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Method for directly liquefying coal

A coal liquefaction, direct technology, applied in the preparation of liquid hydrocarbon mixture, petroleum industry and other directions, can solve the problem of large consumption of alcohol, and achieve the effects of low raw material cost, reduced methanol consumption and low reaction pressure

Active Publication Date: 2014-02-05
XINJIANG ZHUNDONG GASOLINEEUM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the mass ratio of coal to alcohol has reached 1:5-15, and the alcohol consumption is large

Method used

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  • Method for directly liquefying coal

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0064] A method for direct liquefaction of coal is carried out according to the following steps:

[0065] Step 1, pulverizing and grinding the coal until the particle size is no more than 300 mesh;

[0066] Step 2, mixing the pulverized coal, solvent, and pyrolysis catalyst according to the proportion, fully stirring with a stirring device, performing coal swelling treatment and making coal slurry;

[0067] Step 3: Add the coal slurry to the thermal flash reaction section and heat it together with the circulating gas to 360°C to make the pyrolysis material;

[0068] Step 4: Add the cracking catalyst and co-catalyst to the feeder in proportion, mix well and heat to 410°C;

[0069] Step 5. The feeder continuously feeds the high-temperature cracking catalyst and high-temperature co-catalyst into the pyrolysis material in the thermal flash reaction section at a constant speed, so that it can react directly, and enter the pyrolysis reactor by self-pressure under the condition ...

Embodiment 2

[0073] A method for direct liquefaction of coal is carried out according to the following steps:

[0074] Step 1: pulverizing and grinding the coal until the particle size is not greater than 300 mesh;

[0075] Step 2, mixing the pulverized coal, solvent, and pyrolysis catalyst according to the proportion, fully stirring with a stirring device, performing coal swelling treatment and making coal slurry;

[0076] Step 3: Add the coal slurry to the thermal flash reaction section and heat it together with the circulating gas to 260°C to make the pyrolysis material;

[0077] Step 4: Add the cracking catalyst and co-catalyst to the feeder in proportion, mix well and heat to 280°C;

[0078] Step 5. The feeder continuously feeds the high-temperature cracking catalyst and high-temperature co-catalyst into the pyrolysis material in the thermal flash reaction section at a constant speed, so that it can react directly, and enter the pyrolysis reactor by self-pressure under the condit...

Embodiment 3

[0082] A method for direct liquefaction of coal is carried out according to the following steps:

[0083] Step 1: pulverizing and grinding the coal until the particle size is not greater than 300 mesh;

[0084] Step 2, mixing the pulverized coal, solvent, and pyrolysis catalyst according to the proportion, fully stirring with a stirring device, performing coal swelling treatment and making coal slurry;

[0085] Step 3: Add the coal slurry to the thermal flash reaction section and heat it together with the circulating gas to 380°C to make the pyrolysis material;

[0086] Step 4: Add the cracking catalyst and co-catalyst to the feeder in proportion, mix well and heat to 410°C;

[0087] Step 5. The feeder continuously feeds the high-temperature cracking catalyst and high-temperature co-catalyst into the pyrolysis material in the thermal flash reaction section at a constant speed, so that it can react directly, and enter the pyrolysis reactor by self-pressure under the condit...

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Abstract

The invention belongs to the technical field of coal liquefaction, and more particularly relates to a method for directly liquefying coal by adopting methanol as a hydrogen carrier. The solved technical problem is to provide a direct coal liquefaction method adopting methanol as a hydrogen carrier, wherein the method has characteristics of low reaction pressure and low cost. The adopted technical scheme comprises: crushing raw material coal, uniformly mixing the crushed raw material coal, a solvent and a pyrolysis catalyst, uniformly mixing a cracking catalyst and an auxiliary catalyst, and conveying the mixed catalyst to a reactor filled with the pyrolysis materials, such that the pyrolysis materials are subjected to a reaction under catalysis of the mixed catalyst and enter the pyrolysis reactor through the self-pressure so as to liquefy the coal, wherein the pyrolysis reactor reaction temperature is 280-450 DEG C, the reaction pressure is 1-7 MPa, and the reaction time is 30-120 min. The method is widely used in the technical field of coal liquefaction.

Description

technical field [0001] The invention belongs to the technical field of coal liquefaction, and more specifically, the invention relates to a method for directly liquefying coal with methanol as a hydrogen carrier. Background technique [0002] Solving the shortage of oil based on abundant coal resources is one of the ways to ensure the sustainable development of human beings. The essential difference between coal and petroleum is that coal has a high C / H atomic ratio and a large molecular weight. Coal liquefaction is a technology that improves the hydrogen-to-carbon atomic ratio of coal to produce liquid hydrocarbons with suitable molecular weights as the main product. Coal liquefaction processes include direct liquefaction and indirect liquefaction. The direct coal liquefaction process is one of the most effective coal liquefaction methods. [0003] As early as 1913, the German chemist Bergius first successfully studied the high-pressure hydrogenation of coal, which la...

Claims

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Application Information

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IPC IPC(8): C10G1/06
Inventor 史万年秦勇张福强
Owner XINJIANG ZHUNDONG GASOLINEEUM TECH