Gas-liquid circulation flow reactor and method for treating odorous waste gas containing hydrocarbons
A loop reactor and reactor technology, applied in the direction of chemical instruments and methods, separation methods, and dispersed particle separation, can solve the problems of loop reactors that cannot realize functions, narrow gas volume application range, and decreased mass transfer efficiency, etc., and eliminate Liquid surface disturbance phenomenon, high absorption efficiency, space-saving effect
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Embodiment 1
[0033] The composition of the main odor pollutants in the exhaust gas emitted by the acidic water storage tank of an enterprise is shown in Table 1, and the pressure is normal pressure. The circular flow reactor of the present invention is used for desulfurization treatment. The circular cover plate in the purification device is a screen with an aperture of 2mm, which is located at the variable diameter part of the upper part of the inner cylinder. The sodium hydroxide aqueous solution is used as the absorption liquid, and a trace amount of manganese sulfate is added to the absorption liquid. The added amount of manganese element meter is 30 μg / g, and when the pH value of the solution drops to 9, fresh lye is added and replaced. The packed tower is filled with Dg50 plastic Pall rings, and the average exhaust gas volume space velocity is 1000h -1 , the concentrations of various components in the exhaust gas are shown in Table 1, in which the hydrogen sulfide and organic sulfide...
Embodiment 2
[0037] The concentration of hydrocarbon-containing waste gas produced by a sweetening device is 30% (v / v), and the pressure is 1 atm. It is processed by the loop reactor of the present invention, diesel oil is used as the absorbent, the distillation range is 200-360 ° C, and the temperature is 15-20 ° C. The oil product absorbent enters from the liquid inlet 12 of the loop reactor and is discharged from the liquid outlet 11, and the diesel oil flows continuously. The circular cover plate in the reactor is a screen with a pore size of 10 mm, which is located at the upper part of the inner cylinder at the variable diameter; the connection method between the inner cylinder and the base is figure 2 In the manner shown, after purification, the hydrocarbon waste gas concentration is reduced to 1% (v / v), and the hydrocarbon recovery rate can reach 96.7%.
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