A method for catalytic reaction rectification separation and cracking of carbon five and its catalytic reaction rectification tower
A catalytic reaction, rectification separation technology, applied in distillation purification/separation, fractionation, addition of unsaturated hydrocarbons to hydrocarbons, etc., can solve the problems of low conversion rate and short residence time, and achieve higher yield and easier reaction , the effect of increasing the reaction speed
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Embodiment 1
[0044] The method and device thereof of present embodiment catalytic reaction rectification separation cracking carbon five are as above-mentioned, and concrete operation parameter is: catalytic reaction rectification tower, tower diameter 2m, rectifying section 2m packing (equivalent to 30 theoretical trays ), 2m packing (equivalent to 30 theoretical trays) in the stripping section, 30 layers of catalytic reaction rectification trays in the catalytic reaction section, the number of hoods on the trays in the catalytic reaction section is 24, and the total number of catalyst bags in each layer The area is 1.25m 2 , with a volume of 0.15m 3 , The quality of each layer of catalyst is 300kg. The operating conditions are: tower top pressure 0.25MPa, tower top temperature 55.6°C, tower bottom temperature 87°C, reflux ratio 8, space velocity 4h -1 . After running normally, the measured test results are shown in Table 2.
[0045] Table 2
[0046] component name
[0047]...
Embodiment 2
[0054] The method and device thereof of present embodiment catalytic reaction rectification separation cracking carbon five are as above-mentioned, and concrete operation parameter is: catalytic reaction rectification tower, tower diameter 2m, rectifying section 2m packing (equivalent to 30 theoretical trays ), 2m packing (equivalent to 30 theoretical trays) in the stripping section, 30 layers of catalytic reaction rectification trays in the catalytic reaction section, the number of hoods on the trays in the catalytic reaction section is 24, and the total number of catalyst bags in each layer The area is 1.25m 2 , with a volume of 0.15m 3 , The quality of each layer of catalyst is 300kg. The operating conditions are: tower top pressure 0.2MPa, tower top temperature 47.8°C, tower bottom temperature 82°C, reflux ratio 6, space velocity 5h -1 . After running normally, the measured test results are shown in Table 4.
[0055] Table 4
[0056] Composition
[0057] ...
Embodiment 3
[0060] The method and device thereof of present embodiment catalytic reaction rectification separation cracking carbon five are as above-mentioned, and concrete operation parameter is: catalytic reaction rectification tower, tower diameter 2m, rectifying section 2m packing (equivalent to 30 theoretical trays ), 2m packing (equivalent to 30 theoretical trays) in the stripping section, 30 layers of catalytic reaction rectification trays in the catalytic reaction section, the number of hoods on the trays in the catalytic reaction section is 24, and the total number of catalyst bags in each layer The area is 1.25m 2 , with a volume of 0.15m 3 , The quality of each layer of catalyst is 250kg. The operating conditions are: tower top pressure 0.3MPa, tower top temperature 62.5°C, tower bottom temperature 93°C, reflux ratio 4, space velocity 6h -1 . After running normally, the measured test results are shown in Table 5.
[0061] table 5
[0062] Composition
[0063] Res...
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