Lift pipe catalytic cracking device
A catalytic cracking device and riser technology, applied in catalytic cracking, cracking, chemical instruments and methods, etc., can solve the problems of easy nozzle blockage, low cracking activity, poor sulfur reduction effect, etc., to improve atomization effect and reduce sulfur content, the effect of improving shear tearing ability
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Embodiment 1
[0108] The catalytic cracking device of the present invention is used to carry out catalytic cracking. Under the single variable situation, the catalytic situation is investigated, wherein the catalyst regeneration temperature is 650 ° C, the reaction temperature in the riser is 430 ° C, the agent-oil ratio is 5, and the hydrogen flow rate of the oxidation-reduction treatment unit is 20 L / h. The variables are specifically:
[0109] Catalyst A is treated with hydrogen in the oxidation-reduction treatment unit at different temperatures for 30 minutes, and the catalytic cracking reaction results are listed in Table 3;
[0110] Catalyst A is treated with hydrogen in the oxidation-reduction treatment unit at a temperature of 500 ° C for different time and the catalytic cracking reaction results are listed in Table 4; Catalysts A, B, and C are treated with hydrogen in the oxidation-reduction treatment unit The reaction results after treatment for 20 minutes at ℃ temperature are list...
Embodiment 2
[0112] Using the catalytic cracking device of the present invention, the reaction results after the catalyst C was treated with hydrogen at a temperature of 550° C. for 20 minutes in the oxidation-reduction treatment unit are listed in Table 6. Other conditions: reaction temperature 500° C., regeneration temperature 690° C., agent The oil ratio is 6, and the hydrogen flow rate is 20L / h.
Embodiment 3
[0114] Using the catalytic cracking unit of the present invention, the reaction results after catalyst C was treated with hydrogen at 550°C for 20 minutes in the oxidation-reduction treatment unit are listed in Table 7. Other conditions: raw oil riser reaction temperature 500°C, regeneration temperature 690°C, agent-to-oil ratio 6; gasoline (light feedstock) riser reaction temperature 450°C, regeneration temperature 690°C, agent-to-oil ratio 5.
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