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Catalytic gasification method of high ash anthracite

An anthracite, high-ash technology, applied in the gasification process, the manufacture of combustible gas, the petroleum industry, etc., can solve the problems of the catalytic gasification reaction cannot be carried out smoothly, the content of oxygen-containing functional groups is low, and the catalyst loses catalytic activity.

Active Publication Date: 2019-01-22
ENN SCI & TECH DEV
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  • Abstract
  • Description
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Problems solved by technology

[0003] In the above-mentioned catalytic gasification method of high-ash anthracite, commonly used catalysts are potassium salts, sodium salts, calcium salts, etc. Since the content of oxygen-containing functional groups in high-ash anthracite is low, the catalyst is combined with the oxygen-containing functional groups in high-ash anthracite The formation of high catalytic activity sites is less, which makes the catalytic gasification reaction of high ash anthracite cannot be carried out effectively, especially when calcium salt catalyst is used.
In addition, the potassium salt or sodium salt catalyst will also react with the alumina and silica in high-ash anthracite to form aluminosilicate, which will cause the catalyst to lose its catalytic activity, and then make the catalytic gasification reaction of high-ash anthracite difficult to proceed smoothly.

Method used

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  • Catalytic gasification method of high ash anthracite
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  • Catalytic gasification method of high ash anthracite

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] The ash content is 21%, the aluminum oxide content in the ash is 25%, and the high ash content anthracite of silicon oxide content is 50% is crushed to below 40 meshes, then weighs 20g of the high ash content anthracite after crushing, and puts it into poly In the vinyl fluoride reactor, then add the hydrofluoric acid of 200ml 1mol / L and the hypochlorous acid of 40ml 1mol / L in the polytetrafluoroethylene reactor, to form the first mixture, at room temperature (20 ℃) ​​for the first The mixture was stirred for 1 h. Then, the first mixture is subjected to solid-liquid separation, and the solid obtained from the solid-liquid separation is pretreated high-ash anthracite. After measurement, the ash content in the pretreated high ash anthracite is 14%, the alumina content in the ash is 13.7%, the silicon oxide content in the ash is 27.5%, and the content of oxygen-containing functional groups in the pretreated high ash anthracite is 8.3 %. After calculation, the removal rat...

Embodiment 2

[0043] The ash content is 30%, the alumina content in the ash is 40%, the high ash content anthracite coal that the silicon oxide content is 30% is crushed to below 40 meshes, then weighs 20g of the crushed high ash content anthracite, and puts it into poly In the vinyl fluoride reactor, then add 300ml of 3mol / L tetrafluoroboric acid and 80ml of 5mol / L sodium hypochlorite aqueous solution to the polytetrafluoroethylene reactor to form the first mixture. Then the first mixture was heated so that the temperature of the heated first mixture was 40° C., and the first mixture was stirred for 2 hours. Then, the first mixture is subjected to solid-liquid separation, and the solid obtained from the solid-liquid separation is pretreated high-ash anthracite. After measurement, the ash content in the pretreated high ash anthracite is 10%, the alumina content in the ash is 35.4%, the silicon oxide content in the ash is 17.6%, and the content of oxygen-containing functional groups in the p...

Embodiment 3

[0055]The ash content is 21%, the aluminum oxide content in the ash is 25%, and the high ash content anthracite of silicon oxide content is 50% is crushed to below 40 meshes, then weighs 20g of the high ash content anthracite after crushing, and puts it into poly In the vinyl fluoride reactor, 250ml of 2mol / L hydrofluoric acid and 60ml of 4mol / L hypochlorous acid were then added to the polytetrafluoroethylene reactor to form a first mixture. Then the first mixture was heated so that the temperature of the heated first mixture was 50° C., and the first mixture was stirred for 1 h. Then, the first mixture is subjected to solid-liquid separation, and the solid obtained from the solid-liquid separation is pretreated high-ash anthracite. After measurement, the ash content in the pretreated high ash anthracite is 7%, the alumina content in the ash is 18.7%, the silicon oxide content in the ash is 29.5%, and the content of oxygen-containing functional groups in the pretreated high as...

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Abstract

The invention discloses a catalytic gasification method for high-ash anthracite, relates to the technical field of high-ash anthracite gasification, and is used for making the catalytic gasification reaction of high-ash anthracite proceed smoothly. The catalytic gasification method of the high-ash anthracite comprises: pretreating the high-ash anthracite to reduce the content of alumina and silicon oxide in the high-ash anthracite, and increasing the content of oxygen-containing functional groups in the high-ash anthracite; The high-ash anthracite is loaded with catalyst; the catalyst-loaded high-ash anthracite is subjected to catalytic gasification. The invention is used for catalytic gasification treatment of high-ash anthracite.

Description

technical field [0001] The invention relates to the technical field of gasification of high-ash anthracite, in particular to a catalytic gasification method of high-ash anthracite. Background technique [0002] High-ash anthracite has the characteristics of high ash content and low content of oxygen-containing functional groups, wherein the main components of ash are alumina and silica. At present, in order to improve the utilization efficiency of high-ash anthracite, catalytic gasification method is usually used to convert high-ash anthracite into gas. [0003] In the above-mentioned catalytic gasification method of high-ash anthracite, commonly used catalysts are potassium salts, sodium salts, calcium salts, etc. Since the content of oxygen-containing functional groups in high-ash anthracite is low, the catalyst is combined with the oxygen-containing functional groups in high-ash anthracite The formation of high catalytic activity sites is less, so that the catalytic gasi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10J3/16C10J3/80
CPCC10J3/16C10J3/80C10J2300/0903C10J2300/093C10J2300/0986
Inventor 王会芳李鹏李克忠
Owner ENN SCI & TECH DEV