Method of removing PM2.5 and gaseous pollutant using steam phase transition and device thereof
A technology for PM2.5 and pollutants, applied in chemical instruments and methods, separation methods, and the use of liquid separation agents, etc., can solve the problems of low dust concentration, low capture rate, and small particle size of smoke and dust, which have not attracted enough attention
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Embodiment 1
[0019] The flue gas is produced by a fully automatic oil-fired boiler with a flue gas volume of 65Nm 3 / h, the water vapor content in the flue gas is 12%, the exhaust gas temperature is 282°C, the peak particle size of the dust concentration is 0.07 μm, most of which are between 0.03 and 0.5 μm, and the SO in the flue gas 2 The concentration is 624mg / Nm 3 ;The wet washing tower adopts a spray tower with a tower diameter of 150mm and a tower height of 1500mm. A wire mesh demister is installed on the top of the spray tower, and the washing and absorbing liquid is Ca(OH) 2 suspension. The dust-containing flue gas produced by the oil-fired boiler directly enters the humidity control room, and sprays fine water mist with a temperature of 70°C and a particle size of 20-30 μm from the atomizing nozzle. 3 The flue gas is 0.01kg. After adjustment, the water vapor content of the outlet flue gas increases to 24%, and the temperature is 235°C; then it enters the tube-and-tube condensati...
Embodiment 2
[0021] Except following change, all the other are the same as embodiment 1.
[0022] The washing and absorbing tower adopts a swirling plate tower, with 3 built-in swirling plates, a swirling plate demister is installed on the top, and the washing and absorbing liquid is Na 2 CO 3 Solution, liquid-gas ratio 3.5L / Nm 3 ;Tested, PM 2.5 The mass concentration removal efficiency is 86%, the number concentration removal efficiency is 72%, and the flue gas desulfurization efficiency is 89%.
Embodiment 3
[0024] The flue gas is produced by waste incineration, and the flue gas volume is 70Nm 3 / h, the water vapor content in the flue gas is 21%, the temperature is 243°C, the SO in the flue gas 2 , HCl, HF concentrations were 729mg / Nm 3 、876mg / Nm 3 、21mg / Nm 3 , the peak particle size of the dust concentration at the outlet of the dust collector is 0.7 μm, and the number concentration is 10 6 piece / cm 3 ; The washing and absorbing tower is a swirling plate tower with a tower diameter of 150mm and a tower height of 1500mm, with 3 built-in swirling plates, a swirling plate demister installed on the top, and the washing and absorbing liquid is Na 2 CO 3 solution. After the waste incineration flue gas is removed from the coarse dust by the cyclone dust collector, it enters the humidity control room, and is sprayed into the fine water mist with a temperature of 65 ℃ and a particle size of 20-30 μm from the atomizing nozzle. 3 The flue gas is 0.008kg. After adjustment, the water v...
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