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Composite metal oxide type alkane dehydrogenation catalyst and preparation method thereof

A technology of alkane dehydrogenation and composite metal, applied in the direction of metal/metal oxide/metal hydroxide catalyst, carbon compound catalyst, physical/chemical process catalyst, etc., can solve the problem of low conversion rate and selectivity of catalyst, conversion rate and Selectivity cannot be coordinated, industrial application conditions are quite different, etc., to achieve the effect of low price, high mechanical strength and high selectivity

Inactive Publication Date: 2021-09-28
SOUTHWEST RES & DESIGN INST OF CHEM IND
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] Chinese patents CN111036260A and CN109939688A disclose a kind of iron-based propane dehydrogenation catalyst respectively, but catalyst conversion rate and selectivity are all low, it is difficult to realize industrialization; CN109382090A discloses a kind of molybdenum vanadium double metal oxide catalyst, and activity is very good, However, vanadium oxide is also highly toxic and has strong carcinogenicity; CN202011090154.6 discloses a Ga-based alkane dehydrogenation catalyst, but a noble metal is added as an auxiliary agent, and the evaluation method is quite different from the industrial application conditions; CN102451677, CN104610768 and CN105289622 provide a series of Al 2 o 3 , SiO 2 , ZrO 2 、TiO 2 The alkane dehydrogenation catalyst with MgO as the carrier and various metals as active components has achieved a good yield of propylene, but there is still the problem that the conversion rate and selectivity cannot be coordinated, and there is still room for optimization and improvement

Method used

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preparation example Construction

[0029] As preferably, the preparation method of described alkane dehydrogenation catalyst comprises the following steps:

[0030] (1) Dissolve a certain amount of A and B precursors in water, stir evenly, and use sol-gel method, co-precipitation method or hydrothermal synthesis method to obtain active components AxB2-xO3 after drying and roasting;

[0031] (2) Grind the active component obtained in step (1) into a fine powder below 20 μm, mix it with the precursor of the carrier evenly, adopt different molding processes, and roast at 450-800 °C for 2-8 hours to obtain a fixed-bed , moving bed, fluidized bed catalyst.

[0032] Preferably, the alkane dehydrogenation catalyst may also contain optional additives, such as extrusion agents, rheology control agents, binders, surfactants and the like.

Embodiment 1

[0036] Dissolve 40.61g of ferric nitrate nonahydrate and 87.99g of aluminum nitrate nonahydrate in water, stir evenly, add an appropriate amount of ammonia water, adjust the pH to about 6.5-7.5, let stand for 4 hours, dry at 120°C for 8 hours, and roast at 620°C for 4 hours to obtain the activity Component Fe0.6Al1.4O3;

[0037] Grind the obtained active components into fine powders below 20 μm, mix them evenly with 54.29 g of pseudoboehmite and 166.7 g of silica sol, add an appropriate amount of nitric acid, adjust the pH to 3-4, spray molding, and roast at 600 ° C for 3 hours to obtain Catalyst 1.

[0038] The evaluation results of the catalyst showed that the conversion rate of propane was 34.65%, and the selectivity was 85.76%.

Embodiment 2

[0040] Dissolve 19.90g of scandium chloride and 73.94g of aluminum nitrate nonahydrate in water, stir well, add an appropriate amount of sodium carbonate to precipitate scandium chloride and aluminum nitrate, filter, wash 4 times, dry at 100°C for 6 hours, and roast at 680°C for 6 hours , to obtain the active component Sc0.8Al1.2O3;

[0041] Grind the obtained active component into a fine powder below 20 μm, mix it with 80 g of titanium oxide and 5.3 g of turnip powder, press it into a tablet, and calcinate at 500° C. for 3 hours to obtain Catalyst 2.

[0042] The evaluation results of the catalyst showed that the conversion rate of propane was 36.03%, and the selectivity was 86.24%.

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Abstract

The invention belongs to the technical field of preparation of alkane dehydrogenation catalysts, and particularly relates to a preparation method of a composite metal oxide type alkane dehydrogenation catalyst. The catalyst prepared by the method contains an active component AxB2-xO3, A is one of La, Fe, Sc, In, Ga and Y, B is one of Al, Bi and B, a carrier is one or more of aluminum oxide, silicon oxide, zirconium oxide and titanium oxide, and the catalyst does not contain Cr and precious metal, is environment-friendly and cheap, and can be applied to fixed bed, moving bed and fluidized bed devices through different forming processes.

Description

technical field [0001] The invention belongs to the technical field of preparation of alkane dehydrogenation catalysts, in particular to a composite metal oxide type alkane dehydrogenation catalyst and a preparation method of the catalyst. Background technique [0002] Alkanes dehydrogenation technology has been industrialized, and currently there are two main types of catalysts used: Pt-based catalysts and CrOx-based catalysts. The cost of Pt-based catalysts is too high, and they are sensitive to poisons such as sulfur and olefins. Therefore, the requirements for raw materials are relatively strict, and raw materials need to be pretreated. CrOx-based catalysts are easy to coke and deactivate quickly, and need to be regenerated repeatedly; moreover, Cr6+ is highly toxic and is a carcinogen announced by the International Anti-Cancer Research Center and the American Toxicology Organization. In the national industrial wastewater discharge standard, hexavalent chromium is the fi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/08B01J23/10B01J23/18B01J23/745C07C5/333C07C11/06
CPCB01J23/745B01J23/10B01J23/08B01J23/18B01J23/002C07C5/3332C07C2523/08C07C2523/10C07C2523/18C07C2523/745B01J2523/00C07C11/06B01J2523/31B01J2523/41B01J2523/842B01J2523/35B01J2523/47B01J2523/305B01J2523/33B01J2523/48B01J2523/32B01J2523/54B01J2523/3706Y02P20/52
Inventor 梁衡潘相米韩伟李南锌艾珍吴砚会李扬张军
Owner SOUTHWEST RES & DESIGN INST OF CHEM IND