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Highly dispersed coal/heavy oil hydrogenation co-refining catalyst prepared by carrier coal modification

A heavy oil hydrogenation, high dispersion technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, preparation of liquid hydrocarbon mixtures, etc. The problems of aggregation and accumulation and the small specific surface area of ​​the carrier coal can achieve the effect of easy and cheap raw material availability, environmental friendliness, and increased loading capacity.

Pending Publication Date: 2020-09-22
CHINA UNIV OF PETROLEUM (EAST CHINA)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, the dispersion methods are mainly divided into two types: one is the coal loading method introduced through coal blending, and the other is the oil-soluble method introduced through oil blending. Chuan Li et al. synthesized an oil-soluble iron-nickel catalyst and used it in The hydrogenation reaction performance of lignite Marui residual oil system was investigated, and it can be dispersed well when it is directly added to the reaction system. Among them, iron and nickel form a mixed crystal phase during the vulcanization process, so that the two metals have a synergistic effect. The dry base ash-free coal The conversion rate is as high as 97%, but the extensive use of oil-soluble ligands makes the synthesis cost high, and industrial application cannot be realized
Deng Wen'an et al. used lignite as a carrier to synthesize a coal-supported catalyst with Fe / Mo as an active component by impregnation method, and found that the addition of a second metal component can promote the improvement of coal conversion rate, and the particle size of the iron-based catalyst is less than 50nm , and the dispersion degree in the system is high, but the specific surface area of ​​the carrier coal is small, especially when the loading capacity is high, the active components are easy to gather and accumulate, and the dispersion degree needs to be improved

Method used

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  • Highly dispersed coal/heavy oil hydrogenation co-refining catalyst prepared by carrier coal modification
  • Highly dispersed coal/heavy oil hydrogenation co-refining catalyst prepared by carrier coal modification
  • Highly dispersed coal/heavy oil hydrogenation co-refining catalyst prepared by carrier coal modification

Examples

Experimental program
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Effect test

Embodiment 1

[0035] This example provides a carrier coal modification to prepare a highly dispersed briquette / heavy oil hydrogenation co-smelting catalyst, which is a highly dispersed catalyst with pore-forming pretreated coal powder as the carrier and metal iron and nickel as the active component. The preparation method of described catalyst comprises the steps:

[0036] (1) Put the carrier coal in a blast drying oven at 110°C for 3 hours of drying treatment;

[0037] (2) Get 2.3705g of ferrous sulfate heptahydrate and 2.3593g of nickel nitrate hexahydrate and add deionized water to prepare a uniform solution, mix and stir 10g of coal powder and mixed salt solution, and disperse evenly by ultrasonic vibration;

[0038] (3) Under magnetic stirring, add 2 mol / L ammonia solution dropwise to carry out precipitation reaction, control the temperature at 30°C, pH value is 7, react for 2 hours, and obtain the precipitate;

[0039] (4) Add alkaline solution drop by drop under the situation of vio...

Embodiment 2

[0043] This example provides a carrier coal modification to prepare a highly dispersed briquette / heavy oil hydrogenation co-smelting catalyst, which is a highly dispersed catalyst with pore-forming pretreated coal powder as the carrier and metal iron and nickel as the active component. The preparation method of described catalyst comprises the steps:

[0044] (1) Place the raw coal powder in a tube furnace under the protection of nitrogen, the heating rate is 10°C / min, the carbonization temperature is 500°C, the carbonization is 80min, and the carbonization material is obtained by cooling;

[0045] (2) Fully mix and stir the carbonized material and the activator, the activator is KOH, the mass ratio of the carbonized material to the activator is 2.5:1, maintain at 800°C for 60 minutes; after cooling to room temperature, use 0.1mol / L hydrochloric acid Wash with deionized water until neutral, and the product is dried to obtain a porous material with a high specific surface area;...

Embodiment 3

[0052] This example provides a carrier coal modification to prepare a highly dispersed briquette / heavy oil hydrogenation co-smelting catalyst, which is a highly dispersed catalyst with pore-forming pretreated coal powder as the carrier and metal iron and nickel as the active component. The preparation method of described catalyst comprises the steps:

[0053] (1) Place the raw coal powder in a tube furnace under the protection of nitrogen, the heating rate is 5°C / min, the carbonization temperature is 550°C, carbonization is 60min, and the carbonization material is obtained by cooling;

[0054] (2) Fully mix and stir the carbonized material and the activator, the activator is NaOH, the mass ratio of the carbonized material to the activator is 2:1, maintain at 850°C for 60 minutes; after cooling to room temperature, use 0.1mol / L hydrochloric acid Wash with deionized water until neutral, and the product is dried to obtain a porous material with a high specific surface area;

[0...

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Abstract

The invention discloses a highly dispersed coal / heavy oil hydrogenation co-refining catalyst prepared by carrier coal modification, belongs to the technical field of coal-heavy oil hydrogenation co-refining, and is a highly dispersed catalyst taking coal powder subjected to pore-forming pretreatment as a carrier and taking metal iron nickel as an active component. The preparation method of the catalyst comprises the following steps: carbonizing raw material coal powder; fully mixing and uniformly stirring the carbonized material and an activating agent, and maintaining the temperature at 750-850 DEG C for 60 minutes; washing to be neutral, and drying to obtain a porous material; uniformly stirring and mixing the porous material and the iron-nickel mixed salt solution; dropwise adding an alkaline solution to generate precipitate; introducing air for oxidation reaction; and carrying out reduced pressure suction filtration, washing, vacuum drying, grinding and screening to obtain the product. The coal powder is subjected to activation pretreatment, so that the specific surface area of the coal powder is increased, the dispersity of the active components on the surface of the coal powder is improved, the loading capacity of the active components is improved, and the dispersion process of the catalyst in the conventional coal-oil suspended bed hydrogenation co-processing is greatlysimplified.

Description

technical field [0001] The invention relates to the technical field of coal-heavy oil hydrogenation co-smelting, in particular to a carrier coal modification to prepare highly dispersed coal / heavy oil hydrogenation co-smelting catalyst. Background technique [0002] my country's national energy composition is mainly coal resources, but the direct combustion of a large amount of coal will bring a heavy burden to the environment. Oil and natural gas resources are relatively scarce, crude oil is heavy and inferior, and the demand for light oil is increasing. With economic development, my country's dependence on foreign crude oil is increasing year by year. Therefore, in coal-rich and oil-poor countries, kerosene co-refining technology It has attracted many researchers. The kerosene co-refining technology is a new type of direct coal liquefaction technology that uses petroleum heavy / inferior oil as solvent oil. It utilizes the synergy between coal powder and heavy oil to convert ...

Claims

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Application Information

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IPC IPC(8): B01J23/755C10G1/00C10G47/12
CPCB01J23/755C10G1/002C10G47/12
Inventor 邓文安刘聪聪李传罗辉杜峰李庶峰杨腾飞
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)
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