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

A technology of Fischer-Tropsch synthesis and iron carbide, which is applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, catalysts for physical/chemical processes, etc., can solve the problem of high selectivity of by-products, achieve simple and easy raw materials, and simple operation steps , The effect of low CO2 selectivity

Pending 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 in order to solve how iron-based catalyst obtains the pure-phase iron carbide material that does not contain Fe impurity, and improves the stability of carrying out Fischer-Tropsch synthesis reaction, reduces CO simultaneously 2 or CH 4 The problem of high selectivity of by-products provides a composition containing supported χ iron carbide and θ iron carbide, its preparation method, catalyst and application, and a method for Fischer-Tropsch synthesis

Method used

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

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Embodiment approach

[0061] In a preferred embodiment of the present invention, the drying and roasting process includes: firstly drying the impregnated carrier at 20-30°C for 0.5-4h, and then drying drying at low temperature for 6-10 hours, drying the dried material at 110-150° C. for 3-24 hours, and then roasting the obtained material at 300-550° C. for 1-10 hours. The above drying process can be performed in an oven, and the roasting process can be performed in a muffle furnace.

[0062] Another embodiment provided by the present invention is to prepare supported θ iron carbide.

[0063] In some embodiments of the present invention, preferably, H in step (1-1) 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 first reduction, preferably, in step (1-1), the pressure of the first reduction is 0.1-15atm, preferably 0.3-2.6atm; time is 0.7-15h, preferably 1 -12h.

[0064] In some embodimen...

preparation example 1

[0110] (1) Weigh 10 g of silicon oxide as a carrier, and then impregnate it with an aqueous solution of ammonium ferric citrate, wherein the aqueous solution of ammonium ferric citrate is weighed and configured according to the content of 30 wt% of elemental iron in the final carrier. Dry the impregnated carrier at 35°C for 2 hours, then dry it in a vacuum oven at a temperature of 30°C and a vacuum of 300Pa for 8 hours, dry the dried material in an oven at 120°C for 24 hours, and then dry the obtained material at a temperature of Baked in a muffle furnace at 500 °C for 5 h. Obtain a loaded iron-based precursor;

[0111] (2) Combine the precursor with H 2 At a pressure of 2.0 atm, H 2 The flow rate is 16000mL / h / g, and the second reduction is carried out at a temperature of 610°C for 1h;

[0112] (3) Cool the product obtained in step (2) to 30°C, and at 30°C 2 Inert gas contact for surface passivation treatment, O in the gas 2 The volume concentration is 1.0%, the pressure ...

preparation example 2

[0116] (a) Weigh 10 g of silicon oxide as a carrier, and then impregnate it with an aqueous solution of ammonium ferric citrate, wherein the aqueous solution of ammonium ferric citrate is weighed and configured according to the content of 30 wt% of elemental iron in the final carrier. Dry the impregnated carrier at 30°C for 3 hours, then dry it in a vacuum oven at a temperature of 35°C and a vacuum of 320Pa for 8 hours, dry the dried material in an oven at 115°C for 24 hours, and then dry the obtained material at a temperature of Baked in a muffle furnace at 500 °C for 5 h. Obtain a loaded iron-based precursor;

[0117] (b) Combine the precursor with H 2 At a pressure of 2.0 atm, H 2 The flow rate is 14000mL / h / g, and the first reduction is carried out at a temperature of 460°C for 12h;

[0118] (c) cooling the product obtained in step (b) from 460°C to 390°C at a rate of 1.5°C / min, and at this temperature with H 2 Contact with CO mixed gas to prepare the first carbide, the...

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Abstract

The invention relates to the field of Fischer-Tropsch synthesis reaction, and discloses a composition containing supported chi iron carbide and theta iron carbide, a preparation method of the composition, a catalyst, application of the catalyst and a Fischer-Tropsch synthesis method. The composition containing supported x iron carbide and theta iron carbide comprises 55-90 wt% of a carrier and 10-45 wt% of an iron component, wherein based on the total amount of the iron, the iron component comprises 95-100 mol% of x iron carbide and theta iron carbide, and 0-5 mol% of an Fe-containing impurity, and the Fe-containing impurities are iron-containing substances except for chi iron carbide and theta iron carbide. According to the invention, Chi iron carbide and theta iron carbide can be simplyand conveniently prepared and are used as active components to obtain 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 loaded χ iron carbide and 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 carbo...

Claims

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Application Information

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IPC IPC(8): B01J27/22C10G2/00
CPCB01J27/22C10G2/332B01J35/613B01J35/615
Inventor 王鹏林泉吕毅军张魁孟祥堃门卓武孙琦
Owner CHNA ENERGY INVESTMENT CORP LTD