A flue gas waste heat recovery system and its recovery method and application
A flue gas waste heat and recovery system technology, applied in the field of flue gas waste heat recovery, can solve problems such as cost increase, achieve the effects of improving efficiency, improving economic benefits, and optimizing heat utilization methods
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Embodiment 1
[0036] This embodiment adopts as figure 1 The system shown in the figure recovers waste heat from the flue gas. The fuel and the air heated by the air preheater 4 from the blower 6 enter the radiant chamber 1 of the heating furnace, and the flue gas leaving the radiant chamber 1 of the heating furnace passes through the flue gas from the convection chamber 2 of the heating furnace. The inlet enters the furnace body 8, and the material is directly added to the material inlet of the steam drum 7. Part of the liquid in the steam drum 7 enters the evaporation section 9 from the downcomer of the steam drum 7 to be heated and starts to produce steam, and a part of the liquid material becomes steam to form a gas-liquid mixture. , the gas-liquid mixture leaves the evaporation section 9 and enters the steam drum 7, where gas-liquid separation is carried out in the steam drum 7, and the liquid falls into the liquid space in the steam drum 7; another part of the liquid in the steam drum 7...
Embodiment 2
[0039] Except that the coal-saving section 11 in the convection chamber 2 of the heating furnace is extracted while one furnace tube in the evaporation section 9 in the convection chamber 2 of the heating furnace is extracted, other processes are uniformly the same as in Example 1.
[0040] It raises the temperature of flue gas at the exit of the convection chamber 2 of the heating furnace to 250-350°C, which in turn can effectively increase the temperature of the air entering the radiation chamber of the heating furnace, and finally achieve the purpose of rationally optimizing the heat energy distribution of the flue gas and reducing the fuel consumption of the heating furnace.
Embodiment 3
[0042] Except that the coal-saving section 11 in the convection chamber 2 of the heating furnace is extracted and three furnace tubes in the evaporation section 9 in the convection chamber 2 of the heating furnace are extracted, other processes are uniformly the same as in Example 1.
[0043] It raises the temperature of flue gas at the exit of the convection chamber 2 of the heating furnace to 250-350°C, which in turn can effectively increase the temperature of the air entering the radiation chamber of the heating furnace, and finally achieve the purpose of rationally optimizing the heat energy distribution of the flue gas and reducing the fuel consumption of the heating furnace.
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