Fluidized bed device and preparation method for preparing aromatic hydrocarbon from alkyl hydrocarbon
A fluidized bed and aromatics technology, applied in chemical instruments and methods, chemical recovery, organic chemistry, etc., can solve problems such as difficult increase in conversion rate and aromatics yield, low process driving force, and influence of heating tube strength, etc., to achieve Increase independence and operational flexibility, reduce equipment cost, and reduce the effect of heating tube area
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Embodiment 1
[0041] For a two-stage fluidized bed device as shown in Figure 1, the distance between the upper outlet of the outer overflow pipe and the adjacent lower distribution plate is 0.1 times the diameter of the device. The inlet of the lower part of the outer overflow pipe is located in the first layer of catalyst bed. The two catalyst inlets lead into two catalyst beds respectively, and the position of the catalyst inlet in the second catalyst bed is 0.4m higher than the upper outlet of the overflow pipe outside the device. The gas contained in the catalyst entering from the upper outlet of the outer overflow pipe is led to the vicinity of the catalyst recovery system in the device through the pipeline. The cross-sectional area of the set finned heating tube accounts for 20% of the radial cross-sectional area of the device.
[0042] While passing air at 600°C from the gas inlet 1 through the gas distributor 2, the fluidized catalyst is loaded into the device from the catalyst i...
Embodiment 2
[0046] For a two-stage fluidized bed device as shown in Figure 1, the distance between the upper outlet of the outer overflow pipe 5 and the adjacent lower distribution plate is 1 times the diameter of the device. The lower inlet of the outer overflow pipe is located in the first catalyst bed. The two catalyst inlets lead into two catalyst beds respectively, and the position of the catalyst inlet 8 in the second catalyst bed is 1.5m higher than the upper outlet of the outer overflow pipe 5 outside the device. The gas contained in the catalyst entering from the upper outlet of the outer overflow pipe is led to the vicinity of the catalyst recovery system 6 in the device through pipelines. The cross-sectional area of the set finned heating tube accounts for 35% of the radial cross-sectional area of the device.
[0047] While the air at 300°C is introduced from the gas inlet of the device through the gas distributor, the fluidized catalyst is loaded into the device from the ...
Embodiment 3
[0051] For a two-stage fluidized bed device as shown in Figure 1, the distance between the upper outlet of the outer overflow pipe and the adjacent lower distribution plate is twice the diameter of the device. The lower inlet of the outer overflow pipe is located in the first catalyst bed. The two catalyst inlets lead into two catalyst beds respectively, and the position of the catalyst inlet in the second catalyst bed is 1m higher than the upper outlet of the overflow pipe outside the device. The gas contained in the catalyst entering from the upper outlet of the outer overflow pipe is led to the vicinity of the catalyst recovery system in the device through the pipeline. The cross-sectional area of the set finned heating tube accounts for 25% of the radial cross-sectional area of the device.
[0052] While nitrogen gas at 600°C is introduced from the gas inlet through the gas distributor, the fluidized catalyst is loaded into the device from the catalyst inlet. The main...
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