A resource-based treatment method for plasma purification of air containing hydrogen sulfide and ammonia pollution
A plasma and air pollution technology, applied in separation methods, gas treatment, chemical instruments and methods, etc., can solve the problems of high operating costs, secondary pollution, and difficult purification, so as to reduce operating costs and eliminate secondary pollution. Effect
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Embodiment 1
[0029] Such as figure 1 with figure 2 Shown is an example of the process of oxidizing hydrogen sulfide based on dielectric barrier discharge and reacting with ammonia to produce ammonium sulfate.
[0030] (1) The polluted air containing hydrogen sulfide and ammonia enters the membrane separator for separation.
[0031] (2) The polluted air containing hydrogen sulfide enters the corona discharge plasma device, the plasma energy density is 0.2J / L, the reaction time is 1s, and the reaction temperature is -10°C, so that the hydrogen sulfide in the range of 100ppm becomes sulfur-containing oxides .
[0032] (3) Introduce the produced sulfur-containing oxides and the ammonia in the ammonia-contaminated air and the moisture in the ammonia-contaminated air after the treatment in step 1) into the catalytic oxidation device. The reaction temperature is -20°C and the reaction time is 2s. , The pressure is 0.3bar, and the ammonia gas in the catalytic oxidation device reacts with sulfur-contain...
Embodiment 2
[0036] (1) Polluted air containing hydrogen sulfide, ammonia, and ozone enters the condenser separator for separation.
[0037] (2) The polluted air containing hydrogen sulfide and ozone enters the dielectric barrier discharge device, and 5g spherical titanium oxide is added. The plasma energy density is 5J / L, the reaction time is 5s, and the reaction temperature is 55°C, so that the hydrogen sulfide in the range of 200ppm becomes Sulfur oxides.
[0038] (3) Introduce the produced sulfur-containing oxides and the ammonia in the ammonia-contaminated air and the moisture in the ammonia-contaminated air after the treatment in step 1) into the thermodynamic combustion device. The reaction temperature is 30°C, and the reaction time is 10s. At a pressure of 1 bar, the ammonia gas in the thermodynamic combustion device reacts with sulfur-containing oxides to produce ammonium sulfate aerosol, and the polluted air is purified into purified air.
[0039] (4) The purified air and ammonium sulf...
Embodiment 3
[0041] (1) Polluted air containing hydrogen sulfide, hydrogen peroxide and ammonia enters the pressure swing separator for separation.
[0042] (2) The polluted air containing hydrogen sulfide and hydrogen peroxide enters the arc discharge device, and 8g spherical zinc oxide is added, the plasma energy density is 10J / L, the reaction time is 10s, and the reaction temperature is 100℃, so that the hydrogen sulfide in the range of 500ppm becomes Sulfur oxides.
[0043] (3) Introduce the generated sulfur-containing oxides and the ammonia in the ammonia-contaminated air and the moisture in the ammonia-contaminated air after the treatment in step 1) into the plasma oxidation device. The reaction temperature is 80°C and the reaction time is 20s. , The pressure is 2bar, the ammonia gas in the plasma oxidation device reacts with sulfur-containing oxides to produce ammonium sulfate aerosol, and the polluted air is purified into purified air.
[0044] (4) The purified air and ammonium sulfate a...
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