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Complex catalyst for direct liquefaction of coal, and preparation method thereof

A technology of direct coal liquefaction and catalyst, which is applied in the direction of physical/chemical process catalysts, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., and can solve the problem of complex catalyst recovery process, high price, easy blockage, etc. problem, to achieve excellent catalytic effect, strong hydrogenation function, and easy to scale-up effect

Active Publication Date: 2015-01-21
CCTEG CHINA COAL RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the disadvantages of this type of catalyst are: high price, easy to block, poisoning, and short life
Patents US4417992, US4374100, etc. have studied the recovery method of this type of catalyst. Generally speaking, the recovery process of this type of catalyst is complicated and the cost is high

Method used

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  • Complex catalyst for direct liquefaction of coal, and preparation method thereof
  • Complex catalyst for direct liquefaction of coal, and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0025] Take the natural laterite nickel ore from the Philippines, its iron content is 46%, and its nickel content is 0.87%. Impurities therein are removed, ground to 100 mesh (150 μm), vacuum dried for 3 hours, and directly used as a catalyst for direct coal liquefaction (set as 1# Catalyst, mass ratio Fe:Ni=100:1.9).

Embodiment 2

[0027] Take the natural laterite nickel ore from Indonesia, its iron content is 49%, and its nickel content is 2.45%. Impurities therein are removed, ground to 150 mesh (112 μm), vacuum dried for 3 hours, and directly used as a catalyst for direct coal liquefaction (set as 2# Catalyst, mass ratio Fe:Ni=100:5).

Embodiment 3

[0029] Take the natural laterite nickel ore from Myanmar, its iron content is 48%, and its nickel content is 1.7%. Impurities therein are removed, ground to 200 mesh (74 μm), vacuum dried for 3 hours, and directly used as a catalyst for direct coal liquefaction (set as 3# Catalyst, mass ratio Fe:Ni=100:3.6).

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Abstract

The invention relates to a complex catalyst for direct liquefaction of coal, and a preparation method thereof. The preparation method comprises the steps of simple-processing outdoor natural laterite-nickel ore which includes iron and nickel or more active metal components and is mainly produced in countries of Southeast Asia and the like near the equator, and grinding the laterite-nickel ore into fine powder to obtain the catalyst for direct liquefaction of the coal; or employing the natural laterite-nickel ore or other iron-containing ores as raw materials, loading chemicals or the ores comprising active components of transition metal elements of nickel, molybdenum, cobalt and the like on the iron ores via a manual method to form the complex catalyst for direct liquefaction of the coal. The preparation method by using the natural laterite-nickel ore as the catalyst or by using the laterite-nickel ore or other iron ores as raw materials and manually loading active metal components of cobalt, molybdenum and nickel to prepare the catalyst is simple and mature. By using the prepared complex catalyst for direct liquefaction of the coal to catalyze a direct liquefaction reaction of the coal, the catalyst has the characteristics of low catalyst consumption, high coal conversion rate, high product oil yield, etc.

Description

technical field [0001] The invention relates to a coal direct liquefaction catalyst in the field of coal chemical industry, in particular to a coal direct liquefaction catalyst containing at least two active components and a preparation method thereof. Background technique [0002] The sharp increase in world oil prices and oil consumption and the reduction of oil resources have forced the energy industry to consider developing alternatives that can replace petroleum fuels. Coal is one of the most abundant hydrocarbon resources on earth, and coal can be converted into liquid fuels through hydrogenation reactions. Coal direct liquefaction is a process in which coal, catalysts, and solvents are hydrogenated into liquid fuels and other chemicals in the reaction under high temperature and high pressure conditions. With the development of direct coal liquefaction technology, the reaction conditions of the new generation of direct coal liquefaction technology are more moderate, a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J23/883B01J23/881C10G1/06
Inventor 王勇张晓静李文博史士东颜丙峰钟金龙
Owner CCTEG CHINA COAL RES INST
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