Hydrogen-producing fuel processing assemblies, heating assemblies, and methods of operating the same
View Patent ↗Hydrogen-producing fuel processing assemblies, including steam reforming fuel processing assemblies, startup assemblies for use therein, and methods of operating the same. In some embodiments, the startup assemblies include a startup reforming region that is upstream from a primary, or second, hydrogen-producing reforming region. In some embodiments, the startup reforming region and primary reforming regions are both steam reforming regions. In some embodiments, the startup assembly further includes at least one of a vaporization region and a startup heating assembly. In some embodiments, the startup heating assembly is an electrically powered heating assembly, and the fuel processing assembly further includes a (primary) heating assembly that combusts a byproduct stream from the fuel processing assembly to produce a combustion exhaust stream. In some embodiments, the startup reforming region is adapted to produce a gaseous output stream that will remain a gas-phase stream even if cooled below a minimum hydrogen-producing temperature.
1. A method for starting up a hydrogen generation assembly that includes a startup assembly and a hydrogen-producing region and produces hydrogen gas via a steam reforming reaction, the method comprising:
heating the startup assembly, which includes a vaporization region and a startup reforming region, to a suitable hydrogen-producing temperature during a startup period in which a temperature of the hydrogen-producing region is less than the hydrogen-producing temperature;
delivering a liquid feed stream that contains water and a carbon-containing feedstock to the startup assembly;
vaporizing the liquid feed stream in the startup assembly;
chemically reacting at least a portion of the liquid feed stream in the startup assembly to produce a gas-phase stream that contains hydrogen gas and has a different composition than the liquid feed stream;
withdrawing at least a portion of the gas-phase stream from the startup assembly as an output stream;
delivering the output stream to the hydrogen-producing region, which includes a steam reforming catalyst, during the startup period;
withdrawing a discharge stream from the hydrogen-producing region; wherein the discharge stream contains hydrogen gas and other gases;
delivering the discharge stream to a separation assembly that is configured to separate the discharge stream into a hydrogen-rich stream, which contains a greater concentration of hydrogen gas than the discharge stream, and a byproduct stream, which contains a greater concentration of the other gases than the discharge stream; and
combusting the byproduct stream to produce a heated exhaust stream for heating the startup assembly and the hydrogen-producing region.
2. The method of claim 1 , wherein the heating includes electrically heating the startup assembly.
3. The method of claim 1 , wherein the output stream does not contain any of the carbon-containing feedstock.
4. The method of claim 1 , wherein the output stream includes all of the gas-phase stream.
5. The method of claim 1 , wherein the method further comprises producing an electrical output from a portion of the hydrogen-rich stream.
6. The method of claim 1 , wherein the hydrogen-producing region and the startup reforming region contain different amounts of steam reforming catalyst.
7. The method of claim 1 , wherein the hydrogen-producing region and the startup reforming region contain the same amount of steam reforming catalyst.
8. The method of claim 1 , wherein the method further comprises chemically reacting at least a portion of any carbon monoxide in the hydrogen-rich stream.
9. The method of claim 1 , wherein heating the startup assembly includes heating the startup assembly with a startup heater, wherein combusting the byproduct stream includes combusting the byproduct stream with a combustion heater, and further wherein the method includes ceasing heating the startup assembly with the startup heater subsequent to the startup reforming region reaching the suitable hydrogen-producing temperature.
10. The method of claim 1 , wherein the method further includes initiating heating the startup assembly responsive to a demand for hydrogen gas.
11. The method of claim 1 , wherein delivering the liquid feed stream to the startup assembly includes delivering the liquid feed stream responsive to a temperature of the hydrogen generation assembly.
12. The method of claim 1 , wherein delivering the liquid feed stream to the startup assembly includes delivering the liquid feed stream responsive to a temperature of the startup assembly.
13. The method of claim 1 , wherein the composition of the discharge stream is substantially similar to the composition of the output stream.
14. The method of claim 1 , wherein the output stream remains in the gaseous state at a temperature that is below the hydrogen-producing temperature.
15. The method of claim 1 , wherein the output stream remains in the gaseous state at a temperature of 25° C. and a pressure of 1 atm.
16. The method of claim 1 , wherein chemically reacting at least a portion of the liquid feed stream includes chemically reacting at least a substantial portion of the liquid feed stream.
17. The method of claim 16 , wherein chemically reacting at least a substantial portion of the liquid feed stream includes chemically reacting all of the liquid feed stream.
18. The method of claim 1 , wherein the separation assembly includes a pressure swing adsorption assembly.
19. The method of claim 1 , wherein the separation assembly includes a hydrogen-selective membrane.
20. The method of claim 1 , wherein, during the startup period, the hydrogen-producing region is not producing any hydrogen gas from the output stream delivered thereto.
21. The method of claim 1 , wherein the startup assembly includes a first housing containing the vaporization region and the startup reforming region.
22. The method of claim 21 , wherein the hydrogen-producing region is contained in a second housing that is separate from the first housing.
23. The method of claim 1 , wherein, during the startup period, a fuel value of the byproduct stream that is combusted to form the heated exhaust stream is sufficient to heat the hydrogen-producing region to the hydrogen-producing temperature.
24. The method of claim 23 , wherein the method further includes combusting only the byproduct stream to produce the heated exhaust stream for heating the startup assembly and the hydrogen-producing region.