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Coal carbon dioxide gasification catalyst and preparation method thereof

A carbon dioxide and catalyst technology, applied in the field of coal gasification, can solve the problems of reducing the recycling rate of catalysts, increasing the usage of catalysts, and increasing the cost of coal gasification, etc., and achieve the effects of high recycling rate, strong mechanical strength and good physical form

Inactive Publication Date: 2015-09-16
宋华
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this also creates a problem that it is difficult to completely recycle the catalyst due to the strong interaction (such as chemical bonds) with the carbon-based solid reactant particle residue after the gasification reaction, which greatly reduces the recycling rate of the catalyst and causes a large amount of catalyst usage. increase, resulting in a significant increase in the cost of coal gasification

Method used

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  • Coal carbon dioxide gasification catalyst and preparation method thereof
  • Coal carbon dioxide gasification catalyst and preparation method thereof
  • Coal carbon dioxide gasification catalyst and preparation method thereof

Examples

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Embodiment 1

[0049] 10%K-10%Mg / 38%SnO 2 -29%Fe 2 o 3 -33%Al 2 o 3 , the meaning of this molecular formula is: the carrier is composed of SnO with a mass ratio of 38% 2 , 29% Fe 2 o 3 , and 33% Al 2 o 3 composition. The carbon active sites consist of 10% K and 10% Mg, accounting for the total weight of the catalyst.

[0050] Its preparation process is as follows:

[0051] 1) Synthesized from SnO 2 -Fe 2 o 3 -Al 2 o 3 Composition carrier:

[0052] 1-1) Weigh 12.79g tin chloride (SnCl 4 ), 28.12g iron nitrate (Fe(NO 3 ) 3 ) and 47.68g aluminum nitrate (Al(NO 3 ) 3 ), and dissolve it into 200mL deionized water to prepare A solution;

[0053] 1-2) Measure out 400mL ammonia solution as B solution;

[0054] 1-3) Pump solution A at a rate of 2.5mL / min into a settling tank filled with 200mL of initial deionized water at 40°C;

[0055] 1-4) At the same time, by adjusting the addition rate of solution B to maintain the pH value (pH) in the sedimentation tank equal to 8 ± 0.2; ...

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Abstract

The invention discloses a coal carbon dioxide gasification catalyst and a preparation method thereof. The catalyst is composed of carbon active site loaded on a carrier, the carrier can provide machinery support and can transfer the oxygen atoms or oxygen ions, the carrier contains CO2 active site; the carbon active site and CO2 active site in the carrier are taken as catalytic activity components, transfer for oxygen ions is realized by a oxidation reduction reaction; the carrier transfers the oxygen atoms or oxygen ions, CO2 is taken as an oxidizing agent, and then ground state carbon is gasified to CO. The catalyst has good catalytic activity, compared with a traditional catalyst, the catalyst in the invention has stronger catalysis performance, and the catalysis condition is more peaceful.

Description

Technical field: [0001] The invention belongs to the technical field of coal gasification, and in particular relates to a coal carbon dioxide gasification catalyst and a preparation method thereof. Background technique: [0002] According to literature reports, most of the catalysts used for gasification coal function in the environment of water vapor or air. For example, in the 1970s, the American Exxon Company proposed the K 2 CO 3 As a catalyst, under the conditions of 3MPa and 700°C, using water vapor as a gasification agent, a coal pressurized fluidized bed catalytic gasification process for the purpose of producing artificial natural gas was developed, and Chinese patent CN103301865A also made further improvements on this . Carbon dioxide is a weaker oxidizing agent than water vapour. Due to its own structural stability, carbon dioxide is very chemically inert. Therefore, the catalytic activity of the existing coal gasification catalysts will be greatly reduced in ...

Claims

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Application Information

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IPC IPC(8): B01J23/835B01J23/10B01J23/825B01J23/78B01J23/14B01J23/83B01J23/18B01J23/04B01J23/28C10J3/00
CPCY02P20/52
Inventor 宋华
Owner 宋华