NANO Ni-Zr OXIDE CATALYST FOR ACTIVATION OF METHANE BY TRI-REFORMING AND A PROCESS FOR THE PREPARATION THEREOF
US-2016289073-A1 · Oct 6, 2016 · US
US11203012B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11203012-B2 |
| Application number | US-201916545480-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 20, 2019 |
| Priority date | Aug 22, 2018 |
| Publication date | Dec 21, 2021 |
| Grant date | Dec 21, 2021 |
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Provided are a Nb-doped nickel oxide-zirconia composite catalyst, and a method for preparing the same. An excellent methane modification reaction is performed by doping a nickel oxide site with niobium, so that alcohol may be prepared at low costs.
Opening claim text (preview).
What is claimed is: 1. A Nb-doped nickel oxide-zirconia composite catalyst, wherein the niobium is comprised in an amount of 0.01 to 0.15 mol based on 1 mol of the composite catalyst, and wherein the composite catalyst consists of the Nb-doped nickel oxide and the zirconia and has a mol ratio of Nb-doped nickel oxide to zirconia of 9.9:0.1 to 8.0:2.0. 2. The composite catalyst of claim 1 , wherein the niobium is niobium dioxide doped on a nickel oxide site. 3. The composite catalyst of claim 2 , wherein the nickel oxide is present in a cubic phase, and the niobium dioxide and the zirconia are present in a tetragonal phase. 4. The composite catalyst of claim 1 , wherein the composite catalyst has an average particle diameter of 1 to 50 μm. 5. A method for preparing the composite catalyst according to claim 1 , the method comprising: obtaining a precursor mixture solution by dissolving a niobium oxide precursor, a nickel oxide precursor, and a zirconia precursor in an organic solvent; drying the precursor mixture solution; and sintering the dried product. 6. The method of claim 5 , wherein the nickel oxide precursor is one or more selected from nickel(II) chloride hydrate, nickel(II) acetate tetrahydrate, and nickel(II) nitrate hexahydrate. 7. The method of claim 5 , wherein the zirconia precursor is zirconium acetate, or zirconium(IV) oxynitrate hydrate. 8. The method of claim 5 , wherein the niobium oxide precursor is ammonium niobate(V) oxalate hydrate or niobium(V) chloride. 9. The method of claim 5 , wherein the organic solvent is one or more selected from methanol, 1-propanol, and 2-propanol. 10. The method of claim 5 , wherein the nickel oxide precursor and the zirconia precursor are mixed at a mol ratio of 10:1 to 8:1. 11. The method of claim 5 , wherein the niobium oxide precursor is used in an amount of 0.7 to 14 parts by weight based on 100 parts by weight of a combined amount of the nickel oxide precursor and the zirconia precursor. 12. The method of claim 5 , wherein the drying of the precursor mixture solution is performed at a temperature of 40 to 100° C. for 1 to 24 hours. 13. The method of claim 5 , wherein the sintering of the dried product is performed at a temperature of 400 to 600° C. for 1 to 4 hours.
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
X-ray diffraction · CPC title
Nuclear magnetic resonance [NMR] · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
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