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A kind of Fischer-Tropsch synthesis iron-based catalyst and preparation method thereof

An iron-based catalyst and Fischer-Tropsch synthesis technology, applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, physical/chemical process catalysts, etc., can solve the problem of large amount of potassium source raw materials, unsatisfactory catalyst stability and oil yield To achieve the continuity of the process, save washing water, improve stability and oil yield

Active Publication Date: 2020-04-17
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Description
  • Claims
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Problems solved by technology

[0004] In order to overcome the problems of unsatisfactory catalyst stability and oil yield in the existing Fischer-Tropsch synthesis iron-based catalyst preparation method, and the large amount of potassium source raw materials used in the preparation process, a Fischer-Tropsch synthesis iron-based catalyst is provided. The preparation method of catalyst, this method comprises:

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  • A kind of Fischer-Tropsch synthesis iron-based catalyst and preparation method thereof

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preparation example Construction

[0015] The present invention provides a kind of preparation method of Fischer-Tropsch synthesis iron-based catalyst, wherein, the method comprises:

[0016] (1) The aqueous solution of iron salt, copper salt and cobalt salt is subjected to coprecipitation reaction with precipitation agent, obtains precipitation slurry;

[0017] (2) aging the precipitated slurry obtained in step 1, adjusting the pH to 4.0-10.0, and filtering to remove water to obtain a filter cake;

[0018] (3) The filter cake obtained in step 2) is beaten with water to make a slurry, which is then spray-dried and roasted;

[0019] (4) remove sodium ions and nitrate ions in the product through roasting in step 3);

[0020] (5) drying the product obtained in step 4), and placing it in the potassium source solution for impregnation;

[0021] (6) Roasting the impregnated product in step 5) to obtain a Fischer-Tropsch synthesis iron-based catalyst;

[0022] And, in step 1) and / or step 2), silicon compound soluti...

Embodiment 1

[0039] 25kg iron nitrate nonahydrate, 0.7kg copper nitrate and 4.5kg cobalt nitrate hexahydrate were dissolved in deionized water to make 160 liters of solution, and 12.5 kg of sodium carbonate was dissolved in deionized water to make 80 liters of solution. Use a pump to flow ferric nitrate, copper nitrate, cobalt nitrate solution and sodium carbonate solution into the reaction kettle, control the temperature in the reaction kettle at 60°C, and control the pH value at 6. After the precipitation is completed, let it stand for aging for 30 minutes. at 60°C; then add a concentration of 15% sodium silicate solution, use nitric acid to control the pH of the material at 5.0, and then squeeze out the moisture through a filter; add demineralized water to control the slurry with a solid content of 20% by mass. The inlet temperature is controlled at 250°C, and the hot air temperature at the exhaust outlet is spray-dried at 120°C, and the sprayed catalyst is roasted in the first stage, th...

Embodiment 2

[0043] 25kg ferric nitrate nonahydrate, 0.40kg copper nitrate, and 0.28kg cobalt nitrate hexahydrate were dissolved in deionized water to make 160 liters of solution, and 12.5 kg of sodium carbonate was dissolved in deionized water to make 80 liters of solution. Use a pump to flow ferric nitrate, copper nitrate, cobalt nitrate solution and sodium carbonate solution into the reaction kettle, control the temperature in the reaction kettle at 80°C, and control the pH value at 8.5. at 80°C; then add a concentration of 15% sodium silicate solution, use nitric acid to control the pH of the material at 4.5, and then squeeze out the moisture through a filter; add demineralized water to control the slurry with a solid content of 20% by mass. The inlet temperature is controlled at 250°C, and the hot air temperature at the exhaust outlet is spray-dried at 120°C, and the sprayed catalyst is roasted in the first stage, the temperature is controlled at 200°C, the time is controlled at 1 hour...

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Abstract

The invention discloses a Fischer-Tropsch synthesis iron-based catalyst and a preparation method thereof. The preparation method comprises that aqueous solutions of a ferric salt, a copper salt and a cobalt salt and a precipitator undergo a coprecipitation reaction, the deposited slurry is aged and then is subjected to filtration and water removal, then the filter cake obtained through filtration and water removal and water are mixed, the mixture is beat to form slurry and then is subjected to spray drying and roasting, sodium and nitrate ions in the roasted product are removed, then the roasted product is dried and is immersed in a potassium source solution, and the immersed product is roasted so that the catalyst is obtained. The preparation method also comprises silicon compound solution introduction in coprecipitation and / or after aging treatment. The sodium and nitrate ions in the dried roasted product are removed by washing so that washing water is greatly reduced, technical continuity is easily realized, a raw material cost is greatly reduced and iron-based catalyst stability and an oil yield are substantially improved.

Description

technical field [0001] The invention relates to the field of catalyst preparation, in particular to a Fischer-Tropsch synthesis iron-based catalyst and a preparation method thereof. Background technique [0002] In 1923, Germans F.Fischer and H.Tropsch discovered syngas (CO+H 2 ) can synthesize liquid fuels and other chemicals under the action of catalysts, and this process is called Fischer-Tropsch synthesis. The catalysts used for Fischer-Tropsch synthesis include Fe, Co, Ni, Ru and other elements, but only iron-based and cobalt-based catalysts have commercial value. Iron-based catalysts are generally divided into molten iron catalysts and precipitated iron catalysts. Molten iron catalysts are generally used in fixed-bed and fluidized-bed reactors, and limited by conditions in industrial scale-up, it is difficult to achieve million-ton production per year. In 1993, Sasol Company realized the industrial production of Fischer-Tropsch synthesis by adopting iron-based catal...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/04B01J23/889B01J23/83C10G2/00
Inventor 朱加清罗明生石玉林吕毅军陈静允程萌常海
Owner CHNA ENERGY INVESTMENT CORP LTD