Systems, Devices and Methods for Input and Output Pressure Management of Air Breathing Engine Reformers
US-2024017993-A1 · Jan 18, 2024 · US
US10017385B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10017385-B2 |
| Application number | US-201615205045-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 8, 2016 |
| Priority date | Nov 26, 2015 |
| Publication date | Jul 10, 2018 |
| Grant date | Jul 10, 2018 |
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The present invention provides a catalyst composition for producing hydrogen and preparation method and use thereof, wherein the catalyst composition comprises a catalytic component and a supporter having a pyrochlore structure. By using the catalyst composition of the present invention, carbon deposition can be reduced and the oxidative steam reforming of ethanol could be operated for a long period of time with high ethanol conversion rate and selectivity of hydrogen.
Opening claim text (preview).
What is claimed is: 1. A catalyst composition for producing hydrogen comprising: a catalytic active component; and a supporter represented by formula (I), wherein the catalytic active component is formed on the supporter, A 2 B 2 O 7 (I) wherein A is an element selected from the group consisting of alkaline earth metals and Group IIIB transition metals, and B is an element selected from Group IVB metals. 2. The catalyst composition of claim 1 , wherein A is the element selected from the group consisting of Ca, Sr, Ba, Sc, Y, La, Ce, Nd, Sm, Gd and Dy. 3. The catalyst composition of claim 1 , wherein B is the element selected from the group consisting of Ti, Zr and Hf. 4. The catalyst composition of claim 1 , wherein the catalytic active component is a metal solid solution represented by formula (II) M 2-x M′ x (Ce y N 2-y )O 7-δ (II) wherein M is an element selected from Group IIIB metals; M′ is an element selected from the group consisting of alkali metals, alkaline earth metals and Group IIIB metals, and M is different from M′; N is a transition metal, and is exclusive from a Group IIIB metal or lanthanides; x is 0.1 to 1.0; y is 1.8 to 1.9; and δ is greater than 0 to 0.5. 5. The catalyst composition of claim 4 , wherein M is the element selected from the group consisting of Sc, Y and La, and M′ is the element selected from the group consisting of alkali metals, alkaline earth metals, Sc, Y and La. 6. The catalyst composition of claim 4 , wherein M is La, M′ is Li, and N is Ru. 7. The catalyst composition of claim 4 , wherein M is La, M′ is Mg or Ca, and N is Ru. 8. The catalyst composition of claim 4 , wherein M is Y, M′ is Sc, and N is Ru. 9. The catalyst composition of claim 4 , wherein N is an element selected from the group consisting of Ru, Os, Rh, Ir and Re. 10. The catalyst composition of claim 1 , wherein the catalytic active component is a metal solid solution represented by formula (III) P 2 (O 2-z Ru z )O 7 (III) wherein P is an element selected from the group consisting of Sc, Y and La; Q is an element selected from the group consisting of Ti, Zr and Ce; and z is 0≤z≤0.4. 11. The catalyst composition of claim 1 , wherein the catalytic active component is a metal solid solution represented by formula (IV) La 2 (C 2-μ D μ )O 7-1.5μ (IV) wherein C is an element selected from the group consisting of Ti, Zr and Ce; D is an element selected from the group consisting of Co, Ni and Cu; and μ is 0≤μ≤ 0 . 9 . 12. The catalyst composition of claim 1 , wherein the catalytic active component is one or two elements selected from the group consisting of Fe, Co, Ni, Cu, Rh, Ru, Pt, Pd and Ir. 13. A preparation method of the catalyst composition for producing hydrogen, comprising: mixing a supporter represented by formula (I) with a catalytic active component or a metal precursor having a metal element with catalytic activity in the presence of solvent, A 2 B 2 O 7 (I) wherein A is an element selected from the group consisting of alkaline earth metals and Group IIIB transition metals; and B is an element selected from Group IVB metals; and removing the solvent. 14. The method of claim 13 , wherein the metal precursor is selected from the group consisting of metal salts, metal hydrates or metal chlorides, and the metal element with catalytic activity of the metal precursor is one or two elements selected from the group consisting of Fe, Co, Ni, Cu, Rh, Ru, Pt, Pd and Ir. 15. The method of claim 13 , wherein the supporter represented by formula (I) is mixed with the catalytic active component, and the solvent is alcohol. 16. The method of claim 15 , wherein the alcohol is selected from the group consisting of methanol, ethanol, butanol or isopropanol. 17. The method of claim 13 , wherein the solvent is removed at a temperature ranging from 80 to 100° C. 18. The method of claim 13 , further comprising calcining a mixture formed by mixing the supporter represented by formula (I) with the metal precessor to allow the metal element with catalytic activity to be formed on the supporter represented by formula (I), wherein the calcination temperature ranges from 200 to 400° C., and the calcination time ranges from 3 to 7 hours. 19. A method for producing hydrogen, comprising: (a) adding the catalyst composition of claim 1 to ethanol to form a mixture; and (b) carrying out oxidative seam reforming on the mixture to produce hydrogen.
to form a gel or a cogel · CPC title
Zirconium or hafnium; Oxides or hydroxides thereof · CPC title
Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Mixed oxides other than spinels, e.g. perovskite · CPC title
Composition of support materials · CPC title
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