Device and method for enhancing removal of fine particle substances in flue gas desulfurization process of fire coal
A technology of fine particles and desulfurization process, which is applied in the direction of combined devices, separation methods, chemical instruments and methods, etc., can solve the problems of fine particles discharged into the atmosphere and low capture efficiency, and achieve enhanced phase change effect, simple process, The effect of increasing relative humidity
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[0016] Example 1:
[0017] The method of applying steam phase change to improve the removal of fine particles in the coal-fired spray drying flue gas desulfurization process of the present invention is as follows figure 1 Shown: the dust-containing flue gas produced by coal-fired boiler 1 first enters the desulfurization reaction tower 2, and is sprayed into lime slurry. After the atomized lime slurry contacts the high-temperature flue gas, the moisture in the slurry begins to evaporate, and the flue gas is cooled and humidified. The smoke temperature drops from 140-160℃ to 50-65℃, the relative humidity increases from 5-8% to more than 50-60%, and the near-adiabatic saturation temperature is 5-15℃. After the desulfurization and purification flue gas is removed by the electrostatic precipitator 3 to remove coarse particles, it enters the steam phase change chamber 4, and injects an appropriate amount of normal pressure saturated steam through the steam nozzle 5 to make the flue gas...
Example Embodiment
[0019] Example 2:
[0020] The method of applying steam phase change to improve the removal of fine particles in the method of applying steam phase change to improve the removal of fine particles in the calcium injection tail humidification activation flue gas desulfurization process of the present invention figure 2 As shown, the difference from Example 1 is that limestone powder is sprayed into the furnace 1 of the coal-fired boiler, the flue gas enters the humidification activator 2 after the first step of desulfurization, and sprayed into the atomized water, the atomized water evaporates rapidly, and the smoke The temperature of the air decreases and the humidity increases. The temperature of the flue gas at the outlet of the activator is 55-60°C, and the relative humidity is increased from 5-8% to more than 50-60%; the rest is the same as in Example 1.
Example Embodiment
[0021] Example 3:
[0022] Such as image 3 As shown, the difference from Embodiments 1 and 2 is that the steam phase change chamber is arranged vertically. The flue gas from the electrostatic precipitator 3 enters from the lower part of the steam phase change chamber 4, and steam is injected from the upper part of the phase change chamber through the steam nozzle 5. , In countercurrent contact with the flue gas, the fine particles captured by the demister 6 are discharged through the flushing waste liquid outlet provided at the bottom of the vapor phase change chamber.
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