Low-temperature flue gas dry desulfurization process for preheating desulfurizer
A low-temperature flue gas and dry desulfurization technology, applied in the field of flue gas desulfurization, can solve the problems of increased energy consumption, low efficiency, and low activity
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Embodiment 1
[0055] refer to figure 2 As shown, the low-temperature flue gas dry desulfurization method of preheating the desulfurizer in this embodiment includes the following steps: the flue gas from the coke oven charging coal, coking and dedusting enters the low-temperature flue gas main pipeline 1 through the gas intake point, and flows through the low-temperature flue gas auxiliary pipe 1. The pipeline 2 enters the heating device 4. In this embodiment, the heating device 4 is a gas-gas heat exchange device 41 and an electric heating device 43 for co-heating. , the gas-gas heat exchange device 41 is a steam heat exchanger, through the steam heat exchanger, the temperature of the flue gas from coke charging and dust removal in the coke oven is heated to 130°C, and then enters the electric heating device 43, which is an electric heater , the electric heater heats the temperature of the flue gas from coke oven charging and dedusting to 250°C; then the hot flue gas at 250°C enters the mi...
Embodiment 2
[0057] refer to image 3 As shown, the low-temperature flue gas dry desulfurization method of preheating the desulfurizer in this embodiment includes the following steps: the outdoor low-temperature air enters the gas-gas heat exchange device 41 through the left end of the high-temperature flue gas pipeline 3, and the heating device in this embodiment 4 is air-gas heat exchange device 41 and electric heating device 43 cooperative heating, the outdoor low-temperature air enters the air-gas heat exchange device 41 first, and the gas-gas heat exchange device 41 is a steam heat exchanger, which heats the outdoor air through the steam heat exchanger. The air temperature reaches 130°C, and then enters the electric heating device 43, the electric heating device 43 is an electric heater, and the electric heater heats up the hot air to 250°C; after that, the 250°C hot air enters the middle section of the high-temperature flue gas pipeline 3, which is called 600-800 mesh NaHCO injected ...
Embodiment 3
[0059] refer to Figure 4 As shown, the low-temperature flue gas dry desulfurization method of preheating the desulfurizer in this embodiment includes the following steps. The flue gas auxiliary pipe 2 enters the heating device 4. In this embodiment, the heating device 4 is a hot air heating device 44, and the hot air heating device 44 is a hot blast stove. The combustion medium of the hot blast stove is coke oven gas / blast furnace gas / natural gas, etc.; then the hot flue gas at 250°C enters the middle section of the high-temperature flue gas pipeline 3, and is mixed with the 600-800 mesh NaHCO injected by the weighing feeder 5 3 Fine powder for mixing, pre-decomposing NaHCO 3Fine powder, before the desulfurizer enters the low-temperature flue gas main pipeline 1 and mixes with the coke oven coal charging and dedusting flue gas to activate the activity of the desulfurizer; The main gas pipeline 1 is evenly mixed with the flue gas from coke oven charging and dedusting, and th...
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