Abstract: The temperature of the flue gas entering a spray dryer SO.sub.2 absorption chamber (26) is increased so as to maintain the temperature of the flue gas leaving the spray dryer SO.sub.2 absorption chamber (26) at a preselected temperature above the adiabatic saturation temperature of the flue gas so as to permit greater amounts of sulfur oxide absorbent slurry (36) to be sprayed into the flue gas, thereby allowing the treatment of flue gas containing high levels of sulfur oxide.

Abstract: A venturi-type rod scrubber for effecting the cleaning of the flue gas produced as a by-product of the combustion process that occurs during the course of the operation of fossil fuel firing steam generators, before the flue gas flows up the exhaust stack and is released to the atmosphere. The subject scrubber includes inlet means through which the flue gas enters the scrubber. A first spray system is suitably mounted in juxtaposed relation to the inlet means so as to be operative to introduce liquid into the stream of flue gas entering the scrubber through the inlet means. In alignment with but in spaced relation to the inlet means, the scrubber is provided with a throat region, i.e., a region of restricted cross-section. A plurality of spaced rows of parallel rods are suitably mounted within the throat region so as to extend substantially perpendicular to the path of flow of the flue gas flowing therethrough.

Abstract: A limestone flue gas scrubbing system includes a confining means which collects the effluent from the spray tower. A portion of this effluent is removed to a secondary reaction tank which operates at low pH for increased utilization of the additive. A first portion of the flow from the tank is passed to waste with the liquid portion returning to the main additive tank. A remaining portion of the slurry from the secondary tank is recirculated to the spray tower in parallel with the main slurry flow from the main reaction tank.