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Method for liquifying coal mildly

A process method and mild technology, applied in the field of clean energy technology and coal chemical industry, can solve problems such as environmental pollution, low relative output, narrow adaptability of raw materials, etc., to reduce the difficulty of process operation, high energy conversion efficiency, and high added value of products Effect

Active Publication Date: 2014-02-05
EAST CHINA UNIV OF SCI & TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

At present, there are some representative coal liquefaction technologies, such as: 1) Fischer-Tropsch synthesis, which generates synthesis gas (carbon monoxide and hydrogen) from coal gasification, and then uses the synthesis gas as raw material to synthesize liquid fuels and chemical products, but its process has some limitations. Disadvantages, such as high hydrogen demand, high cost, low relative output, and low thermal efficiency; 2) Coal is directly liquefied, and coal undergoes hydrogenation reaction under certain conditions, and the product is separated to obtain oil, gas, water and solid residue. The oil product is then hydrogenated to obtain liquid fuel. The main technical core is the high-pressure hydrogenation and dissolution process of coal, which has disadvantages such as difficulty in catalyst separation, easy blockage of coal slurry heat exchanger, and difficulty in high-temperature and high-pressure solid-liquid separation.
Chinese patents CN1438294A and CN101987962A introduce two coal liquefaction processes, each of which has different process characteristics, but both have disadvantages such as high pressure, high hydrogen consumption, and narrow raw material adaptability, resulting in low economic efficiency and poor practicability
In addition, direct combustion or gasification of volatile matter in coal fails to realize cascade utilization of resources, which not only causes waste of coal resources, but also causes environmental pollution

Method used

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  • Method for liquifying coal mildly
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  • Method for liquifying coal mildly

Examples

Experimental program
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Effect test

Embodiment 1

[0044] Dry and pulverize the Shengli lignite, stir and mix it with the catalyst ferrous sulfide (catalyst / coal=1:20) and the hydrogen donating solvent tetrahydronaphthalene (solvent-coal ratio 3:1) to make oil-coal slurry, heat it to 350°C and pass it into In the reactor Ⅰ, the pressure is 4MPa. After keeping for 30 minutes, it is transported into the reactor Ⅱ for decompression flashing, and then the middle oil steam at 450°C is introduced to purge, and then the non-condensable gas at 450°C is added to further crack and coke, and then pass through Enter water vapor to cool down and strip, and decoke after the end. In this example, high gray coke is not used for hydrogen production. Product yield (dry ash-free basis): light oil yield 14.1%, medium oil yield 16.0%, heavy oil yield 11.4%, residue oil yield 6.4%, non-condensable gas yield 15.3%, water yield 8.3%, coke Yield 28.5%.

Embodiment 2

[0046] Dry and pulverize Shengli lignite, stir and mix with catalyst ferrous sulfide (catalyst / coal = 1:20), hydrogen-donating solvent anthracene oil (solvent-to-coal ratio 3:1) to make oil-coal slurry, heat to 350°C and pass into the reaction In the reactor Ⅰ, the pressure is 4MPa at this time, a certain amount of anthracene oil hydrogenation tail gas and non-condensable gas are introduced, kept for 30 minutes, and then transported to the reactor Ⅱ for decompression flash evaporation, and at the same time, 450°C medium oil steam is introduced for purging. Continuously inject the slurry into the reactor II(a) for several times, then add non-condensable gas at 450°C to further crack and coke, then pass in water vapor to lower the temperature and strip, and decoke after the end. In this example, high gray coke is not used for hydrogen production. Product yield (dry ash-free basis): light oil yield 11.3%, medium oil yield 13.0%, heavy oil yield 11.7%, residue oil yield 5.7%, non-...

Embodiment 3

[0048] Dry and pulverize Shendong electric power coal, stir and mix with catalyst ferrous sulfide (catalyst / coal = 1:20), hydrogen-donating solvent (20% tetrahydronaphthalene, solvent-to-coal ratio 3:1) to make oil-coal slurry, and heat to After 350°C, it is passed into the reactor Ⅰ, and a certain amount of anthracene oil hydrogenation tail gas and non-condensable gas are passed in, and the pressure is 4MPa. 450°C medium oil steam purge, inject the slurry into the reactor II (a) several times continuously, when the reactor II (a) is almost full, switch the valve to the reactor II (b), at this time the slurry is injected into the reaction Reduced pressure flash evaporation is carried out in the device II (b). Add non-condensable gas at 450°C to reactor II(a) to further crack and coke, then pass in water vapor to lower the temperature and strip, and decoke after the end. Product yield (dry ash-free basis): light oil yield 9.1%, medium oil yield 10.1%, heavy oil yield 9.4%, res...

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Abstract

The invention relates to a method for liquifying coal mildly. The method mainly comprises steps of dry smashing coal samples and mixing with catalyst and hydrogen-donor solvent to form thick liquid; heating and then injecting into a reactor I, carrying out catalytic hydrogenation reaction on coal and hydrogen-donor solvent under mild condition, continuously dissolving out soluble components in products and coal; then injecting into a reactor II, flash distilling part of the product and solvent, rising temperature so as to split and coke left products to generate low boiling point compound and coke, wherein the coke can be used for preparing activated carbon and hydrogen. After the product which is vacuum flashed and purged through steam stripping is separated, different components are obtained, the component below 200 DEG C is condensed so as to obtain light oil, non-condensed gas and water, 200-300 DEG C component is condensed so as to obtain middle oil, after hydrotreating, the middle oil can be used as hydrogen-donor solvent, 300-500 DEG C component is condensed so as to obtain heavy oil which can be used for preparing chemicals or advanced carbon materials, and the component above 500 DEG C is condensed so as to obtain residual oil which can be used for preparing advanced carbon materials. The method has mild reaction conditions, the reactor is coupling, the efficient of the equipment is high, the yield of liquid product is high, the investment of the equipment is low, and the energy conversion efficiency is high.

Description

technical field [0001] The invention relates to a process method of coal temperature liquefaction, belongs to the field of clean energy technology and coal chemical industry, and refers to the production of hydrocarbon fuels and chemicals with coal. Background technique [0002] Coal liquefaction is a technology for producing gasoline, diesel, aviation kerosene and other chemicals from coal, which can be generally divided into two categories: direct liquefaction and indirect liquefaction. Developing coal conversion technology with high technological content, good economic benefits, and environmental friendliness, and transforming coal processing into clean and efficient secondary energy such as liquid fuel and gas fuel, is based on domestic energy advantages, ensuring sustainable energy development, and strengthening energy strategies An important way of safety. [0003] Coal liquefaction yields products in various forms, such as ash-free coal, fuel oil, synthetic crude oil...

Claims

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Application Information

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IPC IPC(8): C10G1/08C10G1/00
Inventor 吴幼青吴诗勇高晋生李良
Owner EAST CHINA UNIV OF SCI & TECH
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