Method of catalystless denitrification for fluidized bed incinerators

Claim 1

A method of catalystless denitrification for a fluidized bed incinerator, comprising the steps of: (a) forming a fluidized bed in the incinerator by fluidizing the substances to be incinerated and an incombustible fluidizing medium as the substances and the fluidizing medium are supplied to the fluidizing bed along with primary air, the primary air being blown into the fluidized bed by air diffuser tubes provided in the lower part of the incinerator, the air diffuser tubes extending generally parallel to each other; (b) burning the substances in the fluidized bed, the burning of the substances resulting in the generation of combustible pyrolysis gases; (c) forming a downward flow of the combination of the combustion residue of the substances to be incinerated and the fluidizing medium inside the fluidized bed through the air diffuser tubes, and discharging said combination from the bottom of said incinerator; (d) separating the fluidizing medium from the combustion residue in a sieve, and then recirculating the separated fluidizing medium to the fluidized bed; (e) combusting the combustible pyrolysis gases in the incinerator by blowing secondary air into a portion of the incinerator above the fluidized bed, the secondary air being blown into the portion of the incinerator from opposite sides of the incinerator along a plurality of parallel paths defining a lattice arrangement and from at least one upper stage and one lower stage in the incinerator; and, (f) performing denitrification of said combustible pyrolysis gas by mixing a gaseous denitrification agent with a portion of the secondary air which is introduced into the incinerator through said upper stage to react the agent with the nitrogen oxides present in the combustible pyrolysis gas within the incinerator.

Claim 2

A method of catalystless denitrification for a fluidized bed incinerator, comprising the steps of: (a) forming a fluidized bed in the incinerator by fluidizing the substances to be incinerated and an incombustible fluidizing medium as the substances and the fluidizing medium are supplied to the fluidizing bed along with primary air, the primary air being blown into the fluidized bed by air diffuser tubes provided in the lower part of the incinerator, the air diffuser tubes extending generally parallel to each other; (b) burning the substances in the fluidized bed, the burning of the substances resulting in the generation of combustible pyrolysis gases; (c) forming a downward flow of the combination of the combustion residue of the substances to be incinerated and the fluidizing medium inside the fluidized bed through the air diffuser tubes, and discharging said combination from the bottom of said incinerator; (d) separating the fluidizing medium from the combustion residue in a sieve, and then recirculating the separated fluidizing medium to the fluidized bed; (e) combusting the combustible pyrolysis gases in the incinerator by blowing secondary air into a portion of the incinerator above the fluidized bed, the secondary air being blown into the portion of the incinerator from opposite sides of the incinerator along a plurality of parallel paths defining a lattice arrangement and from at least one upper stage and one lower stage in the incinerator; and, (f) performing denitrification of said combustible pyrolysis gas by mixing a gaseous denitrification agent with a portion of the secondary air which is introduced into the incinerator through said upper stage to react the agent with the nitrogen oxides present in the combustible pyrolysis gas within the incinerator.