Movable type catalyst charging device and charging method thereof
A technology of feeding device and catalyst, applied in feeding device, chemical instrument and method, chemical/physical process, etc., can solve the problems of poor applicability of flexible supplements, complicated operation links, and many supporting facilities, etc., and achieve easy disassembly. and maintenance, shorten the test cycle, reduce the effect of labor
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Embodiment 1
[0058] Dosing to the regenerator of a pilot plant, the dosing port elevation is 10m, the state of the regenerator: normal pressure, normal temperature, 20 kg of dosing is to be added, and the median diameter of the catalyst is 76-78μm. Dosing tanks are located on the ground. The main operation process: ① Weigh 20 kg of catalyst to be added on the weighing scale; ② Close the control ball valve 3, slightly open the main flow air outlet 12, the pressure gauge back blow outlet 14, and blow back air 0.1m each 3 / h, the opening of the valve of the venting pipeline 8 is 1 / 3, and the agent is added to the fluidized storage tank 2 through the funnel; ③Close the valve of the venting pipeline 8, and open the mainstreaming tuyere 12 to 0.8m 3 / h, loose air outlet 13 and pressure gauge reverse air outlet 14 each 0.1m 3 / h, pressurize the fluidized storage tank 2 until 0.10-0.15MPa; ④ open the control ball valve 3, and keep the loose air outlet 13 at 0.1m 3 / h, the lifting air outlet 15 i...
Embodiment 2
[0061] Dosing to the regenerator of a pilot plant, the dosing port elevation is 12m, the state of the regenerator: normal pressure, normal temperature, 120 kg of dosing is to be added, and the median diameter of the catalyst is 76-78μm. Dosing tanks are located on the ground. The main operation process: ① Weigh 40 kg of catalyst to be added on the weighing scale; ② Close the control ball valve 3, slightly open the main air (open the mainstream air outlet 12 valve), and the pressure gauge reverse blowing (open the reverse blowing outlet 14) each 0.1m 3 / h, the valve opening of the vent pipeline 8 is 1 / 3, and the agent is added to the fluidized storage tank 2 through the funnel; ③Close the valve 8 of the vent pipeline, and open the main air to 1.0m 3 / h, loose wind (realized by opening the loose air port 13) and pressure gauge back blow 0.1m each 3 / h, pressurize the fluidized storage tank 2 until 0.10-0.15MPa; ④ open the control ball valve 3, and keep the loose air at 0.1m 3 ...
Embodiment 3
[0064] After 50 hours of continuous operation of a pilot plant, the particle size of the catalyst in the reactor changed, and the conversion rate of raw materials decreased. In order to maintain the reaction index, 10 kg of regenerator was added to the pilot plant, and the median diameter of the catalyst was 36-38 μm. The elevation of the dosing port of the regenerator is 10m, the status of the regenerator: pressure 0.10MPa, 620°C, 10kg of supplement is required. Dosing tanks are located on the ground. The main operation process: ① Weigh 10 kg of catalyst to be added on the weighing scale; ② Close the control ball valve 3, slightly open the main air 12, and the pressure gauge reverse air 14, each 0.1m 3 / h, vent pipeline (valve) 8 opening degree 1 / 3, add agent to fluidized storage tank 2 through funnel; ③Close vent pipeline valve 8, open main air 12 to 0.5m 3 / h, loose 13 and pressure gauge blowback each 0.1m 3 / h, pressurize the fluidized storage tank 2 until 0.20MPa; ④ ope...
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