Modified propane dehydrogenation system and method for producing one or more chemical products from propane
US-2018162790-A1 · Jun 14, 2018 · US
US10179763B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10179763-B2 |
| Application number | US-201515102950-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 4, 2015 |
| Priority date | Mar 6, 2014 |
| Publication date | Jan 15, 2019 |
| Grant date | Jan 15, 2019 |
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There is provided a method for producing an oxide catalyst, the method including a step (a) of obtaining an aqueous mixed liquid A containing Mo, V and Sb, a step (b) of mixing a Nb raw material, water and an organic acid to obtain a Nb aqueous solution, a step (c) of mixing the Nb aqueous solution and a silica raw material to obtain an aqueous mixed liquid B, a step (d) of mixing the aqueous mixed liquid A and the aqueous mixed liquid B to obtain an aqueous mixed liquid (C), a step (e) of drying the aqueous mixed liquid C to obtain a dried powder D, and a step (f) of calcining the dried powder D to obtain the oxide catalyst.
Opening claim text (preview).
The invention claimed is: 1. A method for producing an oxide catalyst, the method comprising: a step (a) of obtaining an aqueous mixed liquid A comprising Mo, V and Sb; a step (b) of mixing a Nb raw material which is one or more selected from the group consisting of niobic acid, and inorganic niobate and an organic niobate, water and an organic acid to obtain a Nb aqueous solution; a step (c) of mixing the Nb aqueous solution and a silica raw material to obtain an aqueous mixed liquid B; a step (d) of mixing the aqueous mixed liquid A and the aqueous mixed liquid B to obtain an aqueous mixed liquid C; a step (e) of drying the aqueous mixed liquid C to obtain a dried powder D; and a step (f) of calcining the dried powder D to obtain the oxide catalyst, wherein the oxide catalyst consists of a metal component represented by formula (1): Mo 1 V a Sb b Nb c W d Z e O n (1), wherein Z is at least one element selected from the group consisting of La, Ce, Pr, Yb, Y, Sc, Sr and Ba; a, b, c, d, e and n represent atomic ratios of each element and satisfy 0.1≤a≤0.3, 0.15≤b≤0.5, 0.01≤c≤0.5, 0≤d≤0.4, and 0≤e≤0.2, and n is a number determined by a, b, c, d and e. 2. The method for producing the oxide catalyst according to claim 1 , wherein a molar ratio (Nb/Si) of Nb to 1 mol of Si in the aqueous mixed liquid B is 0.02 to 0.7. 3. The method for producing the oxide catalyst according to claim 1 , wherein in the step (c), a mixing time of the Nb aqueous solution and the silica raw material is 1 minute to 6 hours. 4. The method for producing the oxide catalyst according to claim 1 , comprising, after the step (d) and before the step (e), a step (d′) of mixing the aqueous mixed liquid C and powder silica and/or silica sol. 5. The method for producing the oxide catalyst according to claim 1 , wherein a content of silica in the oxide catalyst is 20 to 70% by mass in terms of SiO 2 .
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