Method and system for producing a synthesis gas using an oxygen transport membrane based reforming system with secondary reforming and auxiliary heat source
US-9212113-B2 · Dec 15, 2015 · US
US9908091B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9908091-B2 |
| Application number | US-201615059330-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 3, 2016 |
| Priority date | Mar 31, 2015 |
| Publication date | Mar 6, 2018 |
| Grant date | Mar 6, 2018 |
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A furnace for steam reforming a feed stream containing hydrocarbon, preferably methane, having: a combustion chamber, a plurality of reactor tubes arranged in the combustion chamber for accommodating a catalyst and for passing the feed stream through the reactor tubes, and at least one burner which is configured to burn a combustion fuel in the combustion chamber to heat the reactor tubes. In addition at least one voltage source is provided which is connected to the plurality of reactor tubes in such a manner that in each case an electric current which heats the reactor tubes to heat the feedstock is generable in the reactor tubes.
Opening claim text (preview).
The invention claimed is: 1. A furnace for steam reforming a feed stream containing hydrocarbon, preferably comprising methane, comprising: a combustion chamber, a plurality of reactor tubes arranged in the combustion chamber accommodating a reforming catalyst and configured to pass the feed stream through the reactor tubes, at least one burner configured to burn a combustion fuel in the combustion chamber to heat the reactor tubes, at least one voltage source connected to the plurality of reactor tubes in such a manner that an electric current which heats the reactor tubes to heat the feedstock is generable in the reactor tubes, and M outer conductors, wherein M is a natural number greater than or equal to 2, wherein the at least one voltage source is configured to provide an alternating voltage to each of the M outer conductors, and wherein the alternating voltages are phase-shifted relative to one another by 2π/M. 2. Furnace according to claim 1 , characterized in that the reactor tubes open into a manifold. 3. Furnace according to claim 2 , characterized in that the outer conductors are each electrically conductively connected to an associated reactor tube of the plurality of reactor tubes, such that a star connection is formed, in which the neutral point is formed by the manifold. 4. Furnace according to claim 3 , characterized in that each outer conductor has an end region via which it is electrically conductively connected to a contact region of the associated reactor tube. 5. Furnace according to claim 4 , characterized in that the respective end region is connected to the contact region of the associated reactor tube via a press-fit connection or welded connection. 6. Furnace according to claim 4 , characterized in that the contact regions each project transversely of a longitudinal axis of the respective reactor tube from a jacket of the respective reactor tube. 7. Furnace according to claim 4 , characterized in that the contact regions are provided on the reactor tubes outside the combustion chamber and above the combustion chamber. 8. Furnace according to claim 4 , characterized in that the reactor tubes have a cross-sectional thickening at the respective contact region. 9. Furnace according to claim 8 , characterized in that, the outer conductors or the first and second conductors are each surrounded by a sleeve in the form of insulation, wherein the respective sleeve defines a flow duct which is configured to guide the fluid coolant. 10. Furnace according to claim 3 , characterized in that each outer conductor has a first and, connected in parallel thereto, a second electrical conductor, wherein each of the first and second electrical conductors have an end region which is electrically conductively connected to a contact region of the associated reactor tube. 11. Furnace according to claim 10 , characterized in that the respective end region is connected to the contact region of the associated reactor tube via a press-fit connection or welded connection. 12. Furnace according to claim 10 , characterized in that a cooling device is provided which is configured to cool the outer conductors or the first and second electrical conductors by means of a fluid coolant. 13. Furnace according to claim 12 , characterized in that the outer conductors or the first and second conductors each form a flow duct which is configured to guide the fluid coolant. 14. Furnace according to claim 13 , characterized in that the flow duct associated with the respective first conductor is fluidically connected adjacent the contact region to the flow duct associated with the respective second conductor, such that the fluid coolant is guidable via the one flow duct to the contact region and via a flow path away from the contact region.
Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor (application of shock waves B01J3/08) · CPC title
in tube reactors; the solid particles being arranged in tubes · CPC title
using catalysts · CPC title
the reforming step being a steam reforming step · CPC title
by electric heating · CPC title
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