Method and device for desulfurization of high-temperature flue gas through forced grinding and on-line decomposition CaCO3
A high-temperature flue gas and flue gas technology, applied in the field of flue gas desulfurization, can solve the problems of not being widely used in commercial applications, easy formation of wet ash and pulp lumps, and high capital investment costs, so as to improve the utilization rate of calcium base, increase the The effect of large residence time, convenient operation and maintenance
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Embodiment 1
[0024] The simulated flue gas temperature is 700°C, SO 2 Concentration 1000mg / Nm 3 , flue gas volume 400Nm 3 / h, the simulated flue gas enters the desulfurization tower through the flue gas inlet 8, CaCO 3 The height of decomposition zone 1 is 1.0m, the height of desulfurization section 2 is 0.5m, the particle size of desulfurizer is 0.1mm, the flow rate of flue gas is 3.8m / s, and the flue gas after desulfurization treatment flows out from flue gas outlet 9. The calculated desulfurization efficiency is 90.1%.
Embodiment 2
[0026] The simulated flue gas temperature is 700°C, SO 2 Concentration 1000mg / Nm 3 , flue gas volume 400Nm 3 / h, the simulated flue gas enters the desulfurization tower through the flue gas inlet 8, CaCO 3 The height of decomposition zone 1 is 1.2m, the height of desulfurization section 2 is 1.0m, the particle size of desulfurizer is 0.05mm, the flow rate of flue gas is 3.8m / s, and the flue gas after desulfurization treatment flows out from flue gas outlet 9. The calculated desulfurization efficiency is 92.3%.
Embodiment 3
[0028] Simulated flue gas temperature 900°C, SO 2 Concentration 1000mg / Nm 3 , flue gas volume 400Nm 3 / h, the simulated flue gas enters the desulfurization tower through the flue gas inlet 8, CaCO 3 The height of decomposition zone 1 is 1.0m, the height of desulfurization section 2 is 0.5m, the particle size of desulfurizer is 0.1mm, the flow rate of flue gas is 3.8m / s, and the flue gas after desulfurization treatment flows out from flue gas outlet 9. The calculated desulfurization efficiency is 92.7%.
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