Device and method for enhancing removal of fine particle substances in flue gas desulfurization process of fire coal
A desulfurization process and technology for fine particles, which is applied in the field of devices for improving the removal of fine particles based on the principle of steam phase change, 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 reducing steam consumption
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Embodiment 1
[0017] In the coal-fired spray-drying flue gas desulfurization process of the present invention, the method for improving the removal of fine particles by applying steam phase transition is as follows: figure 1 As shown: the dust-laden flue gas generated by the coal-fired boiler 1 first enters the desulfurization reaction tower 2, and is sprayed into the lime slurry. After the atomized lime slurry contacts the high-temperature flue gas, the water in the slurry begins to evaporate, and the flue gas is cooled and humidified. The smoke temperature drops from 140-160°C to 50-65°C, the relative humidity increases from 5-8% to over 50-60%, and the near-adiabatic saturation temperature is 5-15°C. After desulfurization and purification of the flue gas, the coarse particles are removed by the electrostatic precipitator 3, and then enters the steam phase change chamber 4, and an appropriate amount of atmospheric saturated steam is injected through the steam nozzle 5, so that the flue gas...
Embodiment 2
[0020]The method for improving the removal of fine particles by applying steam phase change in the flue gas desulfurization process of humidifying and activating the calcium injection tail in the coal-fired furnace of the present invention is as follows: figure 2 As shown, what is different from Example 1 is that limestone powder is sprayed into the furnace 1 of the coal-fired boiler, and 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 gas temperature decreased and the humidity increased, the temperature of the flue gas at the outlet of the activator was 55-60°C, and the relative humidity was increased from 5-8% to more than 50-60%; the rest were the same as in Example 1.
Embodiment 3
[0022] like 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 the steam is injected from the upper part of the phase change chamber through the steam nozzle 5. , in countercurrent contact with the flue gas, and the fine particles captured by the mist eliminator 6 are discharged through the flushing waste liquid outlet located at the bottom of the vapor phase change chamber.
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