High-efficient iron-series catalyst and its preparation method
A catalyst and catalyst carrier technology, applied in the field of iron-based catalysts and their preparation, can solve the problems of reducing the specific surface area and activity of iron-based catalysts, particle growth, secondary agglomeration, etc., and achieve easy industrial production, simple preparation process, good stability effect
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preparation example Construction
[0020] The preparation method of efficient iron-based catalyst of the present invention consists of the following steps:
[0021] ① Add a solid catalyst carrier to the autoclave, vacuumize or replace the air in the autoclave with high-purity nitrogen or inert gas, and add iron pentacarbonyl liquid;
[0022] ②Start the heating device, heat it to the temperature and keep it warm, so that the iron pentacarbonyl evaporates into steam in the reactor and fully expands, and penetrates into the micropores of the catalyst carrier;
[0023] ③ Continue to raise the temperature or pass high-temperature and high-pressure high-purity nitrogen or other inert gases into the reactor to decompose the iron pentacarbonyl adsorbed in the micropores of the carrier in situ to obtain nano-sized iron particles;
[0024] ④ Cooling, discharge the gas to the tail gas treatment system, put the finished nano-iron-based catalyst into a package filled with high-purity nitrogen or other inert gas, and keep it...
Embodiment 1
[0029] Add zeolite to a 2L high-pressure reaction kettle, blow nitrogen to replace the residual air in the kettle and the pipeline, add 200ml of pentacarbonyl iron liquid, heat to 60°C for 2h, continue heating to 200°C, hold for 1h, cool down, and open the exhaust valve The gas in the kettle is discharged to obtain the nano-iron-based catalyst, which is taken out and put into a packaging bag filled with high-purity nitrogen for airtight storage.
[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 pressure of hydrogen was 6MPa, the amount of catalyst added was 3%, 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 84.3%, and the oil recovery rate is 56.2%.
Embodiment 2
[0032] The same preparation method as in Example 1 was used to produce nanometer iron-based catalysts, wherein the solid catalyst was activated carbon, 800ml of iron pentacarbonyl liquid, the heating temperature was 103°C, the temperature was kept for 1.2h, and the temperature was continued to 250°C for half an hour. The coal type was changed to Shenhua Dongsheng lignite for coal liquefaction experiment, the coal conversion rate was 83.2%, and the oil recovery rate was 58.7%.
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