by weight nickel, expressed as NiO, and has a largest dimension that is at most 15% of the internal diameter of the plurality of tubes, and the structured steam reforming catalyst comprises nickel dispersed over the surface of a porous metal oxide present as a coating on a non-porous metal or ceramic structure, wherein the nickel content of the coating of the porous metal oxide, as expressed as NiO, is in the range of 5 to 50% by weight and the thickness of the coating of the porous metal oxide is in the range of 5 to 150 micrometres, wherein the plurality of the externally heated tubes consists of three layers of nickel steam reforming catalyst: a structured steam reforming catalyst layer at inlets of the plurality of the externally heated tubes, another structured steam reforming catalyst layer at outlets of the plurality of the externally heated tubes, and a particulate steam reforming catalyst layer located in between these two structured stream reforming catalyst layers, and a structured steam reforming catalyst layer at outlets of the plurality of the externally heated tubes.
2 . The process according to claim 1 wherein the hydrocarbon feedstock comprises methane, a pre-reformed gas, an associated gas or natural gas.
3 . The process according to claim 1 , wherein the tubular steam reformer contains the plurality of the externally heated tubes through which the mixture of the hydrocarbon feedstock and steam is passed, and to which heat is transferred by means of a hot gas comprising a combustion gas or a synthesis gas, flowing around the plurality of the externally heated tubes.
4 . The process according to claim 1 , wherein the structured steam reforming catalyst comprises metal or ceramic structures having a plurality of passages through which a process fluid may pass in ordered, non-random directions.
5 . The process according to claim 1 , wherein the structured steam reforming catalyst comprises cylindrical units with a diameter complimentary to the plurality of the externally heated tubes in which they are placed, comprising a plurality of passages through which a process fluid may pass in ordered, non-random directions.
6 . The process according to claim 1 , wherein the particulate steam reforming catalyst comprises an alkali metal oxide, in an amount in the range of 0.5 to 7.0% by weight on the particulate steam reforming catalyst.
7 . The process according to claim 1 , wherein the largest dimension of the particulate steam reforming catalyst is in the range of 3 to 15% of the internal diameter of the plurality of the externally heated tubes in which it is placed.
8 . The process according to claim 1 , wherein the particulate steam reforming catalyst is a pelleted steam reforming catalyst.
9 . The process according to claim 1 , wherein the particulate steam reforming catalyst is cylindrical with a diameter in the range 3 to 10 mm or 5 to 25 mm and a length in the range 2 to 15 mm or 5 to 25 mm and an aspect ratio in the range of 1:0.5 to 2:1.
10 . The process according to claim 1 , wherein the particulate steam reforming catalyst comprises 3 to 10 through holes and optionally 3 to 12 flutes or lobes around the periphery of the pellet.
11 . The process according to claim 9 , wherein the particulate steam reforming catalyst is cylindrical with an aspect ratio in the range of 0.75 to 1.0 and the ratio of the internal diameter of the plurality of the externally heated tubes to the diameter of the particulate steam reforming catalyst (Dt/dp) is in the range 5:1 to 50:1.
12 . The process according to claim 1 , wherein the particulate steam reforming catalyst has an equivalent spherical diameter, expressed as a sphere of the same specific surface area, in the range of 3 to 5 mm.
13 . The process according to claim 1 , wherein the particulate steam reforming catalyst has an external geometric surface area in the range of 200 to 2000 m 2 /m 3 .
14 . The process according to claim 1 , wherein the particulate catalyst is contained within a gas permeable container or containers located between the structured steam reforming catalyst layers.