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
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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
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