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Iron-based catalyst and preparation method thereof

A catalyst and iron-based technology, applied in the field of iron-based catalysts and their preparation, can solve problems such as unfavorable cost saving, large-scale development and application, high raw material cost, complicated preparation process or used equipment, etc. Activity, the effect of increasing coal conversion and oil production

Inactive Publication Date: 2015-09-09
CHNA ENERGY INVESTMENT CORP LTD +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst of the invention has the characteristics of high dispersion, good oil solubility, and high catalytic activity; Taniguchi et al. prepared ultrafine ferrous sulfide catalysts using carbonyl iron complexes as raw materials; Dadyburjor et al. prepared ultrafine iron Sulfur catalyst; Chadha et al. used high-temperature pyrolysis of disproportionated iron sulfide to prepare ultrafine iron sulfide catalysts with different stoichiometric ratios; the ultrafine iron-based catalysts prepared by the above methods have high coal liquefaction activity, but either raw materials The cost is too high, or the preparation process or the equipment used are complicated, which is not conducive to cost saving and large-scale development and application

Method used

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  • Iron-based catalyst and preparation method thereof

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preparation example Construction

[0026] In another typical embodiment of the present invention, a method for preparing an iron-based catalyst is provided. The preparation method includes: step S1, preparing a FeOOH filter cake, the filter cake contains a structural aid component and an optional part of the second Active ingredient; step S2, making FeOOH filter cake into powdered FeOOH; step S3, loading all or remaining second active ingredients on powdery FeOOH to obtain iron-based catalyst; wherein, the second active ingredient includes nickel, molybdenum, cobalt and one or more elements of tungsten; the structural aid component includes one or more elements of silicon, aluminum and zirconium.

[0027] In the above-mentioned preparation method of the present invention, by adopting the structural aid component containing the above-mentioned elements to form a FeOOH filter cake with the first active component Fe, and according to the difference of the element type contained in the second active component, optio...

Embodiment 1

[0041] Weigh 51.16g FeCl respectively 2 4H 2 O, 1.86g Ni(NO 3 ) 2 ·6H 2 O, 20.83g Al(NO 3 ) 3 9H 2 O was dissolved in 600g deionized water together to obtain a mixed solution containing ferrous, nickel and aluminum; weigh 50g Na 2 CO 3 Add to 500g deionized water to form a sodium carbonate solution;

[0042] Using a peristaltic pump, the above-mentioned mixed solution containing ferrous, nickel, aluminum and sodium carbonate solution flow together to form a reaction solution, which is added to a 5L reactor with 500g of cushion water for precipitation reaction. The reaction temperature is controlled to be 65°C, and the feed time is For 45 minutes, control the feed rate of ammonia water to maintain the reaction pH value at 7.5;

[0043] After the precipitation reaction was completed, feed into the air to carry out the oxidation reaction. The oxidation reaction time was 120 minutes. During this period, the reaction pH value was maintained at 8.0 by controlling the sodium...

Embodiment 2

[0047] Weigh 51.16g FeCl 2 4H 2 O and 0.37g Ni(NO 3 ) 2 ·6H 2 O was dissolved in 600g of deionized water to obtain a mixed solution containing ferrous and nickel; at the same time, 40g of concentrated ammonia water with a concentration of 27wt% was weighed and added to 500g of deionized water to form a dilute ammonia solution, and then 1.96g of Na 2 SiO 3 Dissolved in dilute ammonia solution;

[0048] Using a peristaltic pump, the above-mentioned mixed solution containing ferrous and nickel and the ammonia solution containing silicon flow together to form a reaction solution, which is added to a 5L reactor with 500g of cushion water for precipitation reaction. The reaction temperature is controlled to be 50°C, and the feed time is 35 minutes, control the feed rate of ammonia water to maintain the reaction pH value as 8.0;

[0049] After the precipitation reaction was completed, air was introduced to carry out the oxidation reaction. The oxidation reaction time was 180 mi...

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Abstract

The invention discloses an iron-based catalyst and a preparation method thereof. The iron-based catalyst comprises a compound FeOOH containing a first active ingredient Fe, a compound containing a second active ingredient, and a compound containing a structure promoter ingredient, wherein the second active ingredient comprises one or more elements selected from nickel, molybdenum, cobalt and tungsten; the structure promoter ingredient comprises one or more elements selected from silicon, aluminum and zirconium. Based on the compound FeOOH containing the first active ingredient Fe, the compound containing a second active ingredient comprising one or more elements selected from nickel, molybdenum, cobalt and tungsten and the compound containing the structure promoter ingredient comprising one or more elements selected from silicon, aluminum and zirconium are added to compound Fe, the second active ingredient and the structure promoter so as to achieve the synergistic effect, so that the catalytic activity of the iron-based catalyst is improved, the agglomeration phenomenon of catalysts is overcome, the catalyst dose during the coal liquefaction process is reduced, and the coal conversion rate and the oil production rate are increased.

Description

technical field [0001] The invention relates to the field of coal-to-liquids, in particular to an iron-based catalyst and a preparation method thereof. Background technique [0002] my country is in short supply of petroleum resources, but relatively rich in coal resources. Vigorously developing coal-to-liquids and coal chemical industry is one of the effective means to make up for the shortage of petroleum resources. Coal direct liquefaction is a clean coal technology that converts coal into liquid products by allowing hydrogen to enter the molecular structure of coal and its derivatives under high temperature and high pressure with the help of hydrogen-donating solvents and catalysts. Catalyst plays an important role in the direct coal liquefaction reaction. In the direct coal liquefaction reaction, the catalyst can effectively promote the pyrolysis and hydrogenation of coal, and improve the yield and quality of oil produced. [0003] Iron-based catalysts are cheap and ca...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/883B01J23/888B01J23/881B01J23/755C10G1/06
Inventor 谢晶李克健章序文王洪学高山松
Owner CHNA ENERGY INVESTMENT CORP LTD
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