Disclosed are a system (100) and a method (200) for being utilized in an industrial plant (10) for determining injection rate of at least one Flue Gas Conditioning Agent (FGCA) from a FGCA discharge unit (18) into a flue gas leading from a boiler (12) to be introduce into an Electrostatic Precipitator (ESP) (14) of an industrial plant (10). The system (100) and method (200) is capable of determining the optimal injection rate of the FGCA based on ESP (14) data to increase the efficiency of the ESP (14) for efficient collection of dust particles from the flue gas stream.

Disclosed are a system (100) and a method (200) for being utilized in an industrial plant (10) for determining injection rate of at least one Flue Gas Conditioning Agent (FGCA) from a FGCA discharge unit (18) into a flue gas leading from a boiler (12) to be introduce into an Electrostatic Precipitator (ESP) (14) of an industrial plant (10). The system (100) and method (200) is capable of determining the optimal injection rate of the FGCA based on ESP (14) data to increase the efficiency of the ESP (14) for efficient collection of dust particles from the flue gas stream.

The present invention relates in general to a process for removing mercury from a mercury-containing flue gas using dregs from a Kraft pulp mill green liquor clarifier. The dregs are washed with water to produce a particulate carbon slurry which is activated with hydrobromic acid and injected into a mercury-containing flue gas to oxidize and adsorb the mercury at temperatures less than about 900 F. A slurry of sodium hydroxide and calcium carbonate, optionally also obtained from Kraft mill waste, is injected into the hot flue gas to absorb and remove CO.sub.2, SO.sub.2, and SO.sub.3.

The present invention relates in general to a process for removing mercury from a mercury-containing flue gas using dregs from a Kraft pulp mill green liquor clarifier. The dregs are washed with water to produce a particulate carbon slurry which is activated with hydrobromic acid and injected into a mercury-containing flue gas to oxidize and adsorb the mercury at temperatures less than about 900 F. A slurry of sodium hydroxide and calcium carbonate, optionally also obtained from Kraft mill waste, is injected into the hot flue gas to absorb and remove CO.sub.2, SO.sub.2, and SO.sub.3.