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Composition containing precipitated theta iron carbide, preparation method of composition, catalyst, application of catalyst, and Fischer-Tropsch synthesis method.

A Fischer-Tropsch synthesis and composition technology, which is used in the preparation of liquid hydrocarbon mixtures, catalysts for physical/chemical processes, chemical instruments and methods, etc. The effect of low CO2 selectivity

Active Publication Date: 2021-03-30
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0012] The purpose of the present invention is to solve how iron-based catalysts can obtain pure-phase iron carbide materials without Fe impurities, and improve the stability of Fischer-Tropsch synthesis while reducing CO 2 or CH 4 The problem of high selectivity of by-products provides a composition containing precipitated θ iron carbide and its preparation method, catalyst and application, and a method for Fischer-Tropsch synthesis

Method used

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  • Composition containing precipitated theta iron carbide, preparation method of composition, catalyst, application of catalyst, and Fischer-Tropsch synthesis method.
  • Composition containing precipitated theta iron carbide, preparation method of composition, catalyst, application of catalyst, and Fischer-Tropsch synthesis method.
  • Composition containing precipitated theta iron carbide, preparation method of composition, catalyst, application of catalyst, and Fischer-Tropsch synthesis method.

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Embodiment approach

[0045] In a preferred embodiment of the present invention, the drying and roasting process includes: first drying the solid at a temperature of 35-80°C and a vacuum of 250-1200Pa for 6-10 hours; Dry at 75-180°C for 3-24h, and then roast the obtained material at 250-580°C for 1-10h. The above drying process can be performed in an oven, and the roasting process can be performed in a muffle furnace.

[0046] In some embodiments of the present invention, step (2) can simultaneously generate nano-iron powder in situ from the iron element in the precursor and reduce the generated nano-iron powder.

[0047] In some embodiments of the present invention, H in step (2) 2 Can be H 2 The form of flow is passed into the reaction system, and at the same time, by controlling the H 2 Flow pressure to control the pressure of the precursor reduction, preferably, in step (2), the pressure of the precursor reduction is 0.1-15atm, preferably 0.3-2.6atm, and the time is 0.7-15h, preferably 1-12h...

Embodiment 1

[0084] (1) Mix ferric nitrate with a concentration of 1.2mol / L and 0.9mol / L sodium carbonate solution at 55°C and pH=6.2 to obtain a precipitated slurry, wash with deionized water, filter to obtain a filter cake, and dry at 110°C 24h, 400°C calcined for 10h to obtain the precursor.

[0085] (2) Combine the precursor with H 2 At a pressure of 2.6atm, H 2 The flow rate is 22000mL / h / g, and the precursor reduction is carried out at a temperature of 470°C for 12h;

[0086] (3) Cool the product obtained in step (2) from 470°C to 400°C at a rate of 1.5°C / min, and mix with H at this temperature 2 Contact with CO mixed gas to prepare precipitated carbides, the conditions are: pressure 20atm, total gas flow 20000mL / h / g, H 2 The molar ratio to CO is 60:1, and the treatment time is 24 hours to obtain precipitated iron carbide, which is determined as pure θ iron carbide by Mössbauer spectroscopy, which is recorded as iron carbide 1;

[0087] (4) Under the protection of Ar gas, mix 97 m...

Embodiment 2

[0089] (1) Mix the ammonium carbonate solution with a concentration of 1.3mol / L ferric ammonium citrate and 0.7mol / L at 65°C and pH=6.9 to obtain a precipitated slurry, wash with deionized water, and filter to obtain a filter cake, 110 ℃ drying for 24 hours, and 300 ℃ calcination for 10 hours to obtain the precursor.

[0090] (2) Combine the precursor with H 2 At a pressure of 0.3atm, H 2 The flow rate is 2800mL / h / g, and the precursor reduction is carried out at a temperature of 620°C for 1h;

[0091] (3) Cool the product obtained in step (2) from 620°C to 300°C at a rate of 1.5°C / min, and mix with H at this temperature 2 Contact with CO mixed gas to prepare precipitated carbides, the conditions are: pressure 0.01atm, total gas flow 1200mL / h / g, H 2 The molar ratio to CO is 60:1, and the treatment time is 80h, to obtain precipitated iron carbide, which is determined as pure θ iron carbide by Mössbauer spectroscopy, which is recorded as iron carbide 2;

[0092] (4) Under the...

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Abstract

The invention relates to the field of Fischer-Tropsch synthesis reaction, and discloses a composition containing precipitated theta iron carbide, a preparation method of the composition, a catalyst, application of the catalyst, and a Fischer-Tropsch synthesis method. The composition containing precipitated theta iron carbide comprises 95-100 mol% of precipitated theta iron carbide and 0-5 mol% ofan Fe-containing impurity, wherein the Fe-containing impurity is an iron-containing substance other than theta iron carbide, and the specific surface area of the composition is 20-275 m<2> / g. According to the invention, theta iron carbide can be simply and conveniently prepared and is used as an active component to obtain a continuous and stable Fischer-Tropsch synthesis reaction, and the selectivity of effective products is high.

Description

technical field [0001] The invention relates to the field of Fischer-Tropsch synthesis reaction, in particular to a composition containing precipitated θ iron carbide, a preparation method thereof, a catalyst and its application, and a method of Fischer-Tropsch synthesis. Background technique [0002] my country's primary energy structure is characterized by rich coal, short of oil, and little gas. With the development of my country's economy, the dependence on foreign oil has been increasing. [0003] Fischer-Tropsch synthesis is an increasingly important energy conversion pathway in recent years, which can combine carbon monoxide with H 2 of syngas into liquid fuels and chemicals. [0004] The reaction equation of Fischer-Tropsch synthesis is as follows: [0005] (2n+1)H 2 +nCO→C n h 2n+2 +nH 2 O(1), [0006] 2nH 2 +nCO→C n h 2n +nH 2 O (2). [0007] In addition to alkanes and alkenes, industrial Fischer-Tropsch synthesis produces by-product carbon dioxide (CO...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/22B01J37/03B01J35/10B01J37/18C10G2/00
CPCB01J27/22B01J37/03B01J37/031B01J37/18C10G2/332B01J35/613B01J35/615
Inventor 王鹏林泉赵华博缪平门卓武孟祥堃张琪
Owner CHNA ENERGY INVESTMENT CORP LTD
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