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Fischer-Tropsch synthesis catalyst and application thereof

A Fischer-Tropsch synthesis and catalyst technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problem of methane selectivity decline and increase Co metal surface active sites Density and other issues

Active Publication Date: 2013-11-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Jacobs et al. (AppliedCatalysis A: General, 2009, 361: 137-151) studied the additive effect of Ag and Au on cobalt-based alumina-supported catalysts, and found that the addition of a small amount of Au and Ag can increase the density of active sites on the surface of Co metal. Catalyst activity significantly increased, methane selectivity decreased slightly

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  • Fischer-Tropsch synthesis catalyst and application thereof

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preparation example Construction

[0027] When the catalyst also contains one or more selected from Li, Na, K, Mg, Ca, Sr, Cu, Mo, Ta, W, Zr, Ti, REO, Re, Hf, Ce, Mn, V When an auxiliary component is used, the preparation method of the catalyst further includes the step of introducing the auxiliary component into the catalyst. According to the usual method for preparing the Fischer-Tropsch synthesis catalyst, the auxiliary component may be introduced during the preparation of the carrier, or before, after or at the same time when the metal component is supported. For example, during extrusion molding, the auxiliary component or the compound containing the auxiliary component is directly mixed with the carrier and / or precursor to be shaped, and then extruded. Or it is introduced by the method of impregnating the solution containing the auxiliary component compound before, after or at the same time supporting the metal component.

[0028] In a specific embodiment, the support is an alumina modified by a metal compo...

Embodiment 1

[0037] (1) Catalyst preparation

[0038] Weigh 20 grams of γ-Al 2 O 3 Powder (sasol alumina, average particle size is 40-80 microns), dissolve 24.6 g of cobalt nitrate hexahydrate in 10 ml of deionized water to make an impregnation solution, impregnate the aforementioned alumina carrier with the solution, and let it stand for 2 hours , Dried in an oven at 120°C for 4 hours, then placed it in a tube furnace and calcined at 450°C for 4 hours to obtain sample A1.

[0039] HAuCl 4 ·4H 2 O (the weight percentage of gold is greater than 47.8%) 0.02 g, 0.17 g of urea is dissolved in water to prepare 250 ml of aqueous solution (the molar ratio of urea to gold atoms is 60:1), mix 20 g of A1 with the solution, and heat up To 80°C, immerse and react for 4 hours under stirring. After that, the slurry was filtered and washed with deionized water until the filtrate was free of chloride ions (the filtrate was titrated with a 0.1 mol / L silver nitrate solution, no turbidity, the same below), the f...

Embodiment 2

[0043] (1) Catalyst preparation

[0044] Weigh 20 grams of γ-Al 2 O 3 Powder (sasol alumina, average particle size is 40-80 microns), then weigh 24.6g cobalt nitrate hexahydrate and dissolve in 10ml deionized water to make an impregnation solution, impregnate the aforementioned alumina carrier with this solution, and let it stand for 2h Afterwards, it was dried in an oven at 120°C for 4 hours, and then placed in a tube furnace and calcined at 450°C for 4 hours to obtain sample A1.

[0045] HAuCl 4 ·4H 2 O (the weight percentage of gold is greater than 47.8%) 0.04 g, 0.70 g of urea is dissolved in water to prepare 250 ml of aqueous solution (the molar ratio of urea to gold atoms is 120:1), mix 20 g of A1 with the solution, and heat up To 80°C, immerse and react for 4 hours under stirring. After that, the slurry was filtered and washed with deionized water until no chloride ions were detected in the filtrate. After the filter cake was dried in an oven at 120°C for 3 hours, it was ca...

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Abstract

A Fischer-Tropsch synthesis catalyst and application thereof. The catalyst contains a carrier, an active metal component loaded on the carrier and selected from iron and / or cobalt and an auxiliary agent metal component selected from one or a plurality of precious metals, wherein the auxiliary agent metal component accounts for 0.01-0.3 wt%, calculated by element and using the catalyst as a reference. The preparation method of the catalyst comprises steps of: (1) carrying out a dipping reaction on a solution containing iron compound and / or cobalt compound and the carrier; (2) drying and roasting products obtained from the step (1); (3) carrying out a dipping reaction on a solution containing at last one precious metal compound and the products obtained from the step (2); (4) drying and roasting products obtained from the step (3); and the solution in the step (3) contains alkali, and a molar ratio of the alkali and the precious metals is 20-200. Compared with a prior art, the catalyst provided by the invention has improved Fischer-Tropsch synthesis performance.

Description

Invention field [0001] The invention relates to a Fischer-Tropsch synthesis catalyst and its application. Background technique [0002] Coal and oil are currently the main energy sources used by humans, and it is difficult to change them in a long historical period. Fischer-Tropsch synthesis technology originated from people’s research on coal technology. Its core is to process coal, natural gas or biomass (cellulose, hemicellulose, lignin) and other raw materials into synthesis gas (including H 2 And CO), and then the synthesis gas is converted into liquid hydrocarbon products through the catalytic action of the catalyst. The fuel products produced by this technology do not contain S, N, aromatics, etc., which can effectively reduce air pollution and meet people's increasingly stringent requirements for environmental protection. Fischer-Tropsch synthesis technology was first industrialized in Germany in the 1930s, and then various countries began to establish synthetic oil plan...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89B01J23/78C10G2/00
Inventor 刘斌吴玉王倩侯朝鹏孙霞夏国富李明丰聂红李大东石亚华
Owner CHINA PETROLEUM & CHEM CORP