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Iron-based catalyst for direct coal liquefaction and preparation method thereof

A technology for direct liquefaction of coal and catalyst, applied in the field of coal chemical industry, can solve the problems of long preparation process, great difficulty in continuous production, and high water consumption of catalyst

Active Publication Date: 2021-08-20
CHNA ENERGY INVESTMENT CORP LTD +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalysts prepared by these two methods all have high catalytic activity, but the water consumption of the catalysts prepared by these two methods is relatively high, and both involve the steps of filtration, which makes continuous production more difficult and equipment malfunctions The rate is high, and it is difficult to develop large-scale applications
[0008] Therefore, the preparation method of iron-based catalysts in the prior art mainly has the disadvantages of high water consumption, high energy consumption, and more waste water generation, and the preparation process is long and complicated, high in cost, difficult in continuous production, and not suitable for large-scale Develop application

Method used

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  • Iron-based catalyst for direct coal liquefaction and preparation method thereof
  • Iron-based catalyst for direct coal liquefaction and preparation method thereof
  • Iron-based catalyst for direct coal liquefaction and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0092]Embodiment 1. obtains catalyst on the continuous preparation device of 100kg / h according to the method of the present invention

[0093] Prepare ferrous sulfate solution concentration 25wt%, feed flow rate is 22kg / h; Ammonia concentration is 25wt%, feed flow rate is 5kg / h, pressurized feed to static mixer by metering pump respectively, by adjusting ferrous sulfate solution The reaction temperature of the static mixer is controlled at 50°C; the feed rate of pulverized coal is adjusted to 100kg / h; the slurry is atomized and sprayed on the three nozzles mounted on the front end of the absorption oxidation reactor, and the diameters of the three nozzles are adjusted. Make 80% of the droplet diameter between 0.5 mm and 1 mm; adjust the rotation speed of the absorption oxidation reactor so that the residence time of the pulverized coal in the absorption oxidation reactor is about 30 minutes. Adjust the air inlet speed and combustion load of the hot blast stove so that the hot ...

Embodiment 2

[0094] Embodiment 2. obtains catalyst on the continuous preparation device of 100kg / h according to the method of the present invention

[0095] Prepare ferrous sulfate solution concentration 15wt%, flow velocity is 30kg / h, ammoniacal liquor concentration is 15wt%, flow velocity is 7kg / h, pressurized feed to static mixer by metering pump respectively, and static mixer reaction temperature is 50 ℃; Coal The powder feed rate is 100kg / h; the slurry is atomized and sprayed on the three nozzles loaded on the front end of the absorption oxidation reactor, and the diameters of the three nozzles are adjusted so that 80% of the droplet diameter is between 0.5mm and 1mm; Adjust the rotational speed of the absorption oxidation reactor so that the residence time of the pulverized coal in the absorption oxidation reactor is about 30 minutes. Adjust the air intake speed and combustion load of the hot blast stove so that the hot air flow in the absorption oxidation reactor is 5000Nm 3 / h, th...

Embodiment 3

[0096] Embodiment 3. obtains catalyst according to the method of the present invention on the continuous preparation device of 100kg / h

[0097] Prepare ferrous sulfate solution concentration 35wt%, flow velocity is 25kg / h, ammoniacal liquor concentration is 35wt%, flow velocity is 5kg / h, pressurized feed to static mixer by metering pump respectively, and static mixer reaction temperature is 50 ℃; Coal The powder feed rate is 100kg / h; the slurry is atomized and sprayed on the three nozzles loaded on the front end of the absorption oxidation reactor, and the diameters of the three nozzles are adjusted so that 80% of the droplet diameter is between 0.5mm and 1mm; Adjust the rotational speed of the absorption oxidation reactor so that the residence time of the pulverized coal in the absorption oxidation reactor is about 30 minutes. Adjust the air inlet speed and combustion load of the hot blast stove so that the hot air flow in the absorption oxidation reactor is 5000Nm3 / h, the ho...

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Abstract

The invention discloses an iron-based catalyst for direct coal liquefaction and a preparation method thereof. The preparation method comprises: preparing an iron salt solution and an ammonia solution; making the iron salt solution and the ammonia solution enter a static mixer for a precipitation reaction to form a slurry mixture containing iron precipitation; making the slurry mixture containing iron precipitation enter an absorption oxidation reaction At the same time, the pulverized coal enters the absorption oxidation reactor, so that the mist and pulverized coal are mixed and absorbed by the pulverized coal; the pulverized coal that has absorbed the mist is subjected to the first hot air in the absorption oxidation reactor Quickly oxidize to undergo crystal phase transformation to generate iron oxide precursors; make the iron oxide precursors continue to undergo the pre-drying of the first hot air to form pre-dried catalysts; make the pre-dried catalysts enter the ball mill dryer, and undergo grinding and crushing at the same time Re-drying of the second hot air to form the catalyst. The method can obtain a more active coal direct liquefaction catalyst with lower cost, water consumption and energy consumption.

Description

technical field [0001] The invention relates to the field of coal chemical industry, in particular to an iron-based catalyst for direct coal liquefaction and a preparation method thereof. Background technique [0002] Coal direct liquefaction refers to a clean coal technology that converts coal into liquid products with the help of hydrogen-donating solvents and catalysts under high temperature and high pressure conditions. The main products of direct coal liquefaction are high-quality gasoline, jet fuel oil, diesel oil, aromatics and carbon chemical raw materials, and its by-products mainly include fuel gas, liquefied petroleum gas, sulfur and ammonia, etc., and the thermal efficiency of direct coal liquefaction is as high as 70%. Therefore, direct coal liquefaction to produce liquid fuel is an important way for clean and efficient conversion and utilization of coal. [0003] However, the direct coal liquefaction process is a complex physical and chemical process, and ther...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J23/75C10G1/08
CPCB01J23/75B01J23/755C10G1/086
Inventor 谢晶舒歌平王洪学单贤根章序文杨葛灵高山松
Owner CHNA ENERGY INVESTMENT CORP LTD