Method and apparatus for cracking hydrocarbon
US-2016369174-A1 · Dec 22, 2016 · US
US12030041B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12030041-B2 |
| Application number | US-201916698496-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 27, 2019 |
| Priority date | May 31, 2017 |
| Publication date | Jul 9, 2024 |
| Grant date | Jul 9, 2024 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A structured catalyst for steam reforming of the present disclosure is used for producing reformed gas containing hydrogen from a reforming raw material containing hydrocarbon, and includes a support having a porous structure constituted of a zeolite-type compound, and at least one catalytic substance present inside the support. The support includes channels connecting with each other, and the catalytic substance is metal nanoparticles and present at least in the channels of the support.
Opening claim text (preview).
What is claimed is: 1. A structured catalyst for steam reforming used for producing, from a reforming raw material containing hydrocarbon, reformed gas containing hydrogen, the structured catalyst comprising: a support having a porous structure constituted of a zeolite-type compound; and at least one catalytic substance present inside the support, wherein the support includes channels connecting with each other, and the catalytic substance is metal nanoparticles and present at least in the channels of the support, wherein the channels include any one of a one-dimensional pore, a two-dimensional pore, and a three-dimensional pore defined by a framework of the zeolite-type compound and a plurality of enlarged pore portions having a diameter different from that of any of the one-dimensional pore, the two-dimensional pore, and the three-dimensional pore, the metal nanoparticles are embedded in a respective enlarged pore portion such that a metal nanoparticle is separate from another metal nanoparticle of the metal nanoparticles, and the average inner diameter of the channels is less than the inner diameter of the enlarged pore portion. 2. The structured catalyst for steam reforming according to claim 1 , wherein the metal nanoparticles are nanoparticles composed of at least one type of metal selected from the group consisting of rhodium (Rh), ruthenium (Ru), iridium (Ir), palladium (Pd), platinum (Pt), iron (Fe), cobalt (Co), and nickel (Ni). 3. The structured catalyst for steam reforming according to claim 2 , wherein the average inner diameter of the channels is from 0.1 nm to 1.5 nm, and the inner diameter of the enlarged pore portion is from 0.5 nm to 50 nm. 4. The structured catalyst for steam reforming according to claim 1 , wherein the enlarged pore portion causes a plurality of pores constituting any one of the one-dimensional pore, the two-dimensional pore, and the three-dimensional pore to connect with each other. 5. The structured catalyst for steam reforming according to claim 1 , wherein a mean particle size of the metal nanoparticles is greater than an average inner diameter of the channels and is less than or equal to an inner diameter of the enlarged pore portion. 6. The structured catalyst for steam reforming according to claim 1 , wherein a metal element (M) of the metal nanoparticles is contained in an amount from 0.5 to 2.5 mass % based on the structured catalyst for steam reforming. 7. The structured catalyst for steam reforming according to claim 1 , wherein the mean particle size of the metal nanoparticles is from 0.08 nm to 30 nm. 8. The structured catalyst for steam reforming according to claim 7 , wherein the mean particle size of the metal nanoparticles is from 0.4 nm to 11.0 nm. 9. The structured catalyst for steam reforming according to claim 1 , wherein a ratio of the mean particle size of the metal nanoparticles to the average inner diameter of the channels is from 0.05 to 300. 10. The structured catalyst for steam reforming according to claim 9 , wherein the ratio of the mean particle size of the metal nanoparticles to the average inner diameter of the channels is from 0,1 to 30. 11. The structured catalyst for steam reforming according to claim 10 , wherein the ratio of the mean particle size of the metal nanoparticles to the average inner diameter of the channels is from 1.4 to 3.6. 12. The structured catalyst for steam reforming according to claim 1 , further comprising at least one other catalytic substance held on an outer surface of the support. 13. The structured catalyst for steam reforming according to claim 12 , wherein a content of the at least one catalytic substance present inside the support is greater than a content of the at least one other catalytic substance held on the outer surface of the support. 14. The structured catalyst for steam reforming according to claim 1 , wherein the zeolite-type compound is a silicate compound. 15. A reforming apparatus comprising the structured catalyst for steam reforming according to claim 1 . 16. A method for manufacturing a reduced structured catalyst for steam reforming, the method comprising the steps of: calcinating a precursor material (B) obtained by impregnating, with metal containing solution, a precursor material (A) for obtaining a support having a porous structure constituted of a zeolite-type compound; hydrothermally treating a precursor material (C) obtained by calcinating the precursor material (B) to obtain an oxidized structured catalyst; and performing a reduction treatment of the oxidized structured catalyst that has been hydrothermally treated to obtain the reduced structured catalyst. 17. The method for manufacturing a structured catalyst for steam reforming according to claim 16 , wherein from 50 to 500 mass % of a non-ionic surfactant is added to the precursor material (A) before the calcinating. 18. The method for manufacturing a structured catalyst for steam reforming according to claim 16 , wherein the precursor material (A) is impregnated with the metal containing solution by adding the metal containing solution to the precursor material (A) in multiple portions before the calcinating. 19. The method for manufacturing a structured catalyst for steam reforming according to claim 16 , wherein in impregnating the precursor material (A) with the metal containing solution before the calcinating, an added amount of the metal containing solution added to the precursor material (A), in terms of a ratio of silicon (Si) constituting the precursor material (A) to a metal element (M) contained in the metal containing solution added to the precursor material (A) (a ratio of number of atoms Si/M), is adjusted to from 10 to 1000.
in a colloidal state · CPC title
MTW-type, e.g. ZSM-12, NU-13, TPZ-12 or Theta-3 · CPC title
Metal or metal oxide crystallite size · CPC title
Metal dispersion value, e.g. percentage or fraction · CPC title
Hydrocarbons · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.