Denitration and purification method of catalytic cracking regenerated flue gas
A technology for regenerating flue gas and catalytic cracking, applied in chemical instruments and methods, separation methods, molecular sieve catalysts, etc., can solve the problems of unexamined molecular sieve reduction nitrogen oxide purification effect, high reaction temperature, single catalyst, etc., to achieve the preparation method Simple, high oxidation performance, low cost effect
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Embodiment 1
[0033] First, 0.2g of the first catalyst La 0.75 K 0.25 mn 0.95 Cu 0.05 o 3 / CeO 2 (Loading capacity is 50%) as the oxidation catalyst is packed on the upper layer of quartz tube reactor, then the 0.4g second catalyst W / HZSM-5 (loading capacity is calculated as tungsten) loading capacity is 2wt%, the silica-alumina of HZSM-5 Ratio is 25) fills in the lower floor of reactor as reducing catalyst;
[0034] The simulated FCC regeneration flue gas enters the reactor (programmed temperature rise reaction section) from the bottom, first passes through the reduction catalyst bed for nitrogen oxide reduction reaction, and then enters the oxidation catalyst bed for oxidation reaction of CO and unreduced hydrocarbons , the reaction flow chart is as figure 1 Shown: simulated FCC regeneration flue gas, reaction gas space velocity is 40000h -1 , the volume composition of simulated FCC regenerated flue gas (based on the total volume of regenerated flue gas) is: CO, 800ppm, NO, 800ppm,...
Embodiment 2
[0041] First, 0.2g of the first catalyst La 0.75 K 0.25 mn 0.95 Cu 0.05 o 3 / CeO 2 (loading capacity is 50%) as oxidation catalyst, fills in the upper layer of quartz tube reactor, then 0.4g second catalyst W-Cu / HZSM-5 (tungsten oxide loading capacity is 2%, molar ratio W: Cu=10 : 2, the silicon-aluminum ratio of HZSM-5 is 25) fills in the lower floor of reactor as reduction catalyst;
[0042] The simulated FCC regeneration flue gas enters the reactor from below, wherein the reaction process, reaction gas space velocity and gas composition of the simulated FCC regeneration flue gas are the same as those in Example 1.
[0043] For the above combined catalysts, after the temperature-programmed reaction, the highest conversion rate of NO is 56.1%, and the temperature at which hydrocarbons are completely converted is 425°C.
Embodiment 3
[0045] First, 0.2g of the first catalyst La 0.75 K 0.25 mn 0.95 Cu 0.05 o 3 / CeO 2 (loading capacity is 50%) as oxidation catalyst and fills in the upper layer of quartz tube reactor, then 0.4g second catalyst W-Ce / HZSM-5 (tungsten oxide loading capacity is 2%, molar ratio W: Ce=10: 2. The silicon-aluminum ratio of HZSM-5 is 25) filled in the lower layer of the reactor as a reduction catalyst;
[0046] The simulated FCC regeneration flue gas enters the reactor from below, wherein the reaction process, reaction gas space velocity and gas composition of the simulated FCC regeneration flue gas are the same as those in Example 1.
[0047] For the above combined catalysts, after the temperature-programmed reaction, the maximum conversion rate of NO is 78.7%, and the temperature at which hydrocarbons are completely converted is 373°C.
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