Process for removing sulfur dioxide from flue gases by using seawater
A technology for sulfur dioxide and flue gas, which is applied to chemical instruments and methods, separation of dispersed particles, lighting and heating equipment, etc., can solve the problems of high construction and operation costs of packed absorption towers, short service life of ordinary polypropylene packings, height of packed towers and Large diameter and other problems, to achieve the effect of reducing the volume of the aeration tank, reducing the dilution ratio of fresh seawater, and reducing the aeration pressure
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[0025] As shown in the figure, after dust removal and heat exchange, the temperature is 110°C, SO 2 The content is 2500mg / m 3 The raw flue gas enters the desulfurization absorption tower with a diameter of 1.2m from the bottom, and is countercurrently absorbed by fresh seawater at a temperature of 30°C that enters the absorption tower from the cooling system of the generator set. The tower is filled with modified polypropylene structured packing with a height of 1.6m, and the amount of flue gas entering the tower is about 1.2×10 4 m 3 / h, sea water spray volume is 40.5m 3 / h (liquid-gas ratio is 3.4L / m 3 ) under the operating conditions, the desulfurization rate can reach 89.8%; maintain the amount of flue gas entering the tower and increase the amount of seawater spraying to 49.9m 3 / h (the liquid-gas ratio is 4.2L / m 3 ), the desulfurization rate can reach 99.0%. The amount of flue gas entering the tower is 1.0×10 4 m 3 / h, sea water spray volume is 19.8m 3 / h (liqui...
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