Steam methane reforming reactor of shell and tube type with cylindrical slots
US-2015376005-A1 · Dec 31, 2015 · US
US11958746B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11958746-B2 |
| Application number | US-202017128601-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 21, 2020 |
| Priority date | Jul 9, 2018 |
| Publication date | Apr 16, 2024 |
| Grant date | Apr 16, 2024 |
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A hydrocarbon reforming catalyst for producing a synthesis gas containing hydrogen and carbon monoxide from a hydrocarbon-based gas, the hydrocarbon reforming catalyst containing a complex oxide having a perovskite structure including at least Ba, Zr, and Ru; and a hydrocarbon reforming apparatus that includes the hydrocarbon-reforming catalyst.
Opening claim text (preview).
The invention claimed is: 1. A hydrocarbon reforming catalyst for producing a synthesis gas containing hydrogen and carbon monoxide from a hydrocarbon-based gas, the hydrocarbon reforming catalyst comprising: a complex oxide having a perovskite structure including at least Ba, Zr, Ru, and Y, wherein a molar ratio of Y to Ba is 0.1 to 0.5. 2. The hydrocarbon reforming catalyst according to claim 1 , wherein a molar ratio of the Ru to the Ba is 0.07 or more. 3. The hydrocarbon reforming catalyst according to claim 2 , wherein the molar ratio of the Ru to the Ba is 0.07 to 0.41. 4. The hydrocarbon reforming catalyst according to claim 1 , wherein a molar ratio of the Y to the Ba is 0.2 to 0.4. 5. The hydrocarbon reforming catalyst according to claim 1 , wherein a molar ratio of the Y to the Zr is 0.1 or more. 6. The hydrocarbon reforming catalyst according to claim 5 , wherein the molar ratio of the Y to the Zr is 0.1 to 1. 7. The hydrocarbon reforming catalyst according to claim 1 , wherein a molar ratio of the Y to the Zr is 0.25 to 0.67. 8. The hydrocarbon reforming catalyst according to claim 1 , wherein a molar ratio of a total amount of the Zr and the Y to the Ba is 0.68 to 1.5. 9. The hydrocarbon reforming catalyst according to claim 1 , wherein a molar ratio of the Y to the Zr is 0.1 to 1, and a molar ratio of a total amount of the Zr and the Y to the Ba is 0.68 to 1.5. 10. A hydrocarbon reforming apparatus for treating a gas containing at least a hydrocarbon, the apparatus comprising: a pipe configured such that the gas containing the at least the hydrocarbon can flow; a heater positioned to heat the gas as the gas flows through the pipe; and a hydrocarbon-reforming catalyst disposed so as to contact the gas while the gas is inside the pipe, the hydrocarbon-reforming catalyst containing a complex oxide having a perovskite structure including at least Ba, Zr, Ru, and Y, wherein a molar ratio of Y to Ba is 0.1 to 0.5. 11. The hydrocarbon reforming apparatus according to claim 10 , wherein a molar ratio of the Ru to the Ba is 0.07 to 0.41. 12. The hydrocarbon reforming apparatus according to claim 10 , wherein the molar ratio of the Y to the Zr is 0.1 to 1. 13. The hydrocarbon reforming apparatus according to claim 10 , wherein a molar ratio of the Y to the Zr is 0.1 to 1, and a molar ratio of a total amount of the Zr and the Y to the Ba is 0.68 to 1.5. 14. The hydrocarbon reforming apparatus according to claim 10 , further comprising a hydrocarbon supply source that is disposed on an upstream side of the pipe and is constructed to supply the hydrocarbon. 15. The hydrocarbon reforming apparatus according to claim 10 , further comprising a hydrogen extraction outlet disposed on a downstream side of the pipe.
X-ray diffraction · CPC title
Perovskite-type · CPC title
characterised by the catalyst · CPC title
Regeneration or reactivation · CPC title
Barium · CPC title
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