The utility model relates to the technical field of desulfurization of combined washing towers, and discloses a combined washing
tower with a
tail gas desulfurization pre-absorption structure, which comprises a combined washing
tower and an absorption
tower arranged on the right side of the combined washing tower. According to the combined washing tower with the
tail gas desulfurization pre-absorption structure, the reverse spraying pre-absorption section is additionally arranged, so that the SO2
absorption efficiency can be improved, downward radial flow
flue gas and upward spraying under-rich amine liquid are subjected to variable flow state turbulent bubble type contact to form a gas-in-liquid SO2 absorption reaction, and after the
flue gas and spraying liquid are subjected to the variable flow state turbulent bubble type
contact reaction, the SO2
absorption efficiency is improved. The gas-liquid mixture downwards enters a lower absorption chamber of the organic amine desulfurization tower for gas-liquid separation, so that the pre-absorption operation is completed, the desulfurization efficiency can be effectively improved, the emission of SO2 in
tail gas is reduced, the risk of
environmental protection accidents is avoided, meanwhile, the
sulfur utilization rate is effectively improved, and better
economic benefits are generated; the problems that the desulfurization efficiency is low, and tail gas exceeds the standard seriously are solved.