Method for eliminating oxynitride from air flow and the special equipment thereof
A technology of nitrogen oxides and gas flow, applied in chemical instruments and methods, separation methods, and separation of dispersed particles, etc., can solve the problems of high requirements for catalyst operating conditions, great impact on catalyst life, and unsuitability for low-temperature emission sources, etc., to achieve The effect of low operating cost, low operation and use cost, and low cost of medicine
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Embodiment 1
[0026] Example 1: Experimental device The system flow is shown in Figure 1, and the electrocatalytic oxidation reactor is shown in Figure 2. The structural size of the reactor is 400mm×400mm×1200mm, and it is composed of 6 sets of mesh electrode units superimposed, and the distance between the plates is 45mm. Mesh anode material is RuO 2 / Ti, the mesh cathode material is stainless steel. The size of the electrode mesh is 380mm×380mm, the thickness is 3mm, and the electrode mesh is 5mm×5mm. The absorption tower is a packed tower with a tower diameter of Φ600mm and a packing layer height of 3000mm. The simulated exhaust gas enters through the air inlet at the bottom of the tower, passes through the absorption reaction zone, and is discharged from the upper part.
[0027] The experimental conditions are: power supply parameters: DC voltage 15V, current 100A,
[0028] Exhaust gas composition: nitrogen oxides (NOx) / air
[0029] Gas flow: 800m 3 / h, gas temperature: 45°C
[0...
Embodiment 2
[0033] Embodiment 2: other conditions are the same as embodiment 1, the power supply parameter becomes direct current 20V, electric current 100A, sodium chloride solution, concentration 10%
[0034] Experimental results: as shown in Table 2
[0035] Import concentration
Embodiment 3
[0036] Embodiment 3: Other conditions are the same as Embodiment 1, the power supply parameters are pulse peak voltage 30V, pulse frequency 50Hz, pulse peak current 100A
[0037] Experimental results: as shown in Table 3
[0038] Import concentration
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