Abstract: The invention relates to a method for controlling a fume treatment center (FTC) (23), scrubbing the baking fumes from a rotary baking furnace (1), in which the fumes are drawn in through at least one suction manifold (11) of the baking furnace (1) and collected in a duct (20, 20?) that conveys said fumes to the fume treatment center (23). The fume treatment center includes a tower (24) which sprays water into the fumes in order to cool same and a least one reactor (25) for the physico-chemical neutralization of the fumes, comprising contact with a reagent powder, such as alumina, followed by filtering (36) of the loaded reagent and the fume dust and recycling in the reactor (25) of at least one fraction of the filtered reagent and mixing of the same with fresh reagent.

Abstract: The method of the invention is used for monitoring the state of a smoke duct connecting each suction rail of a baking furnace (FAC) for carbonated blocks, of the rotating fire type and preferably with open chambers or covered chambers, to a smoke processing center (CTF) for purifying the baking smoke from the FAC, wherein said smoke is drawn through at least one suction rail of the FAC and collected in the smoke duct feeding said smoke to the CTF, the method including at least the step of detecting a leak in the smoke duct consisting of parasitic inlets of ambient air into said duct and/or at least the step of detecting a fire in said duct.

Abstract: The invention relates to a method for controlling a fume treatment centre (FTC) (23), scrubbing the baking fumes from a rotary baking furnace (1), in which the fumes are drawn in through at least one suction manifold (11) of the baking furnace (1) and collected in a duct (20, 20?) that conveys said fumes to the fume treatment centre (23). The fume treatment centre includes a tower (24) which sprays water into the fumes in order to cool same and a least one reactor (25) for the physico-chemical neutralisation of the fumes, comprising contact with a reagent powder, such as alumina, followed by filtering (36) of the loaded reagent and the fume dust and recycling in the reactor (25) of at least one fraction of the filtered reagent and mixing of the same with fresh reagent.

Abstract: A group of at least two gas-flow reactors (21, 22, 2?2, . . . , 2n, 2?n) preferably with an ascending gas flow (3), are supplied in parallel with gas and with a chemical neutralization and/or sorption agent of the pulverulent material type capable of adsorbing effluents present in the gas flow by bringing the chemical neutralization and/or sorption agent in contact with the gas flow, the at least two reactors having elements (10) for collecting the chemical neutralization and/or sorption agent after contact with the gas flow. At least one of the two reactors has elements (11) for discharging the chemical neutralization and/or or sorption agent, after contact with the gas flow, these discharge elements being connected to the collecting elements, and members (7, 16) for injecting the chemical neutralization and/or sorption agent into at least one other of the at least two reactors.

Abstract: A group of at least two gas-flow reactors (21, 22, 2?2, . . . , 2n, 2?n) preferably with an ascending gas flow (3), are supplied in parallel with gas and with a chemical neutralization and/or sorption agent of the pulverulent material type capable of adsorbing effluents present in the gas flow by bringing the chemical neutralization and/or sorption agent in contact with the gas flow, the at least two reactors having elements (10) for collecting the chemical neutralization and/or sorption agent after contact with the gas flow. At least one of the two reactors has elements (11) for discharging the chemical neutralization and/or or sorption agent, after contact with the gas flow, these discharge elements being connected to the collecting elements, and members (7, 16) for injecting the chemical neutralization and/or sorption agent into at least one other of the at least two reactors.