Method for removing nitric oxides by absorption and plasma selective catalytic reduction
A plasma and nitrogen oxide technology, which is applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., can solve the problem of nitrogen oxide removal rate and reaction process energy efficiency improvement, high reaction conditions, and limited scope of application, etc. problems, to achieve high-efficiency and low-energy consumption removal, low requirements for equipment and reaction conditions, and thorough treatment
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Embodiment 1
[0021] (1) Take 1.0 g of the adsorption catalyst and place it in the plasma discharge zone, activate it in an air stream at 500°C for 60 minutes, and cool it to room temperature;
[0022] (2) Pass the mixed gas (total flow rate 80mL / min) containing nitrogen oxides (500 ppm) and oxygen (12%) through the adsorption catalyst bed filled in the plasma reactor to adsorb to nitrogen oxide penetration adsorption Catalyst, the adsorption temperature is 35℃;
[0023] (3) Switch the gas passing through the adsorption catalyst bed to O 2 And CH 4 Mixed gas, O 2 And CH 4 The volume ratio is O 2 / CH 4 = 4, the airspeed is 6000 h -1 , Turn on the plasma power supply to perform the plasma selective catalytic reduction reaction, the temperature in the plasma reactor is 80 ℃, the plasma discharge mode is dielectric barrier discharge, and the reaction stops after 30 minutes. On various adsorption catalysts, nitrogen oxides are converted to N 2 The conversion rate is shown in Table 1.
[0024] Table ...
Embodiment 2
[0027] (1) Take 1.0 g of the adsorption catalyst and place it in the plasma discharge zone, activate it in an air stream at 500°C for 60 min, and cool it to room temperature;
[0028] (2) Pass the mixed gas (total flow rate 80mL / min) containing nitrogen oxides (500 ppm) and oxygen (12%) through the adsorption catalyst bed filled in the plasma reactor to adsorb to nitrogen oxides at 50°C Penetrate the adsorption catalyst;
[0029] (3) Switch the gas passing through the adsorption catalyst bed to contain O 2 And CH 4 Mixed gas, O 2 And CH 4 The volume ratio is O 2 / CH 4 = 4, the airspeed is 6000 h -1 , Turn on the plasma power supply to carry out the plasma selective catalytic reduction reaction, the temperature in the plasma reactor is controlled to 0, 50, 80, 150 ℃, the plasma discharge mode is dielectric barrier discharge, and the reaction stops after 30 minutes. The reaction results are shown in Tables 2 and 3.
[0030] Table 2 Reaction results when Cu-ZSM-5 is the adsorption ca...
Embodiment 3
[0036] (1) Take 1.0 g of the adsorption catalyst and place it in the plasma discharge zone, activate it in an air stream at 500°C for 60 min, and cool it to room temperature;
[0037] (2) Pass the mixed gas containing nitrogen oxide (500 ppm) and oxygen (12%) (total flow rate 80mL / min) through the adsorption catalyst bed filled in the plasma reactor, and adsorb to nitrogen oxide at 35℃ Penetrate the adsorption catalyst;
[0038] (3) Switch the gas passing through the adsorption catalyst bed to contain O 2 And C 3 H 6 Mixed gas, O 2 And C 3 H 6 The volume ratio is O 2 / C 3 H 6 = 1.4, the airspeed is 6000 h -1 , Turn on the plasma power supply to perform the plasma selective catalytic reduction reaction, the temperature of the plasma reactor is controlled to 80°C, and the plasma discharge mode is any of atmospheric glow discharge, dielectric barrier discharge, corona discharge, sliding arc discharge, etc. The reaction was stopped after 30 minutes. Under various discharge methods, n...
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