A kind of reaction system and purification method for purifying VOCs in industrial waste gas
A reaction system and industrial waste gas technology, applied in chemical instruments and methods, separation methods, gas treatment, etc., can solve the problems of low VOCs removal efficiency, achieve good acid and alkali resistance, low percolation rate, and good thermal stability sexual effect
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Embodiment 1
[0044] Take the waste gas generated in the simulated industrial production process, the temperature of the waste gas is 125°C, and the concentration of dichloromethane in the waste gas is 20mg / m 3 . Add the prepared metal-organic framework material Fe@UIO-66 into the catalyst support device of the reaction tower, in which the mass percentage of Fe element is 5%, and its specific surface area is 1290m 2 / g. Prepare 0.5mol / L concentration of H at room temperature 2 o 2 solution, pH 6.4, H 2 o 2 The mass ratio of the solution to Fe@UIO-66 is 1000:1, and it is evenly sprayed into the above reaction system, and the gas-liquid ratio in the reaction tower is 6L / m 3 , the empty tower speed is controlled at 5000h -1 . After 30 minutes, the concentration changes of dichloromethane in the reaction solution and the exhaust gas outlet were detected respectively.
[0045] The removal rate of dichloromethane is 94%.
Embodiment 2
[0047] Take the waste gas produced in the simulated industrial process, the temperature of the waste gas is 65°C, and the concentration of toluene in the flue gas is 20mg / m 3 . Add the prepared metal-organic framework material Fe@UIO-66 into the catalyst support device of the reaction tower, in which the mass percentage of Fe element is 8%, and its specific surface area is 1020m 2 / g. Prepare 0.03mol / L concentration of H at room temperature 2 o 2 solution, pH 6.8, H 2 o 2 The mass ratio of the solution to Fe@UIO-66 is 800:1, and it is evenly sprayed into the above reaction system, and the gas-liquid ratio in the reaction tower is 16L / m 3 , the superficial velocity in the reaction process is controlled at 7000h -1 . After 30 minutes, the changes in the concentration of toluene in the reaction solution and the exhaust gas outlet were detected respectively.
[0048] The removal rate of toluene is 98%.
Embodiment 3
[0050] Take the waste gas produced in the simulated industrial process, the temperature of the waste gas is 65°C, and the concentration of toluene in the flue gas is 20mg / m 3 . Add the prepared metal organic framework material UIO-66 in the catalyst support device of the reaction tower, and its specific surface area is 1020m 2 / g. Prepare 0.03mol / L concentration of H at room temperature 2 o 2 solution, pH 6.8, H 2 o 2 The mass ratio of the solution to UIO-66 is 800:1, evenly sprayed into the above reaction system, the gas-liquid ratio in the reaction tower is 16L / m 3 , the superficial velocity in the reaction process is controlled at 7000h -1 . After 30 minutes, the changes in the concentration of toluene in the reaction solution and the exhaust gas outlet were detected respectively.
[0051] The removal rate of toluene is 82%.
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