Cobalt-based catalyst, and preparation method and application thereof, and Fischer-Tropsch synthesis method

A technology of cobalt-based catalysts and Fischer-Tropsch synthesis, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxides/metal hydroxide catalysts, etc., can solve the problems that the catalyst activity needs to be further improved, and achieve Effects of low methane selectivity, high CO conversion, and high C5+ selectivity

Active Publication Date: 2018-10-16
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although this method can improve the activity of the catalyst under the condition of low metal content to a certain extent, the activity of the catalyst still needs to be further improved.

Method used

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  • Cobalt-based catalyst, and preparation method and application thereof, and Fischer-Tropsch synthesis method

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preparation example Construction

[0018] According to another aspect of the present invention, the present invention also provides a method for preparing a cobalt-based catalyst, comprising the steps of:

[0019] 1) impregnating the carrier with a solution containing a cobalt compound, and then sequentially drying the impregnated carrier, roasting or not roasting, and reducing activation;

[0020] 2) Under a reducing or inert atmosphere, the product obtained in step (1) is impregnated with a solution containing high-boiling organic matter and then heat-treated to obtain the cobalt-based catalyst.

[0021] According to the present invention, the cobalt-containing compound is preferably selected from at least one of cobalt nitrate, acetate, sulfate, basic carbonate, and chloride; the solution concentration in terms of cobalt element is preferably 50-1000 grams / L, more preferably 100-700 g / L.

[0022] The present invention is not particularly limited to the impregnation method and conditions in steps (1) and (2...

Embodiment 1

[0041] (1) Catalyst preparation and characterization

[0042] According to the required metal salt content of equal-volume impregnation method, 36.1 milliliters of cobalt nitrate containing 208 grams per liter of cobalt and 1.38 grams per liter of platinum and the impregnation solution of platinum dichlorotetraammine were prepared. Decant the impregnation solution to 42.5 g SiO 2 Carrier (Fuji Silicon Co., Ltd., Japan, average particle size 40-80 microns, specific surface area 135m 2 / g), stirred evenly at 20°C and allowed to stand for 4 hours, then dried at 120°C, calcined at 400°C for 4 hours, reduced with hydrogen at 400°C for 4 hours, and the hydrogen pressure was 0.1 MPa. After reduction, it was lowered to room temperature, and 36.1 ml of 14.5 g / L sucrose aqueous solution was added under a hydrogen atmosphere. After standing for 2 hours, it was dried at 120°C and then heated at 500°C for dehydration and carbonization. After cooling down to room temperature, the O 2 / N ...

Embodiment 2

[0064] (1) Catalyst preparation and characterization

[0065] According to the required metal salt content of equal-volume impregnation method, 36.1 milliliters of cobalt nitrate containing 208 grams per liter of cobalt and 1.38 grams per liter of platinum and the impregnation solution of platinum dichlorotetraammine were prepared. Decant the impregnation solution to 42.5 g SiO 2 Carrier (Qingdao Ocean Chemical Plant, average particle size 40-80 microns, specific surface area 148m 2 / g), stirred evenly at 20°C and allowed to stand for 4 hours, then dried at 120°C, calcined at 400°C for 4 hours, reduced with hydrogen at 400°C for 4 hours, and the hydrogen pressure was 0.1 MPa. After reduction, it was lowered to room temperature, and 36.1 ml of 15.3 g / L glucose aqueous solution was added under a hydrogen atmosphere, and after standing for 2 hours, it was dried at 120°C and then heated at 500°C for dehydration and carbonization. After cooling down to room temperature, the O 2 ...

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Abstract

The invention discloses a cobalt-based catalyst and a preparation method thereof, and a Fischer-Tropsch synthesis method. The catalyst comprises a carrier and further comprises a carbon component anda metal component cobalt loaded on the carrier. In terms of element and based on the total amount of the catalyst, the content of the carbon component is 1 to 30% by weight, and the content of the metal component cobalt is 5 to 70% by weight, with the balance being the carrier. The carbon component or a carbon component precursor in the catalyst is loaded onto the carrier after introduction of themetal component cobalt; and in each g of the catalyst, a ratio of the weight mC of the carbon component in terms of element to the specific surface area S of the carrier satisfies the equation that mC / S = 0.10-4.0 mg / (m<2> / g). Compared with the prior art, the catalyst of the invention has high C<5+> selectivity and low methane selectivity whiel maintaining high Fischer-Tropsch reactivity.

Description

technical field [0001] The invention relates to a cobalt-based catalyst, a preparation method and application, and a Fischer-Tropsch synthesis method. Background technique [0002] In today's rapidly turbulent international energy situation and fierce competition in energy supply and demand, further efficient and clean utilization of coal and natural gas resources is of great strategic significance. Hydrocarbons produced based on technologies such as Fischer-Tropsch synthesis have excellent performance and can be used directly or mixed with fuel produced from low-quality crude oil to meet the increasingly stringent requirements for environmental protection and oil performance indicators. At present, Sasol Company in South Africa and Shell Company in the United Kingdom / Netherlands have mastered the world's leading Fischer-Tropsch industrial synthetic oil technology, and the reactors they use include tubular fixed bed and slurry bed. Sasol's Oryx plant in Qatar is the world's...

Claims

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Application Information

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IPC IPC(8): B01J23/89C10G2/00
CPCB01J23/8913C10G2/333C10G2300/70
Inventor郑仁垟李明丰夏国富李会峰侯朝鹏吴玉晋超徐润
OwnerCHINA PETROLEUM & CHEM CORP