A Method for Reducing Nox in Catalytic Cracking Incompletely Regenerated Flue Gas
A technology for regenerating flue gas and catalytic cracking, applied in combustion methods, incinerators, combustion types, etc., can solve problems such as system complexity, reducing agent escape, secondary pollution, etc., and achieve high removal efficiency
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Embodiment 1
[0056] see figure 1 , a schematic diagram of a system for reducing the NOx content of incompletely regenerated flue gas from catalytic cracking provided in this example. Including regenerator 1, cyclone separator 2, flue gas turbine 3, waste heat boiler 4 and chimney 5, wherein the outlet at the top of regenerator 1 is connected to the inlet at the top of cyclone separator 2, and the outlet at the top of cyclone separator 2 is connected to the main line 6 connection, the end of the main line 6 is connected with the first pipeline 7 and the second pipeline 8 respectively, the confluence of the first pipeline 7 and the second pipeline 8 is connected with the vertical main line 9, and the end of the vertical main line 9 is connected with the horizontal main line The end of the horizontal main line 10 is connected to the inlet of the flue gas turbine 3 , the outlet of the flue gas turbine 3 is connected to the inlet of the waste heat boiler 4 , and the outlet of the waste heat boi...
Embodiment 2
[0058] see also figure 1 and figure 2 , this embodiment provides a method for reducing the NOx content of incompletely regenerated flue gas from catalytic cracking, including:
[0059] 1) Regenerator 1 produces incompletely regenerated flue gas at a temperature of 600°C. The oxygen content in the incompletely regenerated flue gas is 0.3%, the CO content is 5%, and the H 2 O content is 12%, NH 3 The content is 500ppm, and the HCN content is 50ppm.
[0060] 2) The incompletely regenerated flue gas enters the cyclone separator 2 to remove the catalyst fine powder particles in the incompletely regenerated flue gas, and the incompletely regenerated flue gas exiting the cyclone separator 2 enters the main line 6, and the incompletely regenerated smoke in the main line 6 The gas is divided into the first pipeline 7 and the second pipeline 8, 70% of the incompletely regenerated flue gas enters the first pipeline 7, and 30% of the incompletely regenerated flue gas enters the second...
Embodiment 3-6
[0072] The experimental process is similar to that of Example 2, except that the injecting methods of oxygen-enriched gas, fuel-enriched gas and high-temperature air are changed while the composition of flue gas remains unchanged.
[0073] Experimental parameters in table 1 embodiment 2-6
[0074]
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