An adjustable process for producing SO3 gas by treating high-concentration SO2 flue gas with an inert catalyst
A high-concentration, adjustable technology, applied in the direction of inorganic chemistry, non-metallic elements, sulfur compounds, etc., can solve the problems of large gas volume fluctuations, high investment, and ineffective use of energy, and achieve improved waste heat utilization, high production intensity, and The effect of investment savings
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Embodiment 1
[0032] Environmental protection desulfurization and recovery of SO in a power plant 2 The gas is used to prepare sulfuric acid, and the gas composition of the flue gas after drying is: SO 2 —30.69%, O 2 —18.47%, N 2 —49.36%, CO 2 —1.48%, the total gas volume is about 90000Nm 3 / hr. Flue gas through SO 2 After the blower 1 is pressurized, it is heated to 390℃ by the heat exchanger 2 and then enters the first inert catalyst conversion layer 31, the conversion rate is about 35%, the outlet temperature is 660℃ and contains SO 2 The concentration is 21.43%; after the heat exchange by the first waste heat utilization device 41 (produces medium pressure 2.5MPa saturated steam 17.7t / hr), the temperature is reduced to 390°C and then enters the second inert catalyst conversion layer 32, the total conversion rate of the reaction is about 60%, Outlet temperature is 580℃ and contains SO 2 The concentration is 13.75%; after the heat exchange by the second waste heat utilization device 42 (prod...
Embodiment 2
[0034] A sulfur-burning sulphuric acid plant uses oxy-fuel combustion to produce SO 2 The gas is used to produce sulfuric acid, and its gas composition after combustion is: SO 2 —20.78%, O 2 —17.39%, N 2 —61.83%, total gas volume is about 115930Nm 3 / hr. Flue gas through SO 2 After the fan 1 is pressurized, it is heated to 390°C by the heat exchanger 2 and then enters the first inert catalyst conversion layer 31, the conversion rate is about 35%, the outlet temperature is 587°C and contains SO 2 The concentration is 14.28%; the heat exchange by the first waste heat utilization device 41 (produces medium pressure 2.5MPa saturated steam 15.56t / hr) is cooled to 420°C and then enters the second inert catalyst conversion layer 32. The total conversion rate of the reaction is about 65%. Outlet temperature is 585℃ and contains SO 2 The concentration is 7.95%; after the second waste heat utilization device 42 heat exchange (produces medium pressure 2.5MPa saturated steam 13.32t / hr), the ...
Embodiment 3
[0036] A copper smelter uses oxygen-rich smelting and blowing to produce SO 2 The gas is used to produce sulfuric acid, and its gas composition after combustion is: SO 2 —15.26%, O 2 —13.04%, N 2 -69.64%, CO 2 —2.06%, total gas volume is about 154800Nm 3 / hr. Flue gas through SO 2 After the blower 1 is pressurized, it is heated to 390℃ by the heat exchanger 2 and then enters the first inert catalyst conversion layer 31, the conversion rate is about 47%, the outlet temperature is 590℃ and contains SO 2 The concentration is 8.55%; after the heat exchange by the first waste heat utilization device 41 (production of medium pressure 2.5MPa saturated steam 17.46t / hr), the temperature is reduced to 390℃, and then it enters the first layer reaction of the traditional active catalyst layer 5. The total conversion rate of the reaction About 85%, the outlet temperature is 550℃ and contains SO 2 The concentration is 2.5%, the exhaust gas is cooled to 420℃ by the corresponding heat exchanger,...
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