Method for removing nitrogen oxide in airflow
A nitrogen oxide, gas flow technology, applied in chemical instruments and methods, separation methods, gas treatment and other directions, can solve the problems of expensive pharmaceuticals, low absorption efficiency, high operation and use costs, and achieve safe use, large processing capacity, and operating costs. low effect
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Embodiment 1
[0017] Embodiment 1: a kind of circulating fluidized bed gas-solid reaction tower device of the method for removing nitrogen oxides in the gas stream is as figure 1 shown. The circulating fluidized bed gas-solid reaction tower has a tower diameter of Φ60 mm, a tower height of 2500 mm, and a tower body made of 316L stainless steel. The concentration of nitrogen oxides (about 90% nitric oxide) in the gas stream is 500 ppm, oxygen is 8% by volume, moisture content is 10% by volume, and the balance is nitrogen. Polyferric chloride is used as commercially available industrial-grade powder particles, with an average particle size of about 0.1mm. Polyferric chloride is heated to 70°C, 90°C and 120°C reaction temperature respectively, and then introduced into the gas-solid reaction tower. The gas temperatures of the air stream are 20°C, 40°C, 55°C and 70°C respectively, and the gas-solid contact time in the reaction tower is about 4-6s. The mass ratio of nitrogen oxides to polyferri...
Embodiment 2
[0020] Example 2: Using polyferric chloride as the reactant, commercially available industrial-grade powdered particles with an average particle size of about 0.1 mm, polyaluminum ferric chloride was heated to 80 ° C, 120 ° C and 150 ° C reaction temperature and then introduced For the gas-solid reaction tower, the gas temperatures of the gas entering the tower are 90°C and 120°C respectively, and other conditions are the same as in Example 1. The experimental results are shown in Table 2.
[0021] Table 2
[0022]
Embodiment 3
[0023] Example 3: Polyferric chloride is introduced into the gas-solid reaction tower at normal temperature, the gas temperatures in the tower are respectively 80°C, 95°C and 120°C, and the mass ratio of nitrogen oxides to polyferric chloride is about 1:15. Other conditions are with embodiment 1. The experimental results are shown in Table 3.
[0024] table 3
[0025]
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