Nanometer iron-series catalyst and preparation method thereof
A nano-iron and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of reducing the specific surface area and activity of iron-based catalysts, secondary agglomeration , particle growth and other problems, to achieve the effects of easy industrial production, good stability, and simple preparation process
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[0022] In the preparation method of the nano-iron catalyst of the present invention, the liquid medium used is at least one of oil, fat, naphthalene, anthracene, phenanthrene, phenol, benzene, alcohols or water.
[0023] In the preparation method of the nanometer iron-based catalyst of the present invention, the heating temperature is 103-400°C.
[0024] In the preparation method of the nano-iron catalyst of the present invention, the volume ratio of the iron pentacarbonyl vapor to the liquid medium is 1:10-10:1.
[0025] In the preparation method of the nanometer iron-based catalyst of the present invention, the mixing volume ratio of the iron pentacarbonyl liquid and the liquid medium is 1:20-4:5.
[0026] In the preparation method of the nanometer iron-based catalyst of the present invention, nitrogen or other inert gases are used to replace the air in the kettle.
[0027] In the preparation method of the nanometer iron-based catalyst of the present invention, the reaction...
Embodiment 1
[0029] Fill the heavy oil into a 2L high-pressure reaction kettle with a stirring device, blow nitrogen to replace the residual air in the kettle and the pipeline, heat it to 103°C, open the inlet valve connected to the steam of iron pentacarbonyl, and inject 200ml of iron pentacarbonyl Steam, start the stirring device, keep warm for 2 hours; cool to room temperature, open the exhaust valve to discharge gas products, condense and split to obtain nano-iron catalyst.
[0030] The above-mentioned nano-iron-based catalyst was applied to the direct coal liquefaction experiment: Huolinhe lignite was used, hydrogenated residual oil was used as a solvent, the reaction temperature was 350°C, the initial hydrogen pressure was 6MPa, the catalyst addition amount was 5%, and the mass ratio of Fe:S was 2 : 3 add sulfur powder, the reaction time is 1.5 hours, the coal conversion rate is 85.5%, and the oil recovery rate is 57.2%.
Embodiment 2
[0032] Fill tetrahydronaphthalene into a 2L high-pressure reaction kettle with a stirring device, pass nitrogen to replace the residual air in the kettle and pipeline, heat to 250°C, open the inlet valve connected to iron pentacarbonyl steam, and feed 10L pentacarbonyl Iron steam, start the stirring device, keep warm for 1h; cool to room temperature, open the exhaust valve to discharge gas products, condense and shunt to obtain nanometer iron-based catalysts.
[0033] The above-mentioned nano-iron-based catalyst was applied to the direct coal liquefaction experiment: Huolinhe lignite was used, hydrogenated residual oil was used as a solvent, the reaction temperature was 350°C, the initial hydrogen pressure was 6MPa, the catalyst addition amount was 5%, and the mass ratio of Fe:S was 2 : 3 add sulfur powder, the reaction time is 1.5 hours, the coal conversion rate is 88.9%, and the oil recovery rate is 59.2%.
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