Method for treating non-ferrous metal smelting smoke acid-making tail gas by low-temperature catalytic oxidation cooperated with ultraviolet light
A low-temperature catalysis and oxidation treatment technology, applied in the environmental field, can solve the problems of high one-time investment and operation cost, complex process and large floor space, and achieve the effects of low cost, simple process and low energy consumption.
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Embodiment 1
[0015] Removal of SO from non-ferrous metal smelting flue gas acid production tail gas by ultraviolet light synergistic low-temperature catalytic oxidation 2 , NO x , the method of zero-valent Hg, specifically comprise the following steps: the oxygen that feeds in the tail gas of making acid, makes O in the tail gas 2 The volume percentage of the tail gas is 2% of the total tail gas. The tail gas is irradiated with ultraviolet lamps to ionize the oxygen molecules in the oxygen in the tail gas and recombine to generate strong oxidant ozone. Oxidation, solid phase catalytic oxidant layer bed is equipped with solid catalyst, the solid catalyst is made of Al 2 o 3 As the carrier, the active components are manganese and molybdenum, and the mass percentage of the active components in the catalyst is 4%; the temperature of the catalytic reaction bed is 100 °C, and this method is effective for SO in the tail gas 2 , NO x The oxidation efficiencies of zero-valent Hg were 85%, 87%, ...
Embodiment 2
[0017] Removal of SO from non-ferrous metal smelting flue gas acid production tail gas by ultraviolet light synergistic low-temperature catalytic oxidation 2 , NO x , the method of zero-valent Hg, specifically comprise the following steps: the oxygen that feeds in the tail gas of making acid, makes O in the tail gas 2 The volume percentage of the tail gas is 4% of the total tail gas. The tail gas is irradiated with an ultraviolet lamp to ionize the oxygen molecules in the oxygen in the tail gas and recombine to produce a strong oxidant ozone, and then the tail gas is oxidized through the solid-phase catalytic oxidant layer bed; the solid-phase The catalytic oxidant layer bed is equipped with a solid catalyst, which is made of Al 2 o 3 As the carrier, the active components are manganese and molybdenum, and the mass percentage of the active components in the catalyst is 8%; the temperature of the catalytic reaction bed is 250 °C, and this method can reduce 2 , NO x The oxida...
Embodiment 3
[0019] Removal of SO from non-ferrous metal smelting flue gas acid production tail gas by ultraviolet light synergistic low-temperature catalytic oxidation 2 , NO x , the method of zero-valent Hg, specifically comprise the following steps: the oxygen that feeds in the tail gas of making acid, makes O in the tail gas 2 The volume percentage of the tail gas is 6% of the total tail gas. The tail gas is irradiated with an ultraviolet lamp to ionize the oxygen molecules in the oxygen in the tail gas and recombine to produce a strong oxidant ozone. Oxidation, solid phase catalytic oxidant layer bed is equipped with solid catalyst, the solid catalyst is made of Al 2 o 3 As the carrier, the active components are manganese and molybdenum, and the mass percentage of the active components in the catalyst is 5%; the temperature of the catalytic reaction bed is 120 °C, and this method is effective for SO in the tail gas 2 , NO x The oxidation efficiencies of zero-valent Hg were 87%, 91...
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